TECHNICAL REPORT

A National Inventory of Greenhouse Gas (GHG), Criteria Air Contaminant (CAC) and Hydrogen Sulphide (H2S) Emissions by the Upstream Oil and Gas Industry

Volume 5, Compendium of Terminology, Information Sources, Emission Factors, Equipment Sched’s and Uncertainty Data

September 2004

2005-0015

2100, 350 – 7th Ave. S.W. Calgary, Alberta

Canada T2P 3N9 Tel (403) 267-1100 Fax (403) 261-4622

905, 235 Water Street St. John’s, Newfoundland

Canada A1C 1B6 Tel (709) 724-4200 Fax (709) 724-4225

Email: communication@capp.ca Website: www.capp.ca

The Canadian Association of Petroleum Producers (CAPP) represents 150 companies that explore for, develop and produce natural gas, natural gas liquids, crude oil, oil sands, and elemental sulphur throughout Canada. CAPP member companies produce more than 98 per cent of Canada’s natural gas and crude oil. CAPP also has 125 associate members that provide a wide range of services that support the upstream crude oil and natural gas industry. Together, these members and associate members are an important part of a $75-billion-a-year national industry that affects the livelihoods of more than half a million Canadians.

Review by July 2010

Disclaimer

This publication was prepared for the Canadian Association of Petroleum Producers (CAPP) by Clearstone Engineering. While it is believed that the information contained herein is reliable under the conditions and subject to the limitations set out, CAPP and Clearstone Engineering do not guarantee its accuracy. The use of this report or any information contained will be at the user’s sole risk, regardless of any fault or negligence of Clearstone Engineering, CAPP or its co-funders.

Volume 5 – COMPENDIUM OF

TERMINOLOGY, INFORMATION SOURCES, EMISSION FACTORS, EQUIPMENT SCHED’S AND UNCERTAINTY DATA

A National Inventory of Greenhouse Gas (GHG), Criteria Air Contaminant (CAC) and Hydrogen Sulphide (H2S) Emissions by

the Upstream Oil and Gas Industry PREPARED BY:

Clearstone Engineering Ltd. 700, 900-6 Avenue S.W. Calgary, Alberta T2P 3K2 PREPARED FOR:

CAPP 2100, 350-7 Avenue S.W. Calgary, Alberta T2P 3N9 Attention: Rick Hyndman

September 2004

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TABLE OF CONTENTS 1.0 TERMINOLOGY 1

1.1 GENERAL TERMINOLOGY 1 1.1.1 Crude Oil Related 1 1.1.2 Natural Gas Related 4 1.1.3 Misc. 6

1.2 FACILITY TERMINOLOGY 8 1.2.1 Wells 8 1.2.2 Other Crude Oil Production and Processing Facilities 11

1.2.2.1 Crude Oil Batteries 11 1.2.2.2 Crude Oil Processing Facilities 12 1.2.2.3 Crude Oil Related Injection Facilities 12 1.2.2.4 Other Crude Oil Related Facilities 12

1.2.3 Other Natural Gas Production and Processing Facilities 13 1.2.3.1 Natural Gas Batteries 13 1.2.3.2 Natural Gas Gathering Systems 13 1.2.3.3 Natural Gas Processing Facilities 14 1.2.3.4 Natural Gas Related Injection Facilities 15 1.2.3.5 Other Natural Gas Production and Processing Related Facilities 16

1.2.4 Natural Gas Transmission, Storage and Distribution Facilities 16 1.2.5 Petroleum Liquids Transportation and Storage Facilities 18

1.3 EQUIPMENT TERMINOLOGY 18 1.4 EMISSIONS TERMINOLOGY 24

1.4.1 Emission Substances 24 1.4.2 Criteria Air Contaminants 25 1.4.3 Emission Sources 27 1.4.4 Emission Accounting 32 1.4.5 Other Emission Related Terminology 33

2.0 INFORMATION SOURCES 36 2.1 BRITISH COLUMBIA 36 2.2 ALBERTA 39 2.3 SASKATCHEWAN 45 2.4 REST OF CANADA 47

3.0 EMISSION FACTORS 50 4.0 EQUIPMENT SCHEDULES 201 5.0 UNCERTAINTY DATA 218

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LIST OF ACRONYMS

AGA - American Gas Association BSFC - brake-specific fuel consumption CAC - criteria air contaminant CAPP - Canadian Association of Petroleum Producers CCME - Canadian Council of Ministers of the Environment CGA - Canadian Gas Association CH4 methane CO2AO - carbon dioxide form atmospheric oxidation CO2E - carbon dioxide equivalent CSA - Canadian Standards Association EC - Environment Canada GHG - greenhouse gases GRI - Gas Research Institute GTC - Gas Technology Canada H2S hydrogen sulphide HEL - higher explosive limit HHV - high (or gross) heating value IPCC International Panel on Climate Change Kt kilotonnes LEL - lower explosive limit LHV - lower (or net) heating value N2O nitrous oxide NBS - National Bureau of Standards NMHC - non-methane hydrocarbon NPRI - National Pollutant Release Inventory PM - total suspended particulate matter PM2.5 - particulate matter ≤ 2.5 µm in aerodynamic diameter PM10 - particulate matter ≤ 10 µm in aerodynamic diameter POM - polycyclic organic matter ppm - parts per million SEPAC - Small Explorers and Producers Association of Canada THC - total hydrocarbons TOC - total organic compounds TNMOC - total non-methane organic compounds UOG - upstream oil and gas UNFCCC United Nations Framework Convention on Climate Change U.S. EPA - U.S. Environmental Protection Agency VCR - Voluntary Challenge and Registry VOC - volatile organic compound

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CONVERSIONS

USEFUL CONVERSION FACTORS

Physical Quantity

SI to English Conversion

English to SI Conversion

Length

1 m =3.2808 ft 1 km = 0.6213712 mi

1 ft = 0.3048 m 1 mi = 1.609344 km

Area

1 m2 = 10.7639 ft2

1 ft2 = 0.092903 m2

Volume

1 m3 = 35.3134 ft3 1 L = 0.2641720 U.S. gal

1 ft3 = 0.02837 m3 1 U.S. gal = 3.785412 L

Velocity

1 m/s = 3.2808 ft/s 1 km/h = 0.6213712 mph

1 ft/s = 0.3048 m/s 1 mph = 1.609344 km/h

Density

1 kg/m3 = 0.06243 lbm/ft3

1 lbm/ft3 = 16.018 kg/m3

Force

1 N = 0.2248 lbf

1 lbf = 4.4482 N

Mass

1 kg = 2.20462 lbm

1 lbm = 0.45359737 kg

Pressure

1 kPa = 0.145038 psi 1 kPa = 4.01474" WC

1 psi = 6.89476 kPa 1" WC = 0.249082 kPa

Energy

1 kJ = 0.94783 Btu

1 Btu = 1.05504 kJ

Power

1 W = 3.4121 Btu/h 1 kW = 1.3405 hp

1 Btu/h = 0.29307 W 1 hp = 0.746 kW

Heat Flux/Unit Area

1 W/m2 = 0.317 Btu/h·ft2

1 Btu/h·ft2 = 3.154 W/m2

Heat Flux/Unit Length

1 W/m = 1.0403 Btu/h·ft

1 Btu/h·ft = 0.9613 W/m

Heat Generation/Unit Volume

1 W/m3 = 0.096623 Btu/h·ft3

1 Btu/h·ft3 = 10.35 W/m3

Energy/Unit Mass

1 kJ/kg = 0.4299 Btu/lbm

1 Btu/lbm = 2.326 kJ/kg

Specific Heat

1 kJ/kgºC = 0.23884 Btu/lbmºF

1 Btu/lbm·ºF = 4.1869 kJ/kg·ºC

Thermal Conductivity

1 W/mºC = 0.5778 Btu/h·ftºF

1 Btu/h·ft·ºF = 1.7307 W/m·ºC

Convective Heat Transfer Coefficient

1 W/m2C = 0.1761 Btu/h·ft2·ººF

1 Btu/h·ft2·ºF = 5.6782 W/m2·ºC

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1.0 TERMINOLOGY This glossary is organized into four main categories of crude oil and natural gas related terms:

o General Terminology, o Facility Terminology, o Equipment Terminology, and o Emissions Terminology.

These four main categories are futher divided as required. The terms and their definitions presented below have been adapted from a wide variety of sources including publications of:

• the American Petroleum Institute, • United States Environmental Protection Agency, • Canadian Gas Association, • Alberta Environment, • Alberta Energy and Utilities Board, • oil and gas producers, and • equipment manufactures.

They are intended to assist in the general interpretation and understanding of emission estimates and activity data for the oil and gas industry as presented in this report. 1.1 GENERAL TERMINOLOGY 1.1.1 Crude Oil Related Crude Oil : a mixture of hydrocarbons that exist in the liquid phase in natural

underground reservoirs and remains liquid at atmospheric pressure and temperature after passing through surface separation facilities.

Petroleum : a term sometimes used as a substitute for crude oil and sometimes as a

collective term for natural gas and crude oil. Light/Medium Crude Oil: a category of crude oil characterized by relatively low viscosity, a lower

carbon-to-hydrogen ratio, and a relatively lower density - typically less than 900 kg/m3 (greater than 25º API).

Heavy Crude Oil : a category of crude oil characterized by relatively high viscosity, a higher

carbon-to-hydrogen ratio, and a relatively higher density - typically. 900 kg/m3 or more (25º or less API) Heavy crude oil typically is more difficult to extract with conventional recovery techniques and is more costly to refine.

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Bitumen : a naturally occurring viscous mixture consisting of hydrocarbons heavier than pentane and other contaminants, such as sulphur compounds, which in its natural state will not flow under reservoir conditions or on the surface. Bitumen occupies the lower end of the range of heavy crude oils and is sometimes referred to as ultra-heavy crude oil.

Bituminous Sands : an unconsolidated mixture of sand, clay, water and bitumen. Crude Bitumen : a term used by the Government of Alberta to designate any non-coal, non-

natural gas hydrocarbon produced from a designated oil sands area. Oil Sands : a term applied by the Government of Alberta to particular geographical

areas of the Province of Alberta wherein are located concentrations of bituminous sands but which also contain deposits of other heavy crude oil. Often used, in error, in casual conversation as a synonym for bituminous sands.

Oil Shale: a laminated, sedimentary rock that contains a solid, waxy hydrocarbon

called kerogen which is commingled with the rock structure. Shale oil is the hydrocarbon produced from the decomposition of the kerogen when oil shale is heated in an oxygen-free environment. Raw shale oil resembles a heavy, viscous, low-sulphur high-nitrogen crude oil but can be upgraded to produce a good-quality sweet crude oil.

Conventional Crude Oil : crude oil obtained via “conventional” recovery methods (i.e., normal

primary, secondary or tertiary processes) from a “conventional” source (i.e., not from bituminous sands, shales or carbonates) in a “conventional” location (i.e., not from the frontier, including the offshore).

Primary Recovery : the production of crude oil using natural resevoir pressure and/or a simple

downhole pump. Secondary Recovery : the production of crude oil using reservoir flooding with water or natural

gas. Tertiary Recovery : the production of crude oil using more sophisticated techniques such as

reservoir flooding with CO2 or lighter hydrocarbons such as ethane. Tertiary recovery also encompasses all thermal recovery techniques.

Enhanced

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Recovery : the production of crude oil using secondary and/or tertiary recovery techniques.

Cold Recovery : the production of crude oil which does not involve the use of any thermal

techniques. Thermal Recovery : the production of crude oil which involves the use of one or more thermal

techniques whereby heat is introduced into the crude oil reservoir or bituminous sands (oil sands) deposit to enhance the ability of the crude oil to flow and thereby facilitate its recovery.

In-Situ Recovery : recovery of bitumen (oil sands) from a reservoir using a series of wells.

This is in contrast to oil sands recovery by mining. Natural Gas Injection : an enhanced crude oil recovery technique in which natural gas is

compressed into a producing reservoir through an injection well to drive oil to the well bore and the surface.

Natural Gas Cycling : an enhanced petroleum recovery technique that takes produced natural gas

and condensate and injects it back into the reservoir to increase pressure and increase the production of natural gas liquids.

Petroleum Liquids : liquid hydrocarbons, that is crude oil, diluted bitumen, natural gas liquids,

condensate, etc. Diluent : light petroleum liquids used to dilute heavy crude oil, particularly

bitumen, so that it can flow more easily through pipelines. Condensate : hydrocarbon liquid separated from natural gas that condenses due to

changes in the temperature, pressure, or both, that remains liquid at standard reference conditions.

Pentanes Plus : a mixture of hydrocarbons, mostly pentanes and heavier, extracted from

natural gas. It includes natural gasoline, isopentane and gas plant condensate.

Gas Plant Condensate : a natural gas processing plant product, mostly pentanes and heavier,

recovered and separated as liquids at the gas inlet separators or scrubbers in natural gas processing plants or field facilities.

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Sour Crude Oil : crude oil containing free sulphur, hydrogen sulphide or other sulphur compounds

Synthetic Crude Oil : a mixture of hydrocarbons, similar to natural crude oil, derived by

upgrading heavy crude oil, particularly bitumen. Black Oil : a hydrocarbon (petroleum) liquid with an initial producing gas-to-oil ratio

(GOR) less than 0.31 cubic meters per liter and an API gravity less than 40 degrees.

Crude Oil Losses : the volume of crude oil (including lease condensate) reported by

petroleum refineries, pipelines and lease holders as being lost or unaccounted for in their operations. These losses are of a non-processing nature (i.e., losses due to spills, contamination, fires, etc.), as opposed to refinery processing losses or gains.

1.1.2 Natural Gas Related Natural Gas : a naturally occurring mixture of hydrocarbon and non-hydrocarbon

compounds existing in the gaseous phase or in solution with hydrocarbon liquids in geologic formations beneath the earth’s surface. The principal hydrocarbon constituent is methane.

Conventional Natural Gas : natural gas obtained via “conventional” recovery methods (i.e., normal

primary, secondary or tertiary processes) from a “conventional” source (i.e., not from coalbeds or tight reservoir formations) in a “conventional” location (i.e., not from the frontier, including the offshore).

Dissolved Natural Gas : natural gas that is in solution with crude oil in the reservoir at reservoir

conditions (temperature and pressure). Solution Natural Gas : natural gas that is in solution with produced crude oil. Associated Natural Gas : natural gas that is produced in conjunction with crude oil, including

bitumen. Casinghead Gas : dissolved natural gas and associated natural gas may be produced

concurrently from the same well bore. In such situations, it is not feasible to measure the production of dissolved gas and associated gas separately; therefore, production is reported as casinghead gas. Sometime it may simply be referred to as either associated gas or solution gas.

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Sweet Natural Gas : raw natural gas with a relatively low concentration of sulphur compounds,

such as hydrogen sulphide. Sour Natural Gas : raw natural gas that contains quantities of hydrogen sulphide (H2S),

carbon dioxide (CO2), and other sulphide-based compounds in sufficient quantities to pose a public safety hazard if released or to result in unacceptable off-lease odours if vented to the atmosphere.

Compressed Natural Gas (CNG) : natural gas compressed into high-pressure fuel cylinders to power a car or

truck. It comes from special CNG fuel stations. Dry Natural Gas : field natural gas that does not require any processing to meet contract

hydrocarbon dew point requirements. Wet Natural Gas -: field natural gas that needs to be processed to extract natural gas liquids in

order to meet contract hydrocarbon dew point requirements. Field Natural Gas : natural gas extracted from a production well prior to its entering the first

stage of processing, such as dehydration. Liquefied Natural Gas (LNG) : natural gas that has been refrigerated to –160ºC to condense it into a

liquid. The liquefaction process removes most of the water vapor, butane, propane, and other trace gases, that are usually included in ordinary natural gas. The resulting LNG is usually more than 98 percent pure methane.

Natural Gas Liquids (NGLs) : liquid hydrocarbons, such as ethane, propane, butane, pentane, natural

gasoline, and condensate that are extracted from field natural gas. Liquefied Petroleum Gas (LPG) : a natural gas mixture composed of mainly ethane, propane, and butanes,

with small amounts of pentanes plus (C5+) in any combination. The fluid is usually gaseous under standard reference conditions but becomes a liquid under pressure.

Non-Associated Natural Gas : natural gas that is produced from a predominantly natural gas pool (e.g.,

gas that is not associated with crude oil, including bitumen). Methane Content of Natural Gas - the volume of methane contained in a unit volume of natural gas at

standard temperature, 15°C, and pressure, 101.325 kPa.

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Residue Gas : natural gas from which gas plant products (natural gas liquids), and in some cases non-hydrocarbons, have been extracted in natural gas processing plants.

1.1.3 Misc. Reservoir : a porous and permeable underground formation containing an individual

and separate natural accumulation of producible hydrocarbons (oil and/or gas) which is confined by impermeable rock or water barriers and is characterized by a single natural pressure system. In most situations, reservoirs are classified as oil reservoirs or as gas reservoirs by a regulatory agency. In the absence of a regulatory authority, the classification is based on the natural occurrence of the hydrocarbons in the reservoir as determined by the operator.

Pool : is synonymous with the term reservoir; however, in certain situations, a

pool may consist of more than one reservoir. Field : an area consisting of a single reservoir or multiple reservoirs all grouped

on, or related to, the same individual geological structural feature and/or stratigraphic condition. There may be two or more reservoirs in a field that are separated vertically by intervening impervious strata, or laterally by local geologic barriers, or by both.

Well Drilling : the process of boring a hole from the surface to a potential producing zone

in an oil or gas reservoir. Diesel engines are typically used to power the drilling mechanism.

Well Testing : flow testing conducted to determine the deliverability of a well.

(Sometimes the test may be conducted into a flow or gathering line; however, more often the liquids are produced into temporary tankage brought on site for the test, and the gas phase is either vented or flared.)

Well Drill-Stem Test : when the target zone has been reached, a drill-stem test may be performed

to determine the production potential of the zone. This test occurs when the drilling rig is on the well. During a test, the zone is produced through the centre of the drill-stem. At the surface, the gas and liquid phases are separated and measured. If it is a sour well, the gas phase is flared; otherwise, the gas may be vented to the atmosphere.

Well Servicing (or Workover): work performed on a well after its initial completion to repair downhole

equipment or to increase production rates. Pumping Well : an oil well that requires a pump to bring the oil to the surface. Either a

pumpjack (polished rod pump) or a progressive cavity pump may be used.

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Blowdown Treatments : some natural gas wells must be blown down periodically to remove water

that has accumulated in the production tubing. These are primarily shallow (less than 1000 m deep), low-pressure (less than 2000 kPa) gas wells. Shallow gas wells are typically sweet and usually are not equipped with flares. Thus, the natural gas that is discharged during blowdown operations is vented to the atmosphere unburned.

Abandonment : the permanent dismantlement of a facility so that it is permanently

incapable of its original intended use. This includes leaving downhole or subsurface structures in a permanently safe and stable condition; the removal of associated equipment and structures; the removal of all produced liquids; and the removal and appropriate disposal of structural concrete.

Acid Gas : a gaseous mixture that is separated in the treating of solution or non-

associated natural gas and which typically contains hydrogen sulphide (H2S), total reduced sulphur compounds, and/or carbon dioxide (CO2).

API Gravity : the weight per unit volume of hydrocarbon liquids as measured by a

system recommended by the American Petroleum Institute (API). The measuring scale is calibrated in terms of degrees API. API Gravity is the industry standard for expressing the specific gravity of crude oils. A high API gravity means lower specific gravity and lighter oils.

Custody Transfer Point : the transfer of hydrocarbon liquids or natural gas: after processing and/or

treatment in the producing operations, or from storage vessels or automatic transfer facilities or other such equipment, including product loading racks, to pipelines or any other forms of transportation.

Emulsion : a combination of two immiscible liquids, that is, liquids that do not mix

together under normal conditions. Extraction Loss (or Shrinkage) : the reduction in volume of natural gas resulting from the removal of the

natural gas liquid constituents of natural gas at the processing plant. Gas-to-Oil Ratio (GOR) : the number of standard cubic meters of natural gas produced per liter of

crude oil or other hydrocarbon liquid. High Vapour Pressure Hydrocarbon : any hydrocarbon or stabilized hydrocarbon mixture with a Reid vapour

pressure greater than 14 kPa.

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Offshore : the geographic area which lies seaward of the coastline. In general, the

term “coastline” means the line of ordinary low water along that portion of the coast which is in direct contact with open sea or the line marking the seaward limit of inland water.

Operator : the entity appointed by venture stakeholders to take primary responsibility

for day-to-day operations and activities for a specific plant or activity. Pipeline Fuel : natural gas consumed in the operation of a natural gas pipeline, primarily

in compressors Produced Water - water that is extracted from the earth from a crude oil or natural gas

production well, or that is separated from crude oil, condensate, or natural gas after extraction.

Standard Reference Conditions : most equipment manufacturers reference flow, concentration and

equipment performance data at ISO standard conditions of 15°C, 101.325 kPa, sea level and 0.0 percent relative humidity.

Stock Tank Vapours :the small volume of dissolved gas present in the oil storage tanks that may

be released from the tanks. Suspension : the cessation of normal production, operation, or injection activities at a

facility. Total Petroleum Stocks : the volume of crude oil (including lease condensate), natural gas plant

liquids and petroleum products held by crude oil producers, storers of crude oil, companies transporting crude oil by water, crude oil pipeline companies, refining companies, product pipeline companies, and by bulk terminal companies. Included are domestic oil and foreign oil that have cleared customs for domestic consumption (i.e., foreign oil in-transit to the receiving country and foreign oils held in bonded storage, to include oils in the foreign trades zone, are excluded from these stock statistics). All stocks are reported on a custody basis, regardless of ownership of the oils.

1.2 FACILITY TERMINOLOGY 1.2.1 Wells Well : a hole drilled in the earth for the purpose of (1) finding or producing crude

oil or natural gas; or (2) providing services related to the production of crude oil or natural gas.

Abandoned Well : a well that has been drilled, abandoned, cut, and capped at surface.

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Blowout : the complete loss of control of the flow of fluids from a well to the

atmosphere or the flow of fluids from one underground reservoir to another (an underground blowout). Wellbore fluids are released uncontrolled at or near the wellbore. Well control can only be regained by installing or replacing equipment to shut in or kill the well or by drilling a relief well.

Cyclical Well : a crude bitumen well requiring steam to be injected to produce the

hydrocarbons. The steaming and producing are performed in alternating cycles.

Deep Natural Gas Well : a gas well greater than 1000 m deep. These wells are typically high

pressure and may be sweet or sour. Shallow Natural Gas Well : a gas well less than 1000 m deep. Shallow gas wells are typically found in

SE Alberta, NE Alberta and SW Saskatchewan and the gas is usually low pressure and sweet. In some cases shallow gas may only require dehydration prior to sales.

Development Well : a well drilled within the proved area of an oil or gas reservoir to the depth

of a stratigraphic horizon known to be productive. If the well is completed for production, it is classified as an oil or gas development well. If the well is not completed for production, it is classified as a dry development hole.

Disposal Well : a well used for the disposal of any oilfield or processing waste fluids or

produced water into a reservoir or aquifer. Dry Hole : an exploratory or development well found to be incapable of producing

either oil or gas in sufficient quantities to justify completion as an oil or gas well.

Farm Well : a well used to supply hydrocarbons or water to a farm for utility purposes. Flowing Well : a well capable of producing fluids to surface through natural reservoir

drive mechanisms, usually formation pressure. Gas Lift Well : a well producing fluids into the tubing/annulus with the assistance of

injected gas alone or in conjunction with mechanical equipment. Industrial Disposal Well : a well used for the disposal of processing wastes from a refinery or

chemical plant or brine from preparation or operation of a storage cavern.

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Injection Well : a well used primarily to inject fluids into a reservoir as part of an enhanced recovery, experimental, or pilot scheme.

Observation Well : a well used to monitor performance in an oil or gas reservoir, oil sands

deposit, or aquifer. Offshore Well : a well that is bottomed at, or produces from a point that lies seaward of the

coastline. Production Well : any hole drilled in the earth from which crude oil, condensate, or field

natural gas is extracted. Producing Well : a well producing hydrocarbons from a petroleum reservoir or a bituminous

[oil] sands deposit. Pumping Well : a well producing fluids with the assistance of mechanical equipment (e.g.,

pump jack or downhole pump) to lift fluids to the surface. Service Well : a well drilled or completed for the purpose of supporting production in an

existing field. Wells of this class are drilled for the following specific purposes:

• gas injection (natural gas, propane, butane or flue-gas), • water injection, • steam injection, • air injection, • salt water injection, • water supply for injection, • observation, • injection for in-situ combustion.

Shut-in Well : a well that has been completed but is not producing. A well may be shut-in

for tests, repairs, to await construction of gathering or flow lines, or better economic conditions.

Steam-Assisted Gravity Drainage (SAGD) Well : a well used to produce heavy oil, particularly bitumen, with the assistance

of thermal heating by steam. Storage Well : a well used to inject hydrocarbons into a storage reservoir or cavern. Suspended Well : a well in which production or injection operations have ceased for an

indefinite period of time. Wellhead : the equipment fitted to the top of a well casing to maintain surface control

of the well (i.e., outlets, valves, blowout preventers, etc). Sub-Sea

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Wellhead -: a wellhead installed on the sea floor and controlled remotely from a platform, a floating production facility or land.

1.2.2 Other Crude Oil Production and Processing Facilities 1.2.2.1 Crude Oil Batteries Crude Oil Battery : a system or arrangement of tanks or other surface equipment receiving

primarily oil or bitumen from one or more wells prior to delivery to market or other disposition. An oil battery may include equipment for measurement, for separating inlet streams into oil, gas, and/or water phases, for cleaning and treating the oil, for disposal of the water, and for conservation of the produced gas. A tank battery may or may not include a glycol dehydration unit and compressor

Crude Oil Single Battery : crude oil production facility for a single oil well or a single zone of a

multiple completion crude oil well. Crude Oil Group Battery : crud oil production facility consisting of two or more flow-lined oil wells

having individual separation and measurement equipment but with all equipment sharing a common surface location.

Crude Oil Satellite Battery : a small group of surface equipment (not including storage tanks) located

between a number of wells and the main crude oil battery that is intended to separate and measure the production from each well, after which the fluids are recombined and piped to the main crude oil battery for treating and storage or delivery.

Crude Oil Proration (or Fieldgate) Battery : a production facility consisting of two or more flow-lined oil wells having

common separation and measuring equipment. Total production is prorated to each well based on individual well tests. Individual well production tests can occur at the central site or at remote satellite facilities.

Crude Bitumen Single Battery : a production facility for a single heavy oil/crude bitumen well or a single

zone of a multiple completion heavy oil/crude bitumen well. Crude Bitumen

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Group Battery : a production facility consisting of two or more flow-lined heavy oil/crude bitumen wells having individual separation and measuring equipment but with all equipment sharing a common surface location.

Crude Bitumen Satellite Battery : a small group of surface equipment (not including storage tanks) located

between a number of wells and the main crude bitumen battery that is intended to separate and measure the production from each well, after which the fluids are recombined and piped to the main crude bitumen battery for treating and storage or delivery.

Crude Bitumen Proration (or Fieldgate) Battery : a production facility consisting of two or more flow-lined heavy oil/crude

bitumen wells having common separation and measuring equipment. Total production is prorated to each well based on individual well tests. Individual well production tests can occur at the central site or at remote satellite facilities.

1.2.2.2 Crude Oil Processing Facilities Central Crude Oil Treating Plant : battery system or arrangements of tanks or other surface equipment

without any directly associated wells. Custom Treating Plant : system or arrangement of tanks and other surface equipment receiving

crude oil/water emulsion exclusively by truck for separation prior to delivery to market or other disposition.

1.2.2.3 Crude Oil Related Injection Facilities Injection Facility : facility constructed and operated for the purpose of moving (waste)

product(s) into a petroleum reservoir. Waste Water Injection Facility : facility constructed and operated for the purpose of moving waste

produced water (brine) into a petroleum reservoir. 1.2.2.4 Other Crude Oil Related Facilities Offshore Production Platform : platform from which development wells are drilled and that carries all the

associated processing plants and other equipment needed to maintain a field in production

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1.2.3 Other Natural Gas Production and Processing Facilities 1.2.3.1 Natural Gas Batteries Natural Gas Battery : a system or arrangement of surface equipment that receives primarily gas

from one or more wells prior to delivery to a gas gathering system, to market, or to other disposition. Gas batteries may include equipment for measurement and for separating inlet streams into gas, hydrocarbon liquid, and/or water phases. There are many occurrences of gas battery codes being assigned for the purpose of being a proration hub. In these instances there is no equipment onsite except a meter.

Natural Gas Single Battery : a production facility for a single gas well where production is measured at

the wellhead. Production is delivered directly and is not combined with production from other wells prior to delivery to a gas plant, gas gathering system, or other disposition.

Natural Gas Group Battery : a production facility consisting of two or more flow-lined natural gas

wells having individual separation and measurement equipment but with all equipment sharing a common surface location.

Natural Gas Satellite Battery : a small group of surface equipment (not including storage tanks) located

between a number of wells and the main natural gas battery that is intended to separate and measure the production from each well, after which the production is recombined and piped to the main natural gas battery for treating and storage or delivery.

Natural Gas Proration (or Fieldgate) Battery : a production facility consisting of two or more flow-lined natural gas

wells having common separation and measuring equipment. Total production is prorated to each well based on individual well tests. Individual well production tests can occur at the central site or at remote satellite facilities.

Natural Gas Test Battery : a production facility for a natural gas well testing gas production prior to

commencement of regular production. 1.2.3.2 Natural Gas Gathering Systems NaturalGas

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Gathering System : a facility consisting of gas lines used to move products from one facility to another. The facility may also include compressors and/or line heaters.

Compressor Station : service equipment intended to maintain or increase the flowing pressure of

the gas that it receives from a well, battery, or gathering system prior to delivery to market or other disposition.

Meter Station : a facility whose purpose is to measure the volume of gas passing through a

pipeline. Orifice meters are used in most cases but turbine, vortex shedding and ultrasonic meters are also used.

Regulation Station : a facility whose purpose is to regulate the pressure of gas passing through

a pipeline to a set level. Emergency Shutdown (ESD) Valve Station :a valve installed on a pipeline, which will automatically close when the

line pressure drops below critical a predetermined value. There purpose is to minimize the amount of gas released in the event of a line break. ESD valve stations are most commonly used on sour natural gas gathering systems.

Field Facility : an installation designed for one or more specific limited functions. Such

facilities usually process natural gas produced from more than one lease for the purpose of recovering condensate from the stream of natural gas; however, some field facilities are designed to recover propane, butane, natural gasoline, etc., and to control the quality of the natural gas to be marketed. Field facilities include compressors, dehydration units, field extraction units, scrubbers, drip points, conventional single or multiple stage separation units, low temperature separators, and other types of separation and recovery equipment.

Field Dehydrator : a dehydration unit located upstream of a natural gas processing plant or

natural gas battery to control hydrates rather than provide any final treatment to meet sales specifications.

Lease Separator : facility located at the surface for the purpose of separating casinghead gas

from produced crude oil and water at the temperature and pressure conditions of the separator.

1.2.3.3 Natural Gas Processing Facilities Natural Gas Processing Plant : natural gas processing facility for extracting from natural gas helium,

ethane, or natural gas liquids, and/or the fractionation of mixed NGL to natural gas products. A natural gas processing plant may also include

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natural gas purification processes for upgrading the quality of the natural gas to be marketed to meet contract specifications (i.e., for removing contaminants such as water, H2S, CO2, and possibly adjusting the heating value by the addition or removal of nitrogen). The inlet natural gas may or may not have been processed through lease separators and field facilities.

Gas Plant - Acid Gas Injection : a gas processing plant in which the acid gas (CO2 and H2S) extracted from

the raw inlet gas is injected underground into an appropriate reservoir. Gas Plant - Acid Gas Flaring : a gas processing plant in which the acid gas (CO2 and H2S) extracted from

the raw inlet gas contains sufficiently small quantities of sulphur that it can meet provincial sulphur emission and air quality requirements by simply flaring the acid gas. Supplemental fuel is typically required to ensure stable operation of the acid gas flare.

Gas Plant - Sulphur Recovery : a gas processing plant elemental sulphur is extracted from the acid gas

(CO2 and H2S) prior to incineration. Gas Plant - Straddle : a gas processing plant located on or near a gas transmission line that

removes residual natural gas liquids from the gas and returns the residue gas to the line.

Gas Plant - Sweet : a gas processing plant which processes natural gas containing less than

0.01 mole/kmole of H2S. 1.2.3.4 Natural Gas Related Injection Facilities Injection Facility : facility constructed and operated for the purpose of moving (waste)

product(s) into a petroleum reservoir or other porous and permeable geologic formation.

Acid Gas Injection Facility : facility constructed and operated for the purpose of moving acid gas (a

mixture containing hydrogen sulphide (H2S), total reduced sulphur compounds, and/or carbon dioxide (CO2) that is separated in the treating of solution or non-associated natural gas) into a petroleum reservoir or other porous and permeable geologic formation.

Waste Water Injection Facility : facility constructed and operated for the purpose of moving waste

produced water (brine) into a petroleum reservoir.

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1.2.3.5 Other Natural Gas Production and Processing Related Facilities Offshore Production Platform : platform from which development wells are drilled and that carries all the

associated processing plants and other equipment needed to maintain a field in production

1.2.4 Natural Gas Transmission, Storage and Distribution Facilities Block Valve Station : a block valve used to isolate a segment of the main pipeline for tie-in or

maintenance purposes. On gas transmission systems, block valves are typically located at distances of 25 to 80 km along each line to limit the amount of piping that may need to be depressurized for tie-ins and maintenance, and to reduce the amount of gas that would be lost in the event of a line break.

Booster Station : a facility where gas pressure is increased to overcome friction losses

through a pipeline. Centrifugal or axial-flow compressors are most commonly used in these applications. A station typically comprises several units in series or parallel, as well as the necessary suction and discharge piping. Many booster stations also have discharge coolers to reduce the viscosity of the compressed gas and thereby increase the efficiency of gas transmission.

Compressor Station : a facility where gas pressure is increased to allow the gas to enter into a

higher pressure pipeline system (i.e., feed rather than booster service). Both centrifugal and reciprocating compressor units may be used in these applications. However, use of reciprocating compressors is most common. A station typically comprises several units in series or parallel, as well as the necessary suction and discharge piping. Many compressors also have discharge coolers to reduce the viscosity of the compressed gas and thereby increase the efficiency of gas transmission.

Control Valve Station : a modulating valve that controls either the flow rate or pressure through

the pipeline. In the latter case, this facility is often referred to as a regulator station. Usually, high-pressure gas from the pipeline is used as the supply medium needed to energize the valve actuator.

Transmission Station : station associated with a natural gas transmission pipeline that handle

unodourized gas and which meters and/or regulate the gas pressure. It

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may be a Receipt/Sales Station, Border Meter Station or Transmission Farm Tap.

Receipt Meter Station : a meter station for measuring the amount of gas being supplied by a given

source (e.g., gas processing plant or a gas battery) to a natural gas transmission system.

Border Meter Station : a meter station where custody of the natural gas is transferred from one

gas transmission system to another at a provincial or national boundary. These stations are usually larger than normal meter stations. Typically, they have 10 to 20 large diameter meter runs (16 to 20 NPS lines) and no pressure regulation.

Sales Meter Station : a meter station for measuring the amount of natural gas being withdrawn

from a gas transmission system by a customer (e.g., gas distribution system, farm or industrial end user). It might include pressure-regulating equipment.

Storage : most transmission systems incorporate the use of storage caverns or

spheres to help balance daily and seasonal variations in loads, and, therefore, are able to operate at nearly full capacity much of the time.

Transmission Farm Tap : direct gas sales from a transmission pipeline to an individual customer,

usually in rural areas where access to gas distribution system is not available. These facilities usually have only pressure regulating equipment (gas might be provided free of charge as a consideration for an easement, or the meter is located by the residence as part of the customer meter set).

Transmission Pipeline : a pipeline used to transport processed, unodourized natural gas to market

(i.e., to gas distribution systems and major industrial customers). Most transmission pipelines also have some farm taps that provide gas to farmers located along the pipeline in areas where service from distribution systems is not readily available.

The pipelines are usually constructed of steel, although aluminum is used for some lower pressure applications (generally up to 3450 kPa or 500 psig). The pipe sizes range from 60.3 mm to 1219.2 mm O.D. (2 to 48 NPS), with the mid-range sizes most common. The operating pressures typically range from 1380 to over 6900 kPag (200 to 1000+ psig).

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1.2.5 Petroleum Liquids Transportation and Storage Facilities Tank Farm : system or arrangement of tanks or other surface equipment associated with

the operation of a pipeline that may include measurement equipment and line heaters, but does not include separation equipment or storage vessels at a battery.

Terminal : plant and equipment designed to process crude oil or gas to remove

impurities and water. Pipeline Terminal : system or arrangement of tanks and other surface equipment principally

for receiving oil from, and transferring oil to, pipelines. The terminal may also feature facilities for blending petroleum liquids, and loading and unloading facilities for tank trucks and/or tank rail cars.

Truck Terminal : system or arrangement of tanks and other surface equipment receiving

crude oil by truck for the purpose of delivering crude oil into a pipeline. Marine Terminal : system or arrangement of tanks and other surface equipment for receiving

oil from, or transferring oil to, marine tankers. Petroleum Bulk Terminals : system or arrangement of tanks and other surface equipment operated by

refining, pipeline, and bulk terminal companies which (1) receive their principal products by tankers, barges, or pipelines, or (2) have a total combined capacity of 8 000 m3 (50,000 barrels) or more, regardless of the transportation means by which products are received.

High Vapour Pressure Pipeline : pipeline system transporting hydrocarbon mixtures in the liquid or quasi-

liquid state with a vapour pressure greater than 110 kPa absolute at 38ºC. Some examples of these hydrocarbons are liquid ethane, ethylene, propane, butanes, and pentanes.

Pumping Station : system or arrangement of tanks and other surface equipment located at

intervals along a main pipeline to maintain flow to the terminal point. 1.3 EQUIPMENT TERMINOLOGY Ancillary Equipment : any of the following pieces of equipment: pumps, pressure relief devices,

sampling connection systems, open-ended valves, or lines, valves, flanges, or other connectors.

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Boiler : an enclosed device using controlled flame combustion and having the primary purpose of recovering and exporting thermal energy in the form of steam or hot water.

Centrifugal Compressor Seal Systems : Centrifugal compressors generally require shaft-end seals between the

compressor and bearing housings. Either face-contact oil-lubricated mechanical seals or oil-ring shaft seals, or dry-gas shaft seals are used. The amount of leakage from a given seal will tend to increase with wear between the seal and compressor shaft, operating pressure and rotational speed of the shaft.

Closed-Vent System : a system that is not open to the atmosphere and is composed of piping,

ductwork, connections, and if necessary, flow inducing devices that transport gas or vapour from an emission point to one or more control devices.

Combustion Device : an individual unit of equipment, such as a flare, incinerator, process heater,

or boiler, used for the combustion of organic emissions. Connectors : any flanged or threaded connection, or mechanical coupling, but excluding

all welded or back-welded connections. If properly installed and maintained, a connector can provide essentially leak-free service for extended periods of time. However, there are many factors that can cause leakage problems to arise. Some of the common causes include vibration, thermal stress and cycles, dirty or damaged contact surfaces, incorrect sealing material, improper tightening, misalignment, and external abuse.

Control Device : any equipment used for recovering or oxidizing waste natural gas or VOC

vapours. Such equipment includes, but is not limited to, absorbers, carbon adsorbers, condensers, incinerators, flares, boilers, and process heaters.

Cover : a device that is placed on top of, or over, a material such that the entire

surface area of the material is enclosed and sealed. A cover may have openings (such as access hatches, sampling ports, and gauge wells) if those openings are necessary for operation, inspection, maintenance, or repair of the unit on which the cover is installed, provided that each opening is closed and sealed when the opening is not in use. In addition, a cover may have one or more safety devices. Examples of a cover include, but are not limited to, a fixed-roof installed on a tank, an external floating roof installed on a tank, and a lid installed on a drum or other container.

Vent and Flare

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Systems : venting and flaring are common methods of disposing of waste gas volumes at oil and gas facilities. The stacks are designed to provide safe atmospheric dispersion of the effluent. Flares are normally used where the waste gas contains odorous or toxic components (e.g., hydrogen sulphide). Otherwise the gas is usually vented. Typically, separate flare/vent systems are used for high- and low-pressure waste gas streams.

Incinerator : an enclosed combustion device that is used for destroying organic

compounds. Auxiliary fuel may be used to heat waste gas to combustion temperatures. An energy recovery section is not physically formed into one manufactured or assembled unit with the combustion section; rather, the energy recovery section is a separate section following the combustion section and the two are joined by ducts or connections carrying flue gas. The above energy recovery section limitation does not apply to an energy recovery section used solely to preheat the incoming vent stream or combustion air.

Line Heater : an indirectly fired heater used to heat the fluid in the pipeline to above

hydrate or freezing temperatures. Direct-Fired Heater : the combustion gases occupy most of the heater volume and heat the

process stream contained in pipes arranged in front of refractory walls (the radiant section) and in a bundle in the upper portion (the convective section). Convective heaters are a special application in which there is only a convective section.

Flare : an open flame used for routine or emergency disposal of waste gas. There

are a variety of different types of flares including: flare pits, flare stacks, enclosed flares and ground flares.

Fixed Roof : a cover that is mounted on a storage vessel in a stationary manner and that

does not move with fluctuations in liquid level. Flow Indicator : a device that indicates whether gas flow is present in a line or whether the

valve position would allow gas flow to be present in a line. Fire-Tube Heaters : the combustion gases are contained in a fire-tube that is surrounded by a

liquid that fills the heater shell. This liquid may be either the process stream or a heat medium that surrounds the coil bundle containing the process stream. Common applications are indirect-fired water-bath heaters (line heaters) and glycol reboilers.

Gas-Condensate- Glycol (GCG) Separator : a two- or three-phase separator through which the ‘‘rich’’ glycol stream of

a glycol dehydration unit is passed to remove entrained gas and

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hydrocarbon liquid. The GCG separator is commonly referred to as a flash separator or flash tank.

Glycol Dehydration Unit : a device in which a liquid glycol including, but not limited to, ethylene

glycol, diethylene glycol, or triethylene glycol absorbent directly contacts a natural gas stream and absorbs water in a contact tower or absorption column (absorber). The glycol contacts and absorbs water vapour and other gas stream constituents from the natural gas and becomes ‘‘rich’’ glycol. This glycol is then regenerated in the glycol dehydration unit reboiler. The ‘‘lean’’ glycol is then recycled.

Glycol Dehydration Unit Reboiler Vent : the vent through which exhaust from the reboiler of a glycol dehydration

unit passes from the reboiler to the atmosphere or to a control device. Integral Compressor : a reciprocating compressor that shares a common crankshaft and

crankcase with the engine. Open-Ended Valves and Lines : any valve that may release process fluids directly to the atmosphere in the

event of leakage past the valve seat. The leakage may result from improper seating due to an obstruction or sludge accumulation, or because of a damaged or worn seat. An open-ended line is any segment of pipe that may be attached to such a valve and that opens to the atmosphere at the other end.

Few open-ended valves and lines are designed into process systems. However, actual numbers can be quite significant at some sites due to poor operating practices and various process modifications that may occur over time.

Some common examples of instances where this type of source may occur are listed below:

• scrubber, compressor-unit, station and mainline blowdown valves, • supply-gas valve for a gas-operated engine starter (i.e., where

natural gas is the supply medium), • instrument block valves where the instrument has been removed for

repair or other reasons, and • purge or sampling points.

Pressure-Relief or Safety Valves : these are used to protect process piping and vessels from being

accidentally over-pressured. They are spring loaded so that they are fully closed when the upstream pressure is below the set point, and only open

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when the set point is exceeded. Relief valves open in proportion to the amount of overpressure to provide modulated venting. Safety valves pop to a full-open positions on activation.

When relief or safety valves reseat after having been activated, they often leak because the original tight seat is not regained either due to damage of the seating surface or a build-up of foreign material on the seat plug. As a result, they are often responsible for fugitive emissions. Another problem develops if the operating pressure is too close to the set pressure, causing the valve to "simmer" or "pop" at the set pressure.

Gas that leaks from a pressure-relief valve may be detected at the end of the vent pipe (or horn). Additionally, there normally is a monitoring port located on the bottom of the horn near the valve.

Process Heater : an enclosed device using a controlled flame, the primary purpose of which

is to transfer heat to a process fluid or process material that is not a fluid, or to a heat transfer material for use in a process (rather than for steam generation).

Process Vessel : a heater, dehydrator, separator, treater, or any vessel used in the

processing or treatment of produced gas or oil. Pump Seals : positive displacement pumps are normally used for pumping hydrocarbon

liquids at oil and gas facilities. Positive displacement pumps have a reciprocating piston, diaphragm or plunger, or else a rotary screw or gear.

Packing, with or without a sealant, is the simplest means of controlling leakage around the pump shaft. It may be used on both the rotating and reciprocating pumps. Specially designed packing materials are available for different types of service. The selected material is placed in a stuffing box and the packing gland is tightened to compress the packing around the shaft. All packings leak and generally require frequent gland tightening and periodic packing replacement.

Particulate contamination, overheating, seal wear, sliding seal leakage and vibration will contribute to increased leakage rates over time.

Reciprocating Compressor : a piece of equipment that increases the pressure of a process gas by

positive displacement, employing linear movement of the drive shaft. Reciprocating Compressor Packing Systems : are used on reciprocating compressors to control leakage around the piston

rod on each cylinder. Conventional packing systems have always been prone to leaking a certain amount, even under the best of conditions.

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According to one manufacturer, leakage from within the cylinder or through any of the various vents will be on the order of 1.7 to 3.4 m3/h under normal conditions and for most gases. However, these rates may increase rapidly as normal wear and degradation of the system occurs.

Relief Device : a device used only to release an unplanned, non-routine discharge in order

to avoid safety hazards or equipment damage. A relief device discharge can result from an operator error, a malfunction such as a power failure or equipment failure, or other unexpected cause that requires immediate venting of gas from process equipment in order to avoid safety hazards or equipment damage.

Safety Device : a device that meets both of the following conditions: it is not used for

planned or routine venting of liquids, gases, or fumes from the unit or equipment on which the device is installed; and it remains in a closed, sealed position at all times except when an unplanned event requires that the device open for the purpose of preventing physical damage or permanent deformation of the unit or equipment on which the device is installed in accordance with good engineering and safety practices for handling flammable, combustible, explosive, or other hazardous materials. Examples of unplanned events which may require a safety device to open include failure of an essential equipment component or a sudden power outage.

Storage Vessel : a tank or other vessel that is designed to contain an accumulation of crude

oil, condensate, intermediate hydrocarbon liquids, or produced water and that is constructed primarily of non-earthen materials (e.g., wood, concrete, steel, plastic) that provide structural support.

Storage Vessel with the Potential for Flash Emissions : any storage vessel that receives hydrocarbon liquids containing dissolved

natural gas that will evolve from solution when the fluid pressure is reduced.

Tank : a device designed to contain materials produced, generated, and used by

the petroleum industry that is constructed of impervious materials, such as concrete, plastic, fibreglass-reinforced plastic, or steel that provide structural support.

Turnaround : a scheduled large-scale maintenance activity wherein an entire process

unit is taken offstream for an extended period for comprehensive revamp and renewal.

Valve : a device for controlling the flow of a fluid. There are three main locations

on a typical valve where leakage may occur: (1) from the valve body and around the valve stem, (2) around the end connections, or (3) past the

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valve seat. Leaks of the first type are referred to as valve leaks. Emissions from the end connections are classified as connector leaks. Leakage past the valve seat is only a potential source of emissions if the valve, or any downstream piping, is open to the atmosphere. This is referred to as an open-ended valve or line.

The potential leak points on each of the different types of valves are, as applicable, around the valve stem, body seals (e.g., where the bonnet bolts to the valve body, retainer connections), body fittings (e.g., grease nipples, bleed ports), packing guide, and any monitoring ports on the stem packing system. Typically, the valve-stem packing is the most likely of these parts to leak.

The different valve types include gate, globe, butterfly, ball and plug. The first two types are a rising-stem design, and the rest are quarter-turn valves. Valves may either be equipped with a hand-wheel or lever for manual operations, or an actuator or motor for automated operation

1.4 EMISSIONS TERMINOLOGY 1.4.1 Emission Substances Greenhouse Gases : substances involved in climate change. The most important greenhouse

gases are: carbon dioxide (CO2), methane (CH4) and nitrous oxide (N2O). Vented Emissions : emissions to the atmosphere by design or operational practice. They may

occur on either a continuous or intermittent basis. The most common causes or sources of venting are gas operated devices that use natural gas as the supply medium (e.g., compressor start motors, chemical injection and odourization pumps, instrument control loops, valve actuators, and some types of glycol circulation pumps), equipment blowdowns and purging activities, and venting of still-column off-gas by glycol dehydrators.

Fugitive Emissions : the UNFCCC definition is the sum of emissions from accidental

discharges, equipment leaks, filling losses, flaring, pipeline leaks, storage losses, venting, flaring, and all other direct emissions except those from fuel use. For the purposes of this inventory fugitive emissions have been defined as a sub-set of these.

Specifically, unintended releases of GHGs to the atmosphere. This category includes fugitive equipment leaks and accidents and equipment failures. Fugitive equipment leaks are emissions from equipment components that leak as a result of wear, poor design or improper installation. The primary emission sources include but are not limited to:

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threaded and flanged connections, valve stem packing leaks, leakage past valve seats to the atmosphere, compressor seals, pump seals, pressure regulator vents and sampling ports. Accidents and equipment failures include: spills, pipeline ruptures, gas migration and surface casing vent flows.

1.4.2 Criteria Air Contaminants Nitrogen Oxides (NOx) : the total of all forms of oxidized nitrogen at a given measurement point.

The primary form of NOx emitted by combustion devices is NO2; however, other forms may include NO, N2O, NO3, N2O4 and N2O5. Convention is to express total NOx in terms of equivalent NO2.

There are three mechanisms for formation of NOx in combustion processes: thermal fixation of nitrogen from the combustion air (thermal NOx), oxidation of fuel-bound nitrogen compounds (chemical NOx), and the formation of CN compounds in the flame zone which subsequently react to form NO (prompt NOx). Thermal NOx is the predominant form of NOX produced from natural gas combustion. The conditions that govern the formation of thermal NOx are the peak temperature, residence time at the peak temperature and the availability of oxygen while that temperature exists. Fuel-bound nitrogen is an important source of NOx where appreciable amounts of such fuels are used. The extent of conversion of fuel-bound nitrogen to NO is nearly independent of the parent fuel molecule, but is strongly dependent on the local combustion environment and on the initial amount of fuel-bound nitrogen. Prompt NOx is associated with the combustion of hydrocarbons. The maximum formation of prompt NOx is reached on the fuel-rich side of stiochiometric, it remains high through a fuel-rich region, and then drops off sharply when the fuel-air ratio is about 1.4 times the value at stiochiometric. NOx controls can be classified into types: post combustion methods and combustion control techniques. Post combustion methods address NOx emissions after formation while combustion control techniques prevent the formation of NOx during the combustion process. Post combustion methods tend to be more expensive than combustion control techniques. Post combustion control methods include selective non-catalytic reduction, and selective catalytic reduction. Combustion control techniques depend on the type of combustion device and fuel. Nonetheless, they generally are designed to achieve lower

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combustion temperatures without significantly affecting combustion efficiency and power output, and to avoid/minimize the use of nitrogen containing fuels.

Particulate Matter (PM) : Particulate matter is that portion of the flue gas which exists as a solid or

liquid droplet when it leaves the stack and cools to ambient conditions. Carbonaceous particulate that forms from gas-phase processes is generally referred to as soot, and that developed from pyrolysis of liquid hydrocarbon fuels is referred to as coke or cenospheres.

The potential for particulate emissions is generally dependent on the composition of the fuel and the type of combustion device. Combustion of natural gas produces very small amounts of particulate emissions compared to other types of fuels. Nonetheless, the amount of particulate emissions will tend to increase with the molecular weight of the gas. Also, reciprocating engines produce the most particulate matter while heaters and boilers produce the least. Most of the particulate matter emitted by reciprocating engines is reportedly due to lubricating oil leakage past the piston rings. Particulate emissions generally are classified as PM, PM10, PM2.5 and PM1 according to the maximum diameter of the material, namely, total PM, and PM with a diameter less than 10, 2.5 and 1 microns, respectively. PM10 and smaller particulate matter are of greatest concern because of their ability to bypass the body’s natural filtering system.

Products of Incomplete Combustion : These are any compounds, excluding CO2, H2O, SO2, HCl and HF, that

contain C, H, S, Cl or F and occur in the flue gas stream. These compounds may result from thermodynamic, kinetic or transport limitations in the various combustion zones. All input combustibles are potential products of incomplete combustion. Intermediate substances formed by dissociation and recombination effects may also occur as products of incomplete combustion (CO is often the most abundant combustible formed).

Reduced Sulphur Compounds (RSCs) : Any compounds containing the sulphur atom in its reduced oxidation

state. These are taken to be any sulphur-containing compounds except SOx.

Sulphur Oxides (SOx) : Usually almost all sulphur input to a combustion process as part of the fuel

or waste materials being burned is converted to SOx. Only a few percent of the available sulphur is emitted as sulphate particulate and other products

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of incomplete combustion. The produced SOx is comprised mostly of SO2 (typically 95 percent) with the rest being SO3. For simplification purposes it is assumed throughout this document that all input sulphur is converted to SO2.

Total Hydrocarbons : All compounds containing at least one hydrogen atom and one carbon

atom, with the exception of carbonates and bicarbonates. Total Organic Compounds (TOC) : TOC comprises all VOCs plus all non-reactive organic compounds (i.e.,

methane, ethane, methylene chloride, methyl chloroform, many fluorocarbons, and certain classes of per fluorocarbons).

Total Reduced Sulphur (TRS) : The aggregate concentration of all reduced sulphur compounds. Volatile Organic Compounds (VOC) : Any compound of carbon, excluding carbon monoxide, and carbon

dioxide, which participates in atmospheric chemical reactions. This excludes methane, ethane, methylene chloride, methyl chloroform, acetone, many fluorocarbons, and certain classes of per fluorocarbons.

1.4.3 Emission Sources Fuel Combustion : accounts for emissions from the consumption of all types of fuel typically

encountered at oil and gas facilities (i.e., natural gas, propane and diesel) in both internal (reciprocating engines and gas turbines) and external (heater and boilers) combustion devices. Typically emissions are estimated based on measured fuel volumes and published combustion emission factors.

Flaring : flaring is a common method of disposing of waste gas volumes at oil and

gas facilities. The flare stacks are designed to provide safe atmospheric dispersion of the effluent. Flares are normally used where the waste gas contains odorous or toxic components (e.g., hydrogen sulphide). Otherwise the gas may be vented. Typically, separate flare/vent systems are used for high- and low-pressure waste gas streams.

Formation CO2 Releases : atmospheric release of naturally or artificially occurring CO2 originally

present in the produced crude oil and natural gas. Formation CO2 is most often extracted in the gas sweetening process at sour gas processing plants. Artificially occurring CO2 may result from the application of enhanced recovery techniques such as CO2 miscible flooding or fire floods.

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Reported Venting : is the sum of all vented volumes stated in production accounting statistics. These volumes are assumed to comprise, where applicable, casing gas venting, waste associated gas flows, treater and stabilizer off-gas and gas volumes discharged during process upsets and equipment depressurization events

Casing Gas : cold production heavy crude oil wells are relatively shallow

(typically 300 to 900 m deep) and, thus, are characterized by low reservoir pressures (typically 4000 kPa or less). To achieve reasonable flow potential it is necessary to relieve natural gas pressure from the well bore (down-hole pressure of about 250 kPa is maintained). Appropriately, the wells usually are not equipped with a production packer (a device that isolates the annulus from the formation). This allows the well pressure to be controlled using the casing vent. This casing gas may be flared or conserved but is most commonly vented.

Associated Gas : gas that is produced along with the liquids from an oil well. The

associated gas is separated from the oil and water at an oil battery and may be conserved, re-injected, flared or vented. If it is flared or vented it may be termed waste associated gas.

Treater Off-Gas : typically when oil is produced from a well it is passed through a

separator to remove the free water and gas. A treater is used to remove the residual emulsified water from oil to meet pipeline water specifications. Since emulsion treaters operate at a lower pressure and higher temperature than the separator, a quantity of gas (treater off-gas) will also be released at this point. This gas may be conserved, re-injected, flared or vented.

Stabilizer Off-Gas : at a gas processing plant hydrocarbon liquids must be separated

from the gas so that the plant can meet the natural gas dew point specifications. This is typically done using a refrigeration process whereby the gas is cooled and the hydrocarbon liquids condense. A stabilizer is used to boil off the light ends of this liquid stream so that it may be stored in an atmospheric tank. The light ends (stabilizer off-gas) may be stored in pressurized bullets for sale, recombined with the sales gas, flared or vented.

Unreported Venting : venting from processes or equipment that is (at the time of this inventory)

not typically reported in production accounting data. Sources include: glycol dehydrator off-gas, loading/unloading losses, storage losses, pneumatic devices (e.g., chemical injection pumps, natural gas operated instrumentation), compressor start gas, purge gas and blanket gas that is discharged directly to the atmosphere and gas vented from drill-stem tests.

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Pneumatic Devices : pneumatic devices fall into categories: instrumentation (e.g., level controller) and devices that use compressed gas as an energy source to perform work (e.g., gas operated chemical injection pump). Both types are an emission concern only when natural gas is used as the supply medium. Due to the small volumes of gas typically released by each installation and the huge number of individual installations, vent gas rates from pneumatic devices are not routinely measured.

While manufacturer’s published nominal vent rates are sometimes

used to estimate emissions from pneumatic devices, field test data indicates that actual emission rates are often significantly different than the manufacturer’s nominal vent rate. Therefore, these emissions are most often estimated using average emission factors.

Uncertainties associated with estimating emissions from pneumatic

devices using average emission factors are high: instrument controllers - ±30 percent and chemical injection pumps - ±60 percent.

Compressor Start Gas : most gas-fired compressors use a pneumatic motor for starting.

Typically the supply gas is natural gas but in some cases compressed air may be used. During a start the gas passes through the start motor and is vented to the atmosphere. Start volumes are rarely measured and are most often estimated based on number of starts and duration or simply number of starts.

Purge Gas : for safe operation flare systems require a constant purge of gas

(usually fuel gas). The purge rate is usually determined when the system is designed. The purge gas rate is sometimes set by installing an appropriate orifice in the purge fuel line but most often it is set by partially opening a valve. Purge gas rates are not typically measured.

Blanket Gas : storage tanks are equipped with gas blanket systems to reduce

emissions (especially when they contain sour products) and to ensure that oxygen does not enter the vapour space of the tank when it is connected to a flare system. The blanket gas is usually fuel gas but any other inert gas could be used.

Storage tanks with gas blanket systems are usually connected to

flare systems but in some cases (if the gas is not sour) the tank vapours and blanket gas may be released through a vent system.

Dehydrator Still

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Column Off-Gas : glycol dehydrators are sources of atmospheric emissions from both the reboiler still column and the use of gas operated glycol pumps. In the dehydration process, glycol is contacted with the wet gas stream to absorb water. In addition to water, the glycol has a tendency to absorb small amounts of hydrocarbons (primarily hexane and heavier hydrocarbons although some methane is absorbed as well). When the glycol is regenerated in the reboiler, the water and hydrocarbons are liberated and vented to the atmosphere. Most glycol dehydrators employ an energy exchange pump to circulate glycol from the reboiler to the contactor tower. The energy in the rich glycol leaving the bottom of the contactor is used to pump the lean glycol back into the top of the contactor tower. A small amount of wet gas also passes through the glycol pump and is subsequently vented from the top of the reboiler still column. Emissions form glycol dehydrator still columns are very difficult to measure. Therefore, these emissions are estimated using either average emission factors (as was done in the 2000 inventory) or a process simulation package.

Loading/Unloading Losses : when tankers (truck, rail or marine) are used to transport

hydrocarbons a certain quantity of hydrocarbon vapours may be released to the atmosphere during loading and unloading operations. Emissions occur when vapours in a tanker are expelled as liquid is added. The quantity of emissions is dependent on the degree of saturation of the vapour space, the type of loading that is employed (i.e., splash or submerged) and the properties of the product.

These emissions are not measured. Instead, correlations developed

by U.S. EPA are used to estimate emissions.

Storage Losses : storage tanks can release emissions as a result of both normal evaporation and from product flashing. Evaporative losses occur when volatile hydrocarbon products are stored in tanks that are vented to the atmosphere. As the product evaporates, the vapour space in the tank becomes saturated with vapours. These vapours are expelled during tank filling (working losses) and due to diurnal temperature and pressure changes (breathing losses). Greenhouse gas emissions from evaporative losses are generally very small due to the low concentrations of methane and carbon dioxide in the stored products.

31

Flashing losses can, however, be a significant source of GHG emissions. Produced hydrocarbon liquids at production facilities frequently contain a certain amount of gas in solution. The amount is determined by the temperature and pressure of the first vessel upstream of the stock tanks. When the product enters the tank, the solution gas flashes or boils off and is released to the atmosphere.

Due to the difficulty in accessing the emission sources on storage tanks and the variability in emissions with climatic conditions and operational parameters, storage losses are not frequently measured. Instead, they are typically estimated based on the volumes of hydrocarbons produced (from production accounting information), the number and types of storage tanks at each facility, and information regarding whether the stored hydrocarbon liquid is a “wild” (i.e., contains solution gas) or “weathered/stabilized” product. U.S. EPA Tanks model is often used to estimate normal evaporation losses. Flashing losses must be assessed by performing a flash calculation (using a process simulator or empirical correlation) at the temperature and pressure of the last vessel upstream of the storage tanks to estimate how much gas is absorbed by the oil.

Fugitive Emissions : unintended releases of GHGs to the atmosphere. This category includes

fugitive equipment leaks and accidents and equipment failures. Fugitive equipment leaks are emissions from equipment components that leak as a result of wear, poor design or improper installation. The primary emission sources include but are not limited to: threaded and flanged connections, valve stem packing leaks, leakage past valve seats to the atmosphere, compressor seals, pump seals, pressure regulator vents and sampling ports. Accidents and equipment failures include: spills, pipeline ruptures, gas migration and surface casing vent flows.

The uncertainties associated with emissions from individual equipment

components are very high. For example, connectors (flanged, threaded and tubing connections) in gas service have 95 percent confidence limits of approximately ±32 percent and valves in gas service have limits of approximately ±17 percent. Other, less common, components have much larger confidence limits: open-ended lines -60 percent to +170 percent; pressure relief valves -98 percent to 98 percent.

Storage Losses : comprise normal evaporation losses due to breathing and working effects,

plus flashing losses where the received liquids have an initial vapour pressure close to or greater than local atmospheric pressure. Gas carry-through to storage tanks due to leakage past drain valves into tank inlet headers, inefficient gas-liquid separation in upstream vessels, malfunctioning level controllers or leakage past the seat of level control valves, or

32

unintentional storage of high vapour pressure liquids in atmospheric tanks are known to be a noteworthy source at some sites, but could not be accounted for due to a lack of appropriate emission factors.

Loading/Unloading Losses: when tankers (truck, rail or marine) are used to transport hydrocarbons a

certain quantity of hydrocarbon vapours may be released to the atmosphere during loading and unloading operations. Emissions occur when vapours in a tanker are expelled as liquid is added. The quantity of emissions is dependent on the degree of saturation of the vapour space, the type of loading that is employed (i.e., splash or submerged) and the properties of the product.

These emissions are not measured. Instead, correlations developed by U.S.

EPA are used to estimate emissions. Accidental Releases: are unintentional releases of gases and unrecovered hydrocarbon liquids to

the environment due to spills and major equipment failures (e.g., pipeline ruptures, third party dig-ins and well blow-outs).

releases of oil, produced water, process chemicals and/or natural gas to the

environment by human error, equipment malfunction, or a major equipment failure (e.g., pipeline break, well blow out, explosion, etc.).

Pipeline Break : a rupture in any part of a pipeline.

Pipeline Leak : fugitive emission through a small opening in the wall of the

pipeline (e.g., due to corrosion or material defects) or from valves, fittings or connectors attached to that pipeline.

Natural Gas Migration : flow of natural gas around the outside of a well’s casing; may be

fed by leaks far underground (about 8% of conventional heavy crude oil wells experience significant gas migration).

Surface Casing Vent Flows : leakage of natural gas into the well casing. If a vent flow occurs

there is a failure in the casing system; the casing, the production stream or the packer may be leaking. The gas may be produced, flared or vented.

1.4.4 Emission Accounting Atmospheric Oxidation : formation of CO2 by the oxidation of hydrocarbons after release to the

atmosphere. Hydrocarbons have lives of days to years within the

33

atmosphere but are eventually all oxidized to CO2 due to the effect of ultraviolet light. Therefore, the carbon contained in emissions must be converted to CO2 using the equation:

1244

2 ×= CCO

where,

CO2 is the total carbon dioxide emissions in (tones), C is the mass of carbon contained in all hydrocarbon emissions (tonnes), and 44/12 is the ratio of the molecular weight of CO2 to that of carbon.

CAS Number (CAS#) : Chemical Abstracts Number. A unique number that identifies a chemical

substance. Standard Reference Conditions : Most equipment manufacturers reference flow, concentration and

quipment performance data at ISO standard conditions of 15ºC, 101.325 kPa, sea level and 0.0 percent relative humidity.

The following equation shows how to correct air contaminant concentrations measured in the exhaust to 3 percent oxygen (15% excess air) for comparison and regulatory compliance purposes. To correct emission levels to 3 percent oxygen that are referenced to excess air levels other than 3 percent , use the following equation:

1.4.5 Other Emission Related Terminology Combustion Efficiency : The extent to which all input combustible material has been completely

oxidized (i.e., to produce H2O, CO2 and SO2). Complete combustion is often approached but is never actually achieved. The main factors that contribute to incomplete combustion include thermodynamic, kinetic, mass transfer and heat transfer limitations. In fuel rich systems, oxygen deficiency is also a factor.

Destruction Efficiency : The extent to which a target substance present in the input combustibles

has been destroyed (i.e., converted to intermediate, partially-oxidized and fully-oxidized products of combustion).

(actual) ppm x (actual)O - 21

3 - 21 = %) (3 ppm2

34

Heat Rate : The amount of heat energy (based on the net or lower heating value of the

fuel) which must be input to a combustion device to produce the rated power output. Heat rate is usually expressed in terms of net J/kW≅h.

Kinetics and Thermodynamics : Thermodynamic equilibrium defines the maximum extent to which a

chemical reaction such as combustion may proceed (i.e., the point at which there is no further tendency for change).

Chemical kinetics determine the rate at which a chemically reacting system will approach the point of thermodynamic equilibrium.

Power Output : For engines it is the net shaft power available after all losses and power

take-offs (e.g., ignition-system power generators, cooling fans, turbo chargers and pumps for fuel, lubricating oil and liquid coolant) have been subtracted. For heaters and boilers it is the net heat transferred to a target process fluid or system.

Thermal Efficiency : The percentage or portion of input energy converted to useful work or heat

output. For combustion equipment, typical convention is to express the input energy in terms of the net (lower) heating value of the fuel. This results in the following relation for thermal efficiency:

Allternatively, thermal efficiency may be expressed in terms of energy losses as follows:

Losses in thermal efficiency occur due to the following potential factors:

• exit combustion heat losses (i.e, residual heat value in the exhaust gases),

• air infiltration, • incomplete combustion, and • mechanical losses (e.g., friction losses and energy needed to run

cooling fans and lubricating-oil pumps).

100% x Inputy Heat/Energ NetOutput Work/Heat Useful = Efficiency Thermal = η

100% x Inputy Heat/Energ Net

LossesEnergy - 1 =

Ση

35

36

2.0 INFORMATION SOURCES The following sections provide a complete listing of the sources of activity and infrastructure (facility and equipment) data available for the UOG industry in British Columbia, Alberta, Saskatchewan and the rest of Canada, respectively. 2.1 BRITISH COLUMBIA Table 2.1 Summary listing of potentially useful sources of activity data and facility information

for the UOG industry in British Columbia. Ref. No. Author Reference Description Link

OGC Oil and Gas Commission

MEM Ministry of Energy and Mines

MPR Ministry of Provincial Revenue

MWLAP

Ministry of Water, Land and Air Protection

IRIS

Integrated Resource Management System Oracle database

PIMS

Petroleum Information Management System Legacy database

RMS

Royalty Management System confirm with MPR

IRIS OGC Drilling Data for all Wells in B.C. .csv and .txt formats; was in PIMS

http://www.ogc.gov.bc.ca/datadownloads.asp

(30+ files)

wells - well location file, well status file, AOFP tests (Absolute Open Flow Potential), casing file (surface casing information), completion and completion status files, well core file, well DSTs (Drill Stem Tests), well formation file, well log file, well pressure file, work-over file, drilling file, abandoned well and formation files, oil, gas and water analyses files, gas and water injection files; facilities - general information file (location, type, compressor hp, amendments, flaring approval file, receipts and disposition (S2 data) file; gas plants - design capacities file, process description file.

IRIS OGC Production Data for all Wells in B.C. .csv and .txt formats; was in PIMS

http://www.ogc.gov.bc.ca/datadownloads.asp

37

Table 2.1 Summary listing of potentially useful sources of activity data and facility information for the UOG industry in British Columbia.

Ref. No. Author Reference Description Link (zone_prd file) production (S1 data) file

IRIS OGC Well Index .csv, .pdf, and ASCII formats

http://www.ogc.gov.bc.ca/datadownloads.asp

(by authorization, location, name)

IRIS OGC Well Surface Location .csv format

http://www.ogc.gov.bc.ca/datadownloads.asp

IRIS OGC Inspections obtain extract upon request

includes drilling rig, final restoration, flow test, pipeline, production equipment, service rig, spill, suspended well, sump fluid pump-off inspections

IRIS OGC Well Activity Statistics http file

http://www.ogc.gov.bc.ca/corporatereports.asp

annual statistics (no. spudded, m drilled, active producers etc.)

IRIS? OGC Pipeline and Well Query System pipeline data (from PL forms)

http://www.deniverville.com/wconnect/wc.dll?Mycode~logon_start

pipeline specifications, substance code, design pressure, location etc.; well locations

OGC Gas Plant Design Capacities .xls file

http://www.ogc.gov.bc.ca/documents/checklists/pipefac/gasplantcapacities.xls

plant design capacities, processes etc.; information is also in "Drilling Data" facility files above

RMS MPR Facility Codes Facility-type codes (same as OGCs)

http://www.em.gov.bc.ca/subwebs/resourcerev/royataxs/codes/facility-code/facility-c.htm

RMS MPR Producer Cost of Service confirm extract arrangements

location, type, size of facility compressors, dehydrators, field processing facilities; line heater assumptions; average H2S concentration (collected on BC-22)

RMS MPR

Monthly Natural Gas Plant Statement confirm extract arrangements

38

Table 2.1 Summary listing of potentially useful sources of activity data and facility information for the UOG industry in British Columbia.

Ref. No. Author Reference Description Link

Includes gathering system flared gas; plant acid gas shrinkage, flare volume (Form 16)

MEM

Oil and Gas in British Columbia, Statistics and Potential 1991-2001

available in .pdf format (Drilling and Production Statistics file)

http://www.em.gov.bc.ca/Oil&gas/OGPublications/OGBCsrp2001.htm

annual statistics on oil & gas revenue, wells drilled and production volumes

MEM Annual BC Oil & Gas Statistics as above (1966-2001); .xls file

http://www.em.gov.bc.ca/Oil&gas/OilGasStats/AnnualOGStatistics.htm

MEM

Monthly Oil and Gas Statistics Reports can specify year; .xls files

http://www.em.gov.bc.ca/Oil&gas/OilGasStats/MonthlyOGStatistics.htm

supply (receipts) and disposition reporting for province; includes gas plant summaries, refinery, transporter etc. statistics; flared volumes

MWLAP

Registration and amendment information for facilities above specified thresholds

Oil and Gas Waste Reg. req't (s. 6); confirm how to get extract with MWLAP

600 kW<compressor total power<3 000 kW, high sulphur fuel gas, processing plants, testing >=5% H2S wells

MWLAP Permit information confirm extract arrangements with MWLAP

for facilities discharging >=30t/15 days sulphur; drivers for compressors etc. >3000 kW

MWLAP

Emission monitoring, fee collection data

confirm extract arrangements with MWLAP

for facilities covered by gas turbine, sulphur recovery criteria

MWLAP Invert mud records confirm extract arrangements with MWLAP

MWLAP

Incident records (e.g., excessive flaring)

confirm extract arrangements with MWLAP

CAPP Statistical Handbook CD-ROM

Annual drilling, production, expenditure etc. statistics

39

2.2 ALBERTA Table 2.2 Summary listing of potentially useful sources of activity data and facility information

for the UOG industry in Alberta. Ref No. Author Reference Description Link ST-77 EUB Basic Well Code

Conversion File Interpretation of coded data from the EUB's database; code names and abbreviations for such data as field/pool, oil sands area/deposit, company name and address (for operators, licensees, agents, drilling contractors), field centre; for the purpose of printing reports requiring the translation of coded data.

EUB BOS - Board Order System

The EUB issues Field and Pool Orders under the Oil and Gas Conservation Act. For administrative purposes, the EUB alsomaintains Strike Areas that are similiar to Fields but are notlegal documents under the Act. Includes current andhistorical Strike Areas, Field Orders, Pool Orders and Tractsof land in each order.

EUB Drilling Well Data File

Data on new drilling wells, wells being reworked; well status changes; field/pool changes; corrections to previously reported data; basic, descriptive well data. S-4 data included with the well status history.

EUB Environmental Information System List

Environmental incidents reported to the EUB back to 1975, including noise infractions, air quality emissions, oil spills, and failures for pipelines, wells, plants and batteries.

EUB Gas Energy Data System (GEDS) Data Base File

GEMM Model compatible data base contains information on approximately 1300 fields and some 22 000 non-confidential pools. Information includes field data, pool description, reserve location, basic reserve data, contract information, plant data, gas analyses, deliverability test data, number of wells by pool, historical production figures, and pertinent comments. Contains some 290 000 card-image records.

EUB Gas Well AOFP/Pressure File

Absolute Open Flow Potential (AOFP) test and pressure test data collected on nonconfidential wells. Includes basic well information such as test date, pressures, temperatures, shut-in period, flow rate, flow duration, test type, and other information on some 300 000 individual tests.

40

Table 2.2 Summary listing of potentially useful sources of activity data and facility information for the UOG industry in Alberta.

Ref No. Author Reference Description Link ST-75 EUB General Well Data

File Basic drilling data for oil, gas, oil sands, and water wells. Includes such data as licensing, formation tops and markers, logs, DST, casing and cementing, packer data, perforations and treatments, plug back and abandonment and well status history.

ST-80 EUB Historical Well Production-Injection and Well Control Data Files

Includes all production and injection data by month for all Alberta wells from 1962 to present. Adjustments have been applied retroactively. Control data are current. Approximately 700 000 variable-length records.Control data file includes selected control data (well name, field and pool codes interpretation, etc) for retrieval and printout of well data from the historical file. Approximately 65 000 fixed length records.

EUB Individual Well Gas Analysis File

Gas analysis data by zone on some 39 000 non-confidential wells: approximately 70 000 samples providing compositional breakdown of gas, associated liquids, and recombined analysis; sample points and dates; and basic well information.

ST-82 EUB List of Wells in Alberta

Includes the following data for all oil, gas, oil sands experimental, and evaluation wells drilled: identifier, well name, field or oil sands area, pool or oil sands deposit, licence number, licence date, licensee and agent code, finish drilling date, total depth, current status and status date. In order of ascending Well-ID.

EUB Pipeline Attribute File

Complete file of information on pipeline permits and licences, tests, status, construction, and specifications; experimental pipelines not included.

EUB Pool Average Gas Analysis File

Individual pool average gas analysis data on some 22 000 non-confidential pools. Includes compositional breakdown of non-associated, associated, and solution gas, reserve type, pool status, remaining reserves, and basic pool information.

41

Table 2.2 Summary listing of potentially useful sources of activity data and facility information for the UOG industry in Alberta.

Ref No. Author Reference Description Link EUB Pool to Plant

Pointer File Includes percentage of pool production flowing to a plant, plant code, reserve type, field code, pool code, and pool sequence. Contains approximately 25 000 card-image records.

ST-3 EUB Alberta Energy Resource Industries Monthly Statistics

supply and disposition of crude oil and equivalent, natural gas, and gas products for the province.

ST-13A

EUB Alberta Gas Plant Statistics

Includes monthly gas processing plant receipts and disposition volumes, and also liquid and sulphur products from plant processing for the current year and a summary for a ten-year historical period.

ST-13C

EUB Alberta Gas Gathering Systems Receipts and Disposition

ST-37 EUB List of Wells in Alberta Monthly Updates

ST-39 EUB Alberta Oil Sands Plant Statistics Monthly Supplement

ST-41 EUB Regulatory Highlights

ST-44 EUB Alberta Oil Sands Schemes Quarterly Supplement

ST-50 EUB Gas Processing Plants in Alberta Quarterly Update

ST-51 EUB Drill-Stem Test (DST) Service Report

ST-53 EUB Alberta Crude Bitumen In Situ Production Monthly Statistics

ST-56 EUB Gas Production and Capability Summary

ST-59 EUB Alberta Drilling Activity Monthly Statistics

42

Table 2.2 Summary listing of potentially useful sources of activity data and facility information for the UOG industry in Alberta.

Ref No. Author Reference Description Link ST-60A

EUB Crude Oil and Crude Bitumen Batteries Annual Flaring, Venting, and Production Data

This annual report provides a convenient method to identify the batteries flaring solution gas in the province. It allows operators and third parties to identify batteries where conservation of solution gas may be economically viable. The overall objective is to reduce the volume of solution gas flared annually. Contains general information such as operator, battery location, and code, as well as volume of solution gas produced, flared, and vented and oil production

ST-60B

EUB Upstream Petroleum Industry Flaring and Venting Report: Industry Performance for the Year Ending December 31

This annual report provides a summary of flared volumes for the various oil and gas industry sectors, and reports in detail on solution gas conserved, flared and vented during the year ending December 31. Tables show operators by rank based on solution gas flared, solution gas vented, total solution gas production, and total oil from crude oil and bitumen batteries

ST-62 EUB Drill Stem Tests (DST)

ST-63 EUB Absolute Open Flow Tests (AOF)

GB 2001-12

EUB List of EUB-Approved Oilfield Waste Management Facilities

www.eub.gov.ab.ca/bbs/ils/gbs/pdf/gb2001-12.pdf

S2 EUB Disposition Statement

See Guide 7. www.eub.gov.ab.ca/bbs/products/guides/g07/g07-2001.pdf

S8 EUB Gas Gathering Statement

See Guide 7. www.eub.gov.ab.ca/bbs/products/guides/g07/g07-2001.pdf

S18 EUB Injection Disposal Statement

See Guide 7. www.eub.gov.ab.ca/bbs/products/guides/g07/g07-2001.pdf

S20 EUB Gas Processing Statement

See Guide 7. www.eub.gov.ab.ca/bbs/products/guides/g07/g07-2001.pdf

S21 EUB Gas Processing Plants Product Statement

See Guide 7. www.eub.gov.ab.ca/bbs/products/guides/g07/g07-2001.pdf

S30 EUB Gas Processing Plants Sulphur Balance Report

See Guide 7. www.eub.gov.ab.ca/bbs/products/guides/g07/g07-2001.pdf

EUB Licensed Facility Report

lists all licensed oil and gas facilities in the province including licensee code and name, licence number, status, category, location, facility ID and type, and operator code & name

www.eub.gov.ab.ca/bbs/data/facilities/facilities_licensed.txt

43

Table 2.2 Summary listing of potentially useful sources of activity data and facility information for the UOG industry in Alberta.

Ref No. Author Reference Description Link EUB Non-licensed

Facility Report lists all non-licensed oil and gas facilities including operator code and name, location, type, and facility ID and name

www.eub.gov.ab.ca/bbs/data/facilities/facilities_nonlicensed.txt

Pet. Reg. Facility ID - Battery contains all battery codes that existed on the EUB database as of September 24th 2002. The file contains the operator code, facility ID, type, location, sub type, facility operational status, licence number, licence type, licensee and facility name that is based on July production month

www.eub.gov.ab.ca/BBS/new/Projects/FacilityID-Battery.htm

Pet. Reg. Facility ID - Compressor Station

contains reporting IDs for each compressor station that has an EUB facility licence

www.eub.gov.ab.ca/BBS/new/Projects/CompressorStationID.htm

Pet. Reg. Facility ID - Custom Treating

contains all Custom Treating codes that are identified as of October 11, 2002

www.eub.gov.ab.ca/BBS/new/Projects/FacilityID-CustomTreating.htm

Pet. Reg. Facility ID - Gas Gathering System

contains all gas gathering codes that are identified as of October 16, 2002

www.eub.gov.ab.ca/BBS/new/Projects/FacilityID-GasGatheringSystem.htm

Pet. Reg. Facility ID - Gas Plant

contains all gas plant codes that are identified as of October 11, 2002

www.eub.gov.ab.ca/BBS/new/Projects/FacilityID-GasPlant.htm

Pet. Reg. Facility ID - Injection contains all Injection codes that are identified as of October 11, 2002

www.eub.gov.ab.ca/BBS/new/Projects/FacilityID-Injection.htm

Pet. Reg. Facility ID - Pipeline contains all pipeline codes that are identified as of September 27th 2002. The file contains the required data elements for volumetric submission

www.eub.gov.ab.ca/BBS/new/Projects/FacilityIDPipeline.htm

Pet. Reg. Facility ID - Refinery contains all Refinery codes that are identified as of October 11, 2002

www.eub.gov.ab.ca/BBS/new/Projects/FacilityID-Refinery.htm

Pet. Reg. Facility ID - Terminal

contains all Terminal codes that are identified as of October 11, 2002

www.eub.gov.ab.ca/BBS/new/Projects/FacilityID-Terminal.htm

Pet. Reg. Facility ID - Terminal Facilities Not Converted

contains Terminal codes for Terminals that are not converted to the Registry as of November 20, 2002

www.eub.gov.ab.ca/BBS/new/Projects/facilityID-Terminal-NotConverted.htm

Pet. Reg. Facility ID - Waste Plant

contains all Waste Plant codes that are identified as of October 11, 2002

www.eub.gov.ab.ca/BBS/new/Projects/FacilityID-WastePlant.htm

Pet. Reg. Single Well Battery - More Than One Well Linked

contains batteries that have a battery type that indicates the battery is a single well battery

www.eub.gov.ab.ca/BBS/new/Projects/SingleWellBattery.htm

Pet. Reg. Valid Well Status Combinations Table

a reference table used in validating the well status within the Edit Well Status or the Commingle Well Status process of the Petroleum Registry

www.eub.gov.ab.ca/BBS/new/Projects/ValidWellStatus.htm

Pet. Reg. Well DTL 1 to 4 contain all wells that existed on the EUB production injection disposition (PID) system as of October 3rd 2002

www.eub.gov.ab.ca/BBS/new/Projects/welldtl.htm

44

Table 2.2 Summary listing of potentially useful sources of activity data and facility information for the UOG industry in Alberta.

Ref No. Author Reference Description Link Pet. Reg. Wells With Inactive

Status Linked to Battery

contains a list of wells with an inactive well status or wells linked to a wrong facility type that were reported on an S-1 or S-18 statement during the July production month

www.eub.gov.ab.ca/BBS/new/Projects/InactiveWells.htm

Pet. Reg. Water Source Well ID Info

Complete lists of licensed and unlicensed water source wells that currently exist on the EUB data base

www.eub.gov.ab.ca/BBS/new/Projects/WaterSourceWell.htm

Alberta Energy

Pipeline and Terminal Listing

Contains a listing of major pipelines, terminals and cleaning plants in Alberta. Pipeline and terminal codes and locations are provided.

www.energy.gov.ab.ca/com/Oil/Reporting+Information/Pipeline+and+Terminal+Listing.htm

Alberta Energy

Facilities and Transport Regions

Contains a listing of all gas gathering systems and gas processing plants in Alberta. Includes facility code (same as EUB facility code), location, operator, facility name, transport region and facility type code.

www.energy.gov.ab.ca/gmd/docs/FacilitiesAndTransportRegions.xls

Alberta Environment

Inventory of Nitrogen Oxide Emissions and Control Technologies in Alberta’s Upstream Oil and Gas Industry

A report outlining currently installed compressor emission controls. The acccompanying database contains a listing of the majority of compressors that report to Alberta Environment. Includes facility ID, type, location and name as well as compressor make and model, rated power and reported NOx emissions.

EUB EUB Compressor Engine Database

Contains a listing of compressor engines by location (not by facility) for engines installed at licenced facilities between 1996 and 2002. Includes the engine rated power (kW) for each unit.

AENV Approvals Provides a summary of gas-fired equipment installed at licenced facilities. Ususally includes rated power and reported NOx and SO2 emissions.

http://deneb.env.gov.ab.ca/aewp/plsql/avwp_avwh1000_02.startup?Z_CHK=0

45

2.3 SASKATCHEWAN Table 2.3 Summary listing of potentially useful sources of activity data and facility information

for the UOG industry in Saskatchewan. Ref No. Author Reference Description Link

Saskatchewan Digital Well Data Base

an ASCII formatted database containing all wells drilled (whether vertical, directionally drilled or horizontal) for oil, gas, potash, service and other minerals in the sedimentary basin of Saskatchewan under the Oil and Gas Conservation Regulations, 1985

Production Injection History File

All time historical production and injection information is available for all wells in Saskatchewan

Mineral Statistics Yearbook

Contains production and revenue statistics of all minerals produced in the province (including petroleum and natural gas).

Drilling Activity Report

A monthly/weekly report which lists by production and disposition areas and classification the well licences issued, wells finished drilling, well completions, well abandonments, wells brought on production, plugback wells, well name changes, well licences cancelled, well reclassifications and well amendments

Monthly Oil and Gas Production Report

Lists by production and disposition areas the monthly production of oil, gas and water units and pools.

Saskatchewan Horizontal Well Summary

Listing of all horizontal wells licensed in Saskatchewan grouped by well status. The listing is published monthly and includes application and approval dates in addition to licence and drilling data.

Horizontal Well Drilling Data

A listing of all horizontal wells licenced in Saskatchewan

www.gov.sk.ca/enermine/energy/hzwells/hzwelldr.htm

Horizonal-Pool Codes and Name Report

This report contains the following fields: horizon-pool code, horizon-pool name, horizon-pool average depth, area-crude type code.

www.gov.sk.ca/enermine/store/hrznpool.txt

Unit List Report

The Unit List Report is in numeric sequence and is a two-part report. The first part deals with oil units and the second part deals with gas units. This report contains the following fields: code, unit name, horizon-pool code, unit approval date, operator code, operator name, and operator effective date.

www.gov.sk.ca/enermine/store/rpts_o&g.htm

Monthly Natural Gas Production - Associated

This report lists the volume of associated gas produced in each area-crude type by month. Quarterly totals and yearly cumulative totals are provided

www.gov.sk.ca/enermine/store/rpts_o&g.htm

Monthly Natural Gas Production - Non-Associated

This report lists the volume of non-associated gas produced in each area by month. Quarterly totals, provincial monthly totals, and yearly cumulative totals are provided

www.gov.sk.ca/enermine/store/rpts_o&g.htm

46

Table 2.3 Summary listing of potentially useful sources of activity data and facility information for the UOG industry in Saskatchewan.

Ref No. Author Reference Description Link

Monthly Crude Oil Production

This report lists the volume of crude oil produced in each area-crude type by month. Quarterly totals, provincial monthly totals, and yearly cumulative totals are provided.

www.gov.sk.ca/enermine/store/rpts_o&g.htm

The Facility Master Report

By Location is available for download. The file is a compressed self-extracting ASCII file that contains the following fields: Facility (code and name), Location, Current Operator, (code and name) Current Operator Effective Date, Current Status Effective Date and Facility Status. This file will be updated on or about the 8th day of each month

www.gov.sk.ca/enermine/store/rpts_o&g.htm

The Node/Connector Master Report

By Name is available for download. The file is a compressed self-extracting ASCII file that contains the following fields: Node/Connector (code and name), Location, Current Operator, (code and name) Current Operator Effective Date, Current Status Effective Date and Node/Connector Status

www.gov.sk.ca/enermine/store/rpts_o&g.htm

47

2.4 REST OF CANADA Table 2.4 Summary listing of potentially useful sources of activity data and facility information for

the upstream UOG industry in the rest of Canada. Ref No. Author Reference Description Link NEB Crude Oil Supply,

Disposition and Price Report - Monthly

Estimated Production of Canadian Crude Oil; Estimated Disposition of Canadian Light and Heavy Crude Oil and Imports; Estimated Netback Price of Domestic Crude Oil Exports; Exports of Crude Oil by Type

www.neb.gc.ca/stats/oil/sudi0012.xls

NEB Yukon Production Data

Gas production and disposition data for Kotaneelee.

NEB NWT Production Data

Oil and gas production and disposition data for Norman Wells, Pointed Mountain.

CAPP Industry Facts and Information

General information including annual spending, wells drilled, reserves, production, revenue, employment, exports and consumption for each province or region.

www.capp.ca/default.asp?V_DOC_ID=6

CAPP Upstream Petroleum Industry Glycol Dehydrator Benzene Emissions Status Report

Locations and emissions from glycol dehydrators. Report updated in 1999.

www.cappmember.net/ASP/..%5CCache%5CradC632E.tmp%5Cj8601!.PDF

CAPP Statistical Handbook The 2000 CAPP Statistical Handbook is a historical summary of the petroleum industry's progress, summarizing The handbook features drilling, reserves, production and other current and historical data. Additional data is developed annually to retain the value of the handbook as an up-to-date reference source.

Cat 55-201

Statistics Canada

Pipeline transportation of crude oil and refined petroleum products

Cat 55-201. The publication presents information from companies primarily engaged in the gathering and transportation of crude oil and liquefied petroleum gases to refineries and for export. Details include: operating revenue/expenses, employment and payroll, balance sheet data, pumping stations, pipeline length and truck line systems, receipts and disposition of crude oil, summary of pipeline movements of crude oil and equivalent and liquified petroleum gases and petroleum products, summary of pipeline movements by commodity groups, oil and pipeline distance by province and size of pipe in service, for refined petroleum and coal products industries.

48

Table 2.4 Summary listing of potentially useful sources of activity data and facility information for the upstream UOG industry in the rest of Canada.

Ref No. Author Reference Description Link Cat 26-006

Statistics Canada

Supply and disposition of crude oil and natural gas

Cat 26-006. This publication presents information from crude petroleum and natural gas producers, covering the production and final destination of crude petroleum, natural gas and natural gas liquids, by province. The details presented include production statistics, processing plant products and supply, surplus and disposition of crude oil, natural gas and gas use-reprocessing.

Cat 26-213

Statistics Canada

Oil and gas extraction

Cat 26-213. This report covers companies in the oil and gas exploration, development and production industry. It presents data on employment, payroll, production, disposition, exports and imports and the number of establishments. It provides details on wage earners, as well as statistics on reserves, drilling completions, exploration development and other geological and geophysical operations. It also includes definitions, a data analysis and a bibliography.

Cat 55-001

Statistics Canada

Pipeline transportation of crude oil and refined petroleum products

Cat 55-001. This on-line publication covers the activities of the major pipelines carrying crude oil and equivalents, liquefied petroleum gases such as propane, butane, ethane and others within and between provinces. The data are collected by province for receipts, deliveries, imports, exports and inventories.

Cat 55-002

Statistics Canada

Natural gas transportation and distribution

Cat 55-002. The publication provides data from transmission and distribution companies primarily engaged in the selling of natural gas to ultimate consumers through distribution pipelines (distribution systems). Also included are data on receipts and disposition of natural gas

49

Table 2.4 Summary listing of potentially useful sources of activity data and facility information for the upstream UOG industry in the rest of Canada.

Ref No. Author Reference Description Link Cat 57-205

Statistics Canada

Natural gas transportation and distribution

Cat 57-205. The publication provides information from companies engaged in the selling of natural gas to ultimate consumers through distribution pipelines, and those companies engaged in the transportation of natural gas by pipeline to local distribution systems. Details include: employment and payroll, natural gas sales and gas utilities (transport and distribution by type of system, property account data by plant category, income statement and balance sheet data and number and type of compressor stations operated) and pipelines (distance by purpose of pipeline and material used in pipeline).

Cat 57-003

Statistics Canada

Quarterly report on energy supply-demand in Canada

The publication presents energy balance sheets in natural units and heat equivalents in primary and secondary forms, by province, each showing data on production, trade, interprovincial movements, conversion, and consumption by sector. Analytical tables and details on non-energy products are shown. It includes explanatory notes, a historical energy summary table and a data analysis. The publication also presents natural gas liquids, electricity generated from fossil fuels, solid wood waste and spent pulping liquor.

CAODC Annual Drilling Rig Operating Days/Depth Summary

Contains an annual summary of drilling data for each province. Includes metres drilled, metres drilled by depth, and number of drilling days by depth range.

www.caodc.ca/Public%20Statistics/Rig%20Counts/annual_day_depth_summary.htm

CAODC Wells Drilled on a Completion Basis (Provincial Breakdown)

Contains a listing of wells drilled in each province by type of well - oil, gas, dry and service.

www.caodc.ca/Public%20Statistics/Well%20Counts/annual_provincial_completions.htm

NWT Resources, Wildlife and Economic Development

NWT Gas & Oil Production

Oil and gas production by project. www.stats.gov.nt.ca/Statinfo/industry/non_renew/production.otp

Manitoba Energy, Science and Technology

Manitoba Oil Activity Review

Production details for Manitoba oil fields.

www.gov.mb.ca/itm/petroleum/oar/oar.pdf

50

3.0 EMISSION FACTORS Tables 3.1 and 3.2 contain a summary of average emission factors used to estimate emissions from fugitive equipment leaks (see Section 7.1 of Volumes 3 and 4 for a description of how these factors are used). These factors are appropriate for estimating emissions from a large population of sources (i.e., thousands or greater) but may result in significant errors when applied to too small a population. A brief description of the data types contained in the table follows:

• Factor Group – an analysis of data collected from extensive field testing indicates that average emission factors for gas production and processing facilities are statistically different than those for oil production facilities. Therefore, two sets of factors are presented. Those in Table 3.1 are for gas production and processing facilities and those in Table 3.2 are for oil production facilities.

• Natural Gas Type – not surprisingly more care and attention is usually afforded to components containing sour natural gas. Leaking components are easier to locate and, due to the toxic nature of H2S, repairs of leaking components are more timely. Accordingly, if the gas for a particular process unit is known to be either sweet or sour the appropriate factors should be used. Otherwise, the “ALL” category provides average factors without any regard for whether the gas is sweet or sour.

• Service – similar to the Natural Gas Type category, the type of stream a component contains has an affect on emissions from the component. The available services are:

o Gas/Vapour – all gas streams except Fuel Gas. o Fuel Gas – fuel piping tends to receive more modifications, is subjected to heat

and vibration and is generally odourless and, consequently, average emissions for fuel gas piping are greater.

o Light Liquid – the process fluid is a hydrocarbon liquid at the operating conditions and has a vapour pressure of 0.3 kPa or greater at 15ºC. Light/medium crude oil, condensate and NGLs fall into this category.

o Heavy Liquid – the process fluid is a hydrocarbon liquid at the operating conditions and has a vapour pressure of less than 0.3 kPa at 15ºC. Heavy crude oil and crude bitumen fall into this category.

• Equipment Component Type – the type of equipment component for which the average emission factor applies.

• Emission Factor – the average total hydrocarbon (THC) emissions for all components of the specified type. The factor takes into account the fact that only very few components have significant leak rates and the vast majority of components leak very little or not at all. Estimation of emissions of a specific compound (e.g., CH4) requires that a speciation profile be applied to the calculated THC emissions (see Section 8.0 of Volumes 3 and 4).

• Lower and Upper Uncertainties – these values are fractions greater than zero that provide an indication of the variability in the presented data. They are the 95 percent confidence limits on the average emission factor. For example, an open-ended line in fuel gas service at a gas facility would be expected (with 95 percent confidence) to have an emission rate in the range of 0.271 kg/h to 0.803 kg/h with the most likely value being 0.467 kg/h.

51

Table 3.1 Compilation of component average emission factors for estimating total

hydrocarbon (THC) emissions from fugitive equipment leaks at natural gas production and processing facilities (kg/h/source).

Factor Group

Natural Gas Type Service Equipment Component

Type

Emission Factor (kg/h)

Lower Uncertainty

Upper Uncertainty

GAS ALL Fuel Gas Connectors 8.18E-04 0.32 0.32 GAS ALL Fuel Gas Chemical Injection Pumps 1.62E-01 0.60 0.60 GAS ALL Fuel Gas Controllers 2.38E-01 0.27 0.27 GAS ALL Fuel Gas Compressor Seals 7.13E-01 0.36 0.36 GAS ALL Fuel Gas Control Valves 1.62E-02 0.27 0.27 GAS ALL Fuel Gas Open-Ended Lines 4.67E-01 0.58 1.72 GAS ALL Fuel Gas Pressure Relief Valves 1.70E-02 0.98 0.98 GAS ALL Fuel Gas Pressure Regulators 8.11E-03 0.72 2.38 GAS ALL Fuel Gas Compressor Starts 6.34E-03 0.25 0.25 GAS ALL Fuel Gas Valves 2.81E-03 0.17 0.17 GAS ALL Gas/Vapour Connectors 7.06E-04 0.31 0.31 GAS ALL Gas/Vapour Chemical Injection Pumps 1.62E-01 0.60 0.60 GAS ALL Gas/Vapour Controllers 2.38E-01 0.27 0.27 GAS ALL Gas/Vapour Compressor Seals 7.13E-01 0.36 0.36 GAS ALL Gas/Vapour Control Valves 1.46E-02 0.23 0.23 GAS ALL Gas/Vapour Open-Ended Lines 4.27E-01 0.62 1.61 GAS ALL Gas/Vapour Pressure Relief Valves 1.70E-02 0.98 0.98 GAS ALL Gas/Vapour Pressure Regulators 8.11E-03 0.72 2.38 GAS ALL Gas/Vapour Valves 2.46E-03 0.15 0.15 GAS ALL Light Liquid Connectors 5.51E-04 0.90 1.11 GAS ALL Light Liquid Control Valves 1.77E-02 0.45 0.45 GAS ALL Light Liquid Open-Ended Lines 1.83E-02 0.79 1.27 GAS ALL Light Liquid Pressure Relief Valves 5.39E-03 0.80 0.80 GAS ALL Light Liquid Pump Seals 2.32E-02 0.74 1.36 GAS ALL Light Liquid Valves 3.52E-03 0.19 0.19 GAS SOUR Gas/Vapour Connectors 1.36E-04 0.72 0.72 GAS SOUR Gas/Vapour Control Valves 9.64E-03 0.04 0.04 GAS SOUR Gas/Vapour Open-Ended Lines 1.89E-01 0.79 1.27 GAS SOUR Gas/Vapour Pressure Regulators 4.72E-05 0.74 1.26 GAS SOUR Gas/Vapour Valves 1.16E-03 0.31 0.31 GAS SWEET Gas/Vapour Connectors 8.18E-04 0.32 0.32 GAS SWEET Gas/Vapour Control Valves 1.62E-02 0.27 0.27 GAS SWEET Gas/Vapour Open-Ended Lines 4.67E-01 0.58 1.72 GAS SWEET Gas/Vapour Pressure Regulators 8.39E-03 0.72 2.39 GAS SWEET Gas/Vapour Valves 2.81E-03 0.17 0.17

52

Table 3.2 Compilation of component average emission factors for estimating total

hydrocarbon (THC) emissions from fugitive equipment leaks at oil production and processing facilities (kg/h/source).

Factor Group

Crude Oil Type Service Equipment Component

Type

Emission Factor (kg/h)

Lower Uncertainty

Upper Uncertainty

OIL ALL Fuel Gas Connectors 2.46E-03 0.15 0.15 OIL ALL Fuel Gas Chemical Injection Pumps 1.62E-01 0.60 0.60 OIL ALL Fuel Gas Controllers 2.38E-01 0.27 0.27 OIL ALL Fuel Gas Compressor Seals 8.05E-01 0.36 0.36 OIL ALL Fuel Gas Control Valves 1.46E-02 0.21 0.21 OIL ALL Fuel Gas Open-Ended Lines 3.08E-01 0.78 1.29 OIL ALL Fuel Gas Pressure Relief Valves 1.63E-02 0.80 0.80 OIL ALL Fuel Gas Pressure Regulators 6.68E-03 0.72 2.38 OIL ALL Fuel Gas Compressor Starts 6.34E-03 0.25 0.25 OIL ALL Fuel Gas Valves 1.51E-03 0.79 0.79 OIL ALL Gas/Vapour Connectors 2.46E-03 0.15 0.15 OIL ALL Gas/Vapour Chemical Injection Pumps 1.62E-01 0.60 0.60 OIL ALL Gas/Vapour Controllers 2.38E-01 0.27 0.27 OIL ALL Gas/Vapour Compressor Seals 8.05E-01 0.36 0.36 OIL ALL Gas/Vapour Control Valves 1.46E-02 0.21 0.21 OIL ALL Gas/Vapour Open-Ended Lines 3.08E-01 0.78 1.29 OIL ALL Gas/Vapour Pressure Relief Valves 1.63E-02 0.80 0.80 OIL ALL Gas/Vapour Pressure Regulators 6.68E-03 0.72 2.38 OIL ALL Gas/Vapour Valves 1.51E-03 0.79 0.79 OIL ALL Heavy Liquid Connectors 7.50E-06 0.90 1.11 OIL ALL Heavy Liquid Pressure Relief Valves 3.20E-05 0.80 0.80 OIL ALL Heavy Liquid Pump Seals 3.20E-05 0.74 1.36 OIL ALL Heavy Liquid Valves 8.40E-06 0.19 0.19 OIL ALL Light Liquid Connectors 1.90E-04 0.90 1.11 OIL ALL Light Liquid Control Valves 1.75E-02 0.44 0.44 OIL ALL Light Liquid Open-Ended Lines 3.73E-03 0.79 1.27 OIL ALL Light Liquid Pressure Relief Valves 7.50E-02 0.80 0.80 OIL ALL Light Liquid Pump Seals 2.32E-02 0.74 1.36 OIL ALL Light Liquid Valves 1.21E-03 0.19 0.19

53

Table 5.3 provides a summary of published emission factors for estimating combustion emissions from natural gas fired heaters/boilers, reciprocating engines and gas turbines, diesel fuelled reciprocating engines and heaters and propane fuelled heaters. The factors are compiled from a variety of sources including U.S. EPA, manufacturer’s data and test data. Refer to Section 3.0 of Volumes 3 and 4 for a description of how these factors are used. A brief description of each of the fields in the table follows:

• Factor – an unique identifier used to specify a particular emission factor set within the emission calculation database.

• Equipment Type – an identifier used to indicate the general category of combustion device. The current combustion types are: HEAT (heaters/boilers), RECIP (reciprocating engines), TURB (gas turbine drivers), DSEL (diesel fuelled reciprocating engines) and FL (flares).

• Identifier 1, 2 and 3 – specifies the types of equipment and conditions for which the particular factor is applicable.

• Fuel Type – the type of fuel the combustion device consumes. The available types are: NGAS (natural gas), DIESEL (diesel fuel), and PROPANE (liquid propane).

• Factor Reference – a reference for the source of each emission factor. • Year – the year the emission factor was published. • CAS Number (Chemical Abstracts Number) – a code that can be used to uniquely

identify a particular compound. Fictitious CAS numbers of the form CEL0001 have been assigned to compounds for which no CAS Number exists (e.g., TPM, PM10, PM2.5, NOx, VOC, etc).

• Compound – the name of the compound. • Emission Factor – the average emission factor in ng/J of fuel input (on a gross or higher

heating value basis). • Lower and Upper Uncertainties – these values are fractions greater than zero that provide

an indication of the variability in the presented data. They are the 95 percent confidence limits on the average emission factor.

• Uncertainty Reference – provides a reference for the presented uncertainty values. The codes refer to references listed after the last page of the table.

54

Table 3.3 Compilation of combustion emission factors for estimating GHG and CAC emissions.

Fact

or

Equ

ipm

ent

Typ

e

Identifier 1 Identifier 2 Identifier 3 Fuel Type

Factor Reference Y

ear CAS

Number Compound Emission

Factor (ng/J) L

ower

U

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ty

Upp

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Unc

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U

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Ref

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0001 HEAT <29 MW NGAS U.S. EPA AP-42 1998 10024-97-2 N2O 0.9 0.18 5.45 3 0001 HEAT <29 MW NGAS U.S. EPA AP-42 1998 630-08-0 CO 35 0.96 0.96 1 0001 HEAT <29 MW NGAS U.S. EPA AP-42 1998 74-82-8 CH4 1 1.00 1.00 3 0001 HEAT <29 MW NGAS U.S. EPA AP-42 1998 CEL0002 NOx 42 0.18 0.18 1 0001 HEAT <29 MW NGAS U.S. EPA AP-42 1998 CEL0003 TPM 0.8 0.50 0.50 5 0001 HEAT <29 MW NGAS U.S. EPA AP-42 1998 CEL0004 PM10 0.8 0.50 0.50 5 0001 HEAT <29 MW NGAS U.S. EPA AP-42 1998 CEL0005 PM2.5 0.8 0.50 0.50 5 0001 HEAT <29 MW NGAS U.S. EPA AP-42 1998 CEL0006 VOC 2.3 0.52 1.91 1 0001 HEAT <29 MW NGAS U.S. EPA AP-42 1998 CEL0007 THC 4.6 0.54 1.86 1 0002 HEAT <29 MW Low NOx NGAS U.S. EPA AP-42 1998 10024-97-2 N2O 0.3 0.18 5.45 3 0002 HEAT <29 MW Low NOx NGAS U.S. EPA AP-42 1998 630-08-0 CO 35 0.96 0.96 1 0002 HEAT <29 MW Low NOx NGAS U.S. EPA AP-42 1998 74-82-8 CH4 1 1.00 1.00 3 0002 HEAT <29 MW Low NOx NGAS U.S. EPA AP-42 1998 CEL0002 NOx 21 0.18 0.18 1 0002 HEAT <29 MW Low NOx NGAS U.S. EPA AP-42 1998 CEL0003 TPM 0.8 0.50 0.50 5 0002 HEAT <29 MW Low NOx NGAS U.S. EPA AP-42 1998 CEL0004 PM10 0.8 0.50 0.50 5 0002 HEAT <29 MW Low NOx NGAS U.S. EPA AP-42 1998 CEL0005 PM2.5 0.8 0.50 0.50 5 0002 HEAT <29 MW Low NOx NGAS U.S. EPA AP-42 1998 CEL0006 VOC 2.3 0.52 1.91 1 0002 HEAT <29 MW Low NOx NGAS U.S. EPA AP-42 1998 CEL0007 THC 4.6 0.54 1.86 1 0003 HEAT <29 MW Low NOx/FGR NGAS U.S. EPA AP-42 1998 10024-97-2 N2O 0.3 0.18 5.45 3 0003 HEAT <29 MW Low NOx/FGR NGAS U.S. EPA AP-42 1998 630-08-0 CO 35 0.96 0.96 1 0003 HEAT <29 MW Low NOx/FGR NGAS U.S. EPA AP-42 1998 74-82-8 CH4 1 1.00 1.00 3 0003 HEAT <29 MW Low NOx/FGR NGAS U.S. EPA AP-42 1998 CEL0002 NOx 13 0.18 0.18 1 0003 HEAT <29 MW Low NOx/FGR NGAS U.S. EPA AP-42 1998 CEL0003 TPM 0.8 0.50 0.50 5 0003 HEAT <29 MW Low NOx/FGR NGAS U.S. EPA AP-42 1998 CEL0004 PM10 0.8 0.50 0.50 5 0003 HEAT <29 MW Low NOx/FGR NGAS U.S. EPA AP-42 1998 CEL0005 PM2.5 0.8 0.50 0.50 5 0003 HEAT <29 MW Low NOx/FGR NGAS U.S. EPA AP-42 1998 CEL0006 VOC 2.3 0.52 1.91 1 0003 HEAT <29 MW Low NOx/FGR NGAS U.S. EPA AP-42 1998 CEL0007 THC 4.6 0.54 1.86 1

0004 HEAT >29 MW Flue Gas Recirculation NGAS U.S. EPA AP-42 1998 10024-97-2 N2O 0.9 0.18 5.45 3

0004 HEAT >29 MW Flue Gas Recirculation NGAS U.S. EPA AP-42 1998 630-08-0 CO 35 0.96 0.96 1

0004 HEAT >29 MW Flue Gas Recirculation NGAS U.S. EPA AP-42 1998 74-82-8 CH4 1 1.00 1.00 3

0004 HEAT >29 MW Flue Gas NGAS U.S. EPA AP-42 1998 CEL0002 NOx 42 0.18 0.18 1

55

Table 3.3 Compilation of combustion emission factors for estimating GHG and CAC emissions.

Fact

or

Equ

ipm

ent

Typ

e

Identifier 1 Identifier 2 Identifier 3 Fuel Type

Factor Reference Y

ear CAS

Number Compound Emission

Factor (ng/J) L

ower

U

ncer

tain

ty

Upp

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Unc

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U

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Ref

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Recirculation

0004 HEAT >29 MW Flue Gas Recirculation NGAS U.S. EPA AP-42 1998 CEL0003 TPM 0.8 0.50 0.50 5

0004 HEAT >29 MW Flue Gas Recirculation NGAS U.S. EPA AP-42 1998 CEL0004 PM10 0.8 0.50 0.50 5

0004 HEAT >29 MW Flue Gas Recirculation NGAS U.S. EPA AP-42 1998 CEL0005 PM2.5 0.8 0.50 0.50 5

0004 HEAT >29 MW Flue Gas Recirculation NGAS U.S. EPA AP-42 1998 CEL0006 VOC 2.3 0.52 1.91 1

0004 HEAT >29 MW Flue Gas Recirculation NGAS U.S. EPA AP-42 1998 CEL0007 THC 4.6 0.54 1.86 1

0005 HEAT >29 MW Low NOx NGAS U.S. EPA AP-42 1998 10024-97-2 N2O 0.3 0.18 5.45 3 0005 HEAT >29 MW Low NOx NGAS U.S. EPA AP-42 1998 630-08-0 CO 35 0.96 0.96 1 0005 HEAT >29 MW Low NOx NGAS U.S. EPA AP-42 1998 74-82-8 CH4 1 1.00 1.00 3 0005 HEAT >29 MW Low NOx NGAS U.S. EPA AP-42 1998 CEL0002 NOx 59 0.18 0.18 1 0005 HEAT >29 MW Low NOx NGAS U.S. EPA AP-42 1998 CEL0003 TPM 0.8 0.50 0.50 5 0005 HEAT >29 MW Low NOx NGAS U.S. EPA AP-42 1998 CEL0004 PM10 0.8 0.50 0.50 5 0005 HEAT >29 MW Low NOx NGAS U.S. EPA AP-42 1998 CEL0005 PM2.5 0.8 0.50 0.50 5 0005 HEAT >29 MW Low NOx NGAS U.S. EPA AP-42 1998 CEL0006 VOC 2.3 0.52 1.91 1 0005 HEAT >29 MW Low NOx NGAS U.S. EPA AP-42 1998 CEL0007 THC 4.6 0.54 1.86 1

0006 HEAT >29 MW Uncontrolled (Post-NSPS) NGAS U.S. EPA AP-42 1998 10024-97-2 N2O 0.9 0.18 5.45 3

0006 HEAT >29 MW Uncontrolled (Post-NSPS) NGAS U.S. EPA AP-42 1998 630-08-0 CO 35 0.96 0.96 1

0006 HEAT >29 MW Uncontrolled (Post-NSPS) NGAS U.S. EPA AP-42 1998 74-82-8 CH4 1 1.00 1.00 3

0006 HEAT >29 MW Uncontrolled (Post-NSPS) NGAS U.S. EPA AP-42 1998 CEL0002 NOx 80 0.18 0.18 1

0006 HEAT >29 MW Uncontrolled (Post-NSPS) NGAS U.S. EPA AP-42 1998 CEL0003 TPM 0.8 0.50 0.50 5

0006 HEAT >29 MW Uncontrolled (Post-NSPS) NGAS U.S. EPA AP-42 1998 CEL0004 PM10 0.8 0.50 0.50 5

0006 HEAT >29 MW Uncontrolled (Post-NSPS) NGAS U.S. EPA AP-42 1998 CEL0005 PM2.5 0.8 0.50 0.50 5

0006 HEAT >29 MW Uncontrolled (Post-NSPS) NGAS U.S. EPA AP-42 1998 CEL0006 VOC 2.3 0.52 1.91 1

56

Table 3.3 Compilation of combustion emission factors for estimating GHG and CAC emissions.

Fact

or

Equ

ipm

ent

Typ

e

Identifier 1 Identifier 2 Identifier 3 Fuel Type

Factor Reference Y

ear CAS

Number Compound Emission

Factor (ng/J) L

ower

U

ncer

tain

ty

Upp

er

Unc

erta

inty

U

ncer

tain

ty

Ref

eren

ce

0006 HEAT >29 MW Uncontrolled (Post-NSPS) NGAS U.S. EPA AP-42 1998 CEL0007 THC 4.6 0.54 1.86 1

0007 HEAT >29 MW Uncontrolled (Pre-NSPS) NGAS U.S. EPA AP-42 1998 10024-97-2 N2O 0.9 0.18 5.45 3

0007 HEAT >29 MW Uncontrolled (Pre-NSPS) NGAS U.S. EPA AP-42 1998 630-08-0 CO 35 0.96 0.96 1

0007 HEAT >29 MW Uncontrolled (Pre-NSPS) NGAS U.S. EPA AP-42 1998 74-82-8 CH4 1 1.00 1.00 3

0007 HEAT >29 MW Uncontrolled (Pre-NSPS) NGAS U.S. EPA AP-42 1998 CEL0002 NOx 118 0.18 0.18 1

0007 HEAT >29 MW Uncontrolled (Pre-NSPS) NGAS U.S. EPA AP-42 1998 CEL0003 TPM 0.8 0.50 0.50 5

0007 HEAT >29 MW Uncontrolled (Pre-NSPS) NGAS U.S. EPA AP-42 1998 CEL0004 PM10 0.8 0.50 0.50 5

0007 HEAT >29 MW Uncontrolled (Pre-NSPS) NGAS U.S. EPA AP-42 1998 CEL0005 PM2.5 0.8 0.50 0.50 5

0007 HEAT >29 MW Uncontrolled (Pre-NSPS) NGAS U.S. EPA AP-42 1998 CEL0006 VOC 2.3 0.52 1.91 1

0007 HEAT >29 MW Uncontrolled (Pre-NSPS) NGAS U.S. EPA AP-42 1998 CEL0007 THC 4.6 0.54 1.86 1

0008 HEAT Residential Furnace NGAS U.S. EPA AP-42 1998 10024-97-2 N2O 0.9 0.18 5.45 3

0008 HEAT Residential Furnace NGAS U.S. EPA AP-42 1998 630-08-0 CO 17 0.96 0.96 1

0008 HEAT Residential Furnace NGAS U.S. EPA AP-42 1998 74-82-8 CH4 1 1.00 1.00 3

0008 HEAT Residential Furnace NGAS U.S. EPA AP-42 1998 CEL0002 NOx 40 0.18 0.18 1

0008 HEAT Residential Furnace NGAS U.S. EPA AP-42 1998 CEL0003 TPM 0.8 0.50 0.50 5

0008 HEAT Residential Furnace NGAS U.S. EPA AP-42 1998 CEL0004 PM10 0.8 0.50 0.50 5

0008 HEAT Residential Furnace NGAS U.S. EPA AP-42 1998 CEL0005 PM2.5 0.8 0.50 0.50 5

0008 HEAT Residential Furnace NGAS U.S. EPA AP-42 1998 CEL0006 VOC 2.3 0.52 1.91 1

57

Table 3.3 Compilation of combustion emission factors for estimating GHG and CAC emissions.

Fact

or

Equ

ipm

ent

Typ

e

Identifier 1 Identifier 2 Identifier 3 Fuel Type

Factor Reference Y

ear CAS

Number Compound Emission

Factor (ng/J) L

ower

U

ncer

tain

ty

Upp

er

Unc

erta

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U

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Ref

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ce

0008 HEAT Residential Furnace NGAS U.S. EPA AP-42 1998 CEL0007 THC 4.6 0.54 1.86 1

0009 HEAT Tangential NGAS U.S. EPA AP-42 1998 10024-97-2 N2O 0.9 0.18 5.45 3 0009 HEAT Tangential NGAS U.S. EPA AP-42 1998 630-08-0 CO 10 0.96 0.96 1 0009 HEAT Tangential NGAS U.S. EPA AP-42 1998 74-82-8 CH4 1 1.00 1.00 3 0009 HEAT Tangential NGAS U.S. EPA AP-42 1998 CEL0002 NOx 72 0.18 0.18 1 0009 HEAT Tangential NGAS U.S. EPA AP-42 1998 CEL0003 TPM 0.8 0.50 0.50 5 0009 HEAT Tangential NGAS U.S. EPA AP-42 1998 CEL0004 PM10 0.8 0.50 0.50 5 0009 HEAT Tangential NGAS U.S. EPA AP-42 1998 CEL0005 PM2.5 0.8 0.50 0.50 5 0009 HEAT Tangential NGAS U.S. EPA AP-42 1998 CEL0006 VOC 2.3 0.52 1.91 1 0009 HEAT Tangential NGAS U.S. EPA AP-42 1998 CEL0007 THC 4.6 0.54 1.86 1 0010 HEAT Tangential FGR NGAS U.S. EPA AP-42 1998 10024-97-2 N2O 0.3 0.18 5.45 3 0010 HEAT Tangential FGR NGAS U.S. EPA AP-42 1998 630-08-0 CO 41 0.96 0.96 1 0010 HEAT Tangential FGR NGAS U.S. EPA AP-42 1998 74-82-8 CH4 1 1.00 1.00 3 0010 HEAT Tangential FGR NGAS U.S. EPA AP-42 1998 CEL0002 NOx 32 0.18 0.18 1 0010 HEAT Tangential FGR NGAS U.S. EPA AP-42 1998 CEL0003 TPM 0.8 0.50 0.50 5 0010 HEAT Tangential FGR NGAS U.S. EPA AP-42 1998 CEL0004 PM10 0.8 0.50 0.50 5 0010 HEAT Tangential FGR NGAS U.S. EPA AP-42 1998 CEL0005 PM2.5 0.8 0.50 0.50 5 0010 HEAT Tangential FGR NGAS U.S. EPA AP-42 1998 CEL0006 VOC 2.3 0.52 1.91 1 0010 HEAT Tangential FGR NGAS U.S. EPA AP-42 1998 CEL0007 THC 4.6 0.54 1.86 1 0011 RECIP 2-Stroke Lean Burn 90-105% Load NGAS CHEMEX Labs 1996 10024-97-2 N2O 5.72 0.18 5.45 3 0011 RECIP 2-Stroke Lean Burn 90-105% Load NGAS U.S. EPA AP-42 2000 630-08-0 CO 166 0.34 0.34 1 0011 RECIP 2-Stroke Lean Burn 90-105% Load NGAS U.S. EPA AP-42 2000 74-82-8 CH4 624 0.59 0.59 1 0011 RECIP 2-Stroke Lean Burn 90-105% Load NGAS U.S. EPA AP-42 2000 CEL0002 NOx 1363 0.09 0.09 1 0011 RECIP 2-Stroke Lean Burn 90-105% Load NGAS U.S. EPA AP-42 2000 CEL0003 TPM 16.5 1.00 1.00 6 0011 RECIP 2-Stroke Lean Burn 90-105% Load NGAS U.S. EPA AP-42 2000 CEL0004 PM10 16.5 1.00 1.00 6 0011 RECIP 2-Stroke Lean Burn 90-105% Load NGAS U.S. EPA AP-42 2000 CEL0005 PM2.5 16.5 1.00 1.00 6 0011 RECIP 2-Stroke Lean Burn 90-105% Load NGAS U.S. EPA AP-42 2000 CEL0006 VOC 52 0.27 0.27 1 0011 RECIP 2-Stroke Lean Burn 90-105% Load NGAS U.S. EPA AP-42 2000 CEL0007 THC 705 0.51 0.51 1 0012 RECIP 2-Stroke Lean Burn <90% Load NGAS CHEMEX Labs 1996 10024-97-2 N2O 5.72 0.18 5.45 3 0012 RECIP 2-Stroke Lean Burn <90% Load NGAS U.S. EPA AP-42 2000 630-08-0 CO 152 0.34 0.34 1 0012 RECIP 2-Stroke Lean Burn <90% Load NGAS U.S. EPA AP-42 2000 74-82-8 CH4 624 0.59 0.59 1 0012 RECIP 2-Stroke Lean Burn <90% Load NGAS U.S. EPA AP-42 2000 CEL0002 NOx 834 0.09 0.09 1 0012 RECIP 2-Stroke Lean Burn <90% Load NGAS U.S. EPA AP-42 2000 CEL0003 TPM 16.5 1.00 1.00 6 0012 RECIP 2-Stroke Lean Burn <90% Load NGAS U.S. EPA AP-42 2000 CEL0004 PM10 16.5 1.00 1.00 6

58

Table 3.3 Compilation of combustion emission factors for estimating GHG and CAC emissions.

Fact

or

Equ

ipm

ent

Typ

e

Identifier 1 Identifier 2 Identifier 3 Fuel Type

Factor Reference Y

ear CAS

Number Compound Emission

Factor (ng/J) L

ower

U

ncer

tain

ty

Upp

er

Unc

erta

inty

U

ncer

tain

ty

Ref

eren

ce

0012 RECIP 2-Stroke Lean Burn <90% Load NGAS U.S. EPA AP-42 2000 CEL0005 PM2.5 16.5 1.00 1.00 6 0012 RECIP 2-Stroke Lean Burn <90% Load NGAS U.S. EPA AP-42 2000 CEL0006 VOC 52 0.27 0.27 1 0012 RECIP 2-Stroke Lean Burn <90% Load NGAS U.S. EPA AP-42 2000 CEL0007 THC 705 0.51 0.51 1 0013 RECIP 4-Stroke Lean Burn 90-105% Load NGAS CHEMEX Labs 1996 10024-97-2 N2O 5.72 0.18 5.45 3 0013 RECIP 4-Stroke Lean Burn 90-105% Load NGAS U.S. EPA AP-42 2000 630-08-0 CO 136 0.34 0.34 1 0013 RECIP 4-Stroke Lean Burn 90-105% Load NGAS U.S. EPA AP-42 2000 74-82-8 CH4 538 0.59 0.59 1 0013 RECIP 4-Stroke Lean Burn 90-105% Load NGAS U.S. EPA AP-42 2000 CEL0002 NOx 1754 0.09 0.09 1 0013 RECIP 4-Stroke Lean Burn 90-105% Load NGAS U.S. EPA AP-42 2000 CEL0003 TPM 0.0332 0.67 1.50 7 0013 RECIP 4-Stroke Lean Burn 90-105% Load NGAS U.S. EPA AP-42 2000 CEL0004 PM10 0.0332 0.67 1.50 7 0013 RECIP 4-Stroke Lean Burn 90-105% Load NGAS U.S. EPA AP-42 2000 CEL0005 PM2.5 0.0332 0.67 1.50 7 0013 RECIP 4-Stroke Lean Burn 90-105% Load NGAS U.S. EPA AP-42 2000 CEL0006 VOC 51 0.27 0.27 1 0013 RECIP 4-Stroke Lean Burn 90-105% Load NGAS U.S. EPA AP-42 2000 CEL0007 THC 632 0.51 0.51 1 0014 RECIP 4-Stroke Lean Burn <90% Load NGAS CHEMEX Labs 1996 10024-97-2 N2O 5.72 0.18 5.45 3 0014 RECIP 4-Stroke Lean Burn <90% Load NGAS U.S. EPA AP-42 2000 630-08-0 CO 240 0.34 0.34 1 0014 RECIP 4-Stroke Lean Burn <90% Load NGAS U.S. EPA AP-42 2000 74-82-8 CH4 538 0.59 0.59 1 0014 RECIP 4-Stroke Lean Burn <90% Load NGAS U.S. EPA AP-42 2000 CEL0002 NOx 364 0.09 0.09 1 0014 RECIP 4-Stroke Lean Burn <90% Load NGAS U.S. EPA AP-42 2000 CEL0003 TPM 0.0332 0.67 1.50 7 0014 RECIP 4-Stroke Lean Burn <90% Load NGAS U.S. EPA AP-42 2000 CEL0004 PM10 0.0332 0.67 1.50 7 0014 RECIP 4-Stroke Lean Burn <90% Load NGAS U.S. EPA AP-42 2000 CEL0005 PM2.5 0.0332 0.67 1.50 7 0014 RECIP 4-Stroke Lean Burn <90% Load NGAS U.S. EPA AP-42 2000 CEL0006 VOC 51 0.27 0.27 1 0014 RECIP 4-Stroke Lean Burn <90% Load NGAS U.S. EPA AP-42 2000 CEL0007 THC 632 0.51 0.51 1 0015 RECIP 4-Stroke Rich Burn 90-105% Load NGAS CHEMEX Labs 1996 10024-97-2 N2O 5.72 0.18 5.45 3 0015 RECIP 4-Stroke Rich Burn 90-105% Load NGAS U.S. EPA AP-42 2000 630-08-0 CO 1600 0.34 0.34 1 0015 RECIP 4-Stroke Rich Burn 90-105% Load NGAS U.S. EPA AP-42 2000 74-82-8 CH4 99 0.59 0.59 1 0015 RECIP 4-Stroke Rich Burn 90-105% Load NGAS U.S. EPA AP-42 2000 CEL0002 NOx 950 0.09 0.09 1 0015 RECIP 4-Stroke Rich Burn 90-105% Load NGAS U.S. EPA AP-42 2000 CEL0003 TPM 4.09 0.50 2.00 8 0015 RECIP 4-Stroke Rich Burn 90-105% Load NGAS U.S. EPA AP-42 2000 CEL0004 PM10 4.09 0.50 2.00 8 0015 RECIP 4-Stroke Rich Burn 90-105% Load NGAS U.S. EPA AP-42 2000 CEL0005 PM2.5 4.09 0.50 2.00 8 0015 RECIP 4-Stroke Rich Burn 90-105% Load NGAS U.S. EPA AP-42 2000 CEL0006 VOC 12.7 0.27 0.27 1 0015 RECIP 4-Stroke Rich Burn 90-105% Load NGAS U.S. EPA AP-42 2000 CEL0007 THC 154 0.51 0.51 1 0016 RECIP 4-Stroke Rich Burn <90% Load NGAS CHEMEX Labs 1996 10024-97-2 N2O 5.72 0.18 5.45 3 0016 RECIP 4-Stroke Rich Burn <90% Load NGAS U.S. EPA AP-42 2000 630-08-0 CO 1509 0.34 0.34 1 0016 RECIP 4-Stroke Rich Burn <90% Load NGAS U.S. EPA AP-42 2000 74-82-8 CH4 99 0.59 0.59 1 0016 RECIP 4-Stroke Rich Burn <90% Load NGAS U.S. EPA AP-42 2000 CEL0002 NOx 976 0.09 0.09 1 0016 RECIP 4-Stroke Rich Burn <90% Load NGAS U.S. EPA AP-42 2000 CEL0003 TPM 4.09 0.50 2.00 8

59

Table 3.3 Compilation of combustion emission factors for estimating GHG and CAC emissions.

Fact

or

Equ

ipm

ent

Typ

e

Identifier 1 Identifier 2 Identifier 3 Fuel Type

Factor Reference Y

ear CAS

Number Compound Emission

Factor (ng/J) L

ower

U

ncer

tain

ty

Upp

er

Unc

erta

inty

U

ncer

tain

ty

Ref

eren

ce

0016 RECIP 4-Stroke Rich Burn <90% Load NGAS U.S. EPA AP-42 2000 CEL0004 PM10 4.09 0.50 2.00 8 0016 RECIP 4-Stroke Rich Burn <90% Load NGAS U.S. EPA AP-42 2000 CEL0005 PM2.5 4.09 0.50 2.00 8 0016 RECIP 4-Stroke Rich Burn <90% Load NGAS U.S. EPA AP-42 2000 CEL0006 VOC 12.7 0.27 0.27 1 0016 RECIP 4-Stroke Rich Burn <90% Load NGAS U.S. EPA AP-42 2000 CEL0007 THC 154 0.51 0.51 1

0017 RECIP Caterpillar G3304-NA - 10.5:1 NGAS CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0017 RECIP Caterpillar G3304-NA - 10.5:1 NGAS Manufacturer 2003 630-08-0 CO 97 0.34 0.34 1 0017 RECIP Caterpillar G3304-NA - 10.5:1 NGAS Manufacturer 2003 74-82-8 CH4 185 0.59 0.59 1 0017 RECIP Caterpillar G3304-NA - 10.5:1 NGAS Manufacturer 2003 CEL0002 NOx 1767 0.09 0.09 1

0017 RECIP Caterpillar G3304-NA - 10.5:1 NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

0017 RECIP Caterpillar G3304-NA - 10.5:1 NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

0017 RECIP Caterpillar G3304-NA - 10.5:1 NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

0017 RECIP Caterpillar G3304-NA - 10.5:1 NGAS Manufacturer 2003 CEL0006 VOC 34 0.27 0.27 1 0017 RECIP Caterpillar G3304-NA - 10.5:1 NGAS Manufacturer 2003 CEL0007 THC 219 0.51 0.51 1

0018 RECIP Caterpillar G3304-NA - 8:1 NGAS CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0018 RECIP Caterpillar G3304-NA - 8:1 NGAS Manufacturer 2003 630-08-0 CO 88 0.34 0.34 1 0018 RECIP Caterpillar G3304-NA - 8:1 NGAS Manufacturer 2003 74-82-8 CH4 173 0.59 0.59 1 0018 RECIP Caterpillar G3304-NA - 8:1 NGAS Manufacturer 2003 CEL0002 NOx 1640 0.09 0.09 1

0018 RECIP Caterpillar G3304-NA - 8:1 NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

0018 RECIP Caterpillar G3304-NA - 8:1 NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

0018 RECIP Caterpillar G3304-NA - 8:1 NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

0018 RECIP Caterpillar G3304-NA - 8:1 NGAS Manufacturer 2003 CEL0006 VOC 30 0.27 0.27 1 0018 RECIP Caterpillar G3304-NA - 8:1 NGAS Manufacturer 2003 CEL0007 THC 204 0.51 0.51 1

0019 RECIP Caterpillar G3306-130 - 10.5:1 - Catalyst NGAS

CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0019 RECIP Caterpillar G3306-130 - 10.5:1 - Catalyst NGAS Manufacturer 2003 630-08-0 CO 1371 0.34 0.34 1

0019 RECIP Caterpillar G3306-130 - 10.5:1 - Catalyst NGAS Manufacturer 2003 74-82-8 CH4 124 0.59 0.59 1

60

Table 3.3 Compilation of combustion emission factors for estimating GHG and CAC emissions.

Fact

or

Equ

ipm

ent

Typ

e

Identifier 1 Identifier 2 Identifier 3 Fuel Type

Factor Reference Y

ear CAS

Number Compound Emission

Factor (ng/J) L

ower

U

ncer

tain

ty

Upp

er

Unc

erta

inty

U

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tain

ty

Ref

eren

ce

0019 RECIP Caterpillar G3306-130 - 10.5:1 - Catalyst NGAS Manufacturer 2003 CEL0002 NOx 1184 0.09 0.09 1

0019 RECIP Caterpillar G3306-130 - 10.5:1 - Catalyst NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

0019 RECIP Caterpillar G3306-130 - 10.5:1 - Catalyst NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

0019 RECIP Caterpillar G3306-130 - 10.5:1 - Catalyst NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

0019 RECIP Caterpillar G3306-130 - 10.5:1 - Catalyst NGAS Manufacturer 2003 CEL0006 VOC 21 0.27 0.27 1

0019 RECIP Caterpillar G3306-130 - 10.5:1 - Catalyst NGAS Manufacturer 2003 CEL0007 THC 145 0.51 0.51 1

0020 RECIP Caterpillar G3306-130 - 10.5:1 - Standard NGAS

CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0020 RECIP Caterpillar G3306-130 - 10.5:1 - Standard NGAS Manufacturer 2003 630-08-0 CO 83 0.34 0.34 1

0020 RECIP Caterpillar G3306-130 - 10.5:1 - Standard NGAS Manufacturer 2003 74-82-8 CH4 95 0.59 0.59 1

0020 RECIP Caterpillar G3306-130 - 10.5:1 - Standard NGAS Manufacturer 2003 CEL0002 NOx 2015 0.09 0.09 1

0020 RECIP Caterpillar G3306-130 - 10.5:1 - Standard NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

0020 RECIP Caterpillar G3306-130 - 10.5:1 - Standard NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

0020 RECIP Caterpillar G3306-130 - 10.5:1 - Standard NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

0020 RECIP Caterpillar G3306-130 - 10.5:1 - Standard NGAS Manufacturer 2003 CEL0006 VOC 17 0.27 0.27 1

0020 RECIP Caterpillar G3306-130 - 10.5:1 - Standard NGAS Manufacturer 2003 CEL0007 THC 111 0.51 0.51 1

0021 RECIP Caterpillar G3306-130 - 8:1 - Catalyst NGAS

CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0021 RECIP Caterpillar G3306-130 - 8:1 - Catalyst NGAS Manufacturer 2003 630-08-0 CO 1620 0.34 0.34 1

0021 RECIP Caterpillar G3306-130 - 8:1 - Catalyst NGAS Manufacturer 2003 74-82-8 CH4 96 0.59 0.59 1

61

Table 3.3 Compilation of combustion emission factors for estimating GHG and CAC emissions.

Fact

or

Equ

ipm

ent

Typ

e

Identifier 1 Identifier 2 Identifier 3 Fuel Type

Factor Reference Y

ear CAS

Number Compound Emission

Factor (ng/J) L

ower

U

ncer

tain

ty

Upp

er

Unc

erta

inty

U

ncer

tain

ty

Ref

eren

ce

0021 RECIP Caterpillar G3306-130 - 8:1 - Catalyst NGAS Manufacturer 2003 CEL0002 NOx 1371 0.09 0.09 1

0021 RECIP Caterpillar G3306-130 - 8:1 - Catalyst NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

0021 RECIP Caterpillar G3306-130 - 8:1 - Catalyst NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

0021 RECIP Caterpillar G3306-130 - 8:1 - Catalyst NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

0021 RECIP Caterpillar G3306-130 - 8:1 - Catalyst NGAS Manufacturer 2003 CEL0006 VOC 16 0.27 0.27 1

0021 RECIP Caterpillar G3306-130 - 8:1 - Catalyst NGAS Manufacturer 2003 CEL0007 THC 112 0.51 0.51 1

0022 RECIP Caterpillar G3306-130 - 8:1 - Standard NGAS

CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0022 RECIP Caterpillar G3306-130 - 8:1 - Standard NGAS Manufacturer 2003 630-08-0 CO 71 0.34 0.34 1

0022 RECIP Caterpillar G3306-130 - 8:1 - Standard NGAS Manufacturer 2003 74-82-8 CH4 70 0.59 0.59 1

0022 RECIP Caterpillar G3306-130 - 8:1 - Standard NGAS Manufacturer 2003 CEL0002 NOx 2454 0.09 0.09 1

0022 RECIP Caterpillar G3306-130 - 8:1 - Standard NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

0022 RECIP Caterpillar G3306-130 - 8:1 - Standard NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

0022 RECIP Caterpillar G3306-130 - 8:1 - Standard NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

0022 RECIP Caterpillar G3306-130 - 8:1 - Standard NGAS Manufacturer 2003 CEL0006 VOC 13 0.27 0.27 1

0022 RECIP Caterpillar G3306-130 - 8:1 - Standard NGAS Manufacturer 2003 CEL0007 THC 83 0.51 0.51 1

0023 RECIP Caterpillar G3306-90 - 10.5:1 - Catalyst NGAS

CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0023 RECIP Caterpillar G3306-90 - 10.5:1 - Catalyst NGAS Manufacturer 2003 630-08-0 CO 1380 0.34 0.34 1

0023 RECIP Caterpillar G3306-90 - 10.5:1 - Catalyst NGAS Manufacturer 2003 74-82-8 CH4 133 0.59 0.59 1

62

Table 3.3 Compilation of combustion emission factors for estimating GHG and CAC emissions.

Fact

or

Equ

ipm

ent

Typ

e

Identifier 1 Identifier 2 Identifier 3 Fuel Type

Factor Reference Y

ear CAS

Number Compound Emission

Factor (ng/J) L

ower

U

ncer

tain

ty

Upp

er

Unc

erta

inty

U

ncer

tain

ty

Ref

eren

ce

0023 RECIP Caterpillar G3306-90 - 10.5:1 - Catalyst NGAS Manufacturer 2003 CEL0002 NOx 1084 0.09 0.09 1

0023 RECIP Caterpillar G3306-90 - 10.5:1 - Catalyst NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

0023 RECIP Caterpillar G3306-90 - 10.5:1 - Catalyst NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

0023 RECIP Caterpillar G3306-90 - 10.5:1 - Catalyst NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

0023 RECIP Caterpillar G3306-90 - 10.5:1 - Catalyst NGAS Manufacturer 2003 CEL0006 VOC 22 0.27 0.27 1

0023 RECIP Caterpillar G3306-90 - 10.5:1 - Catalyst NGAS Manufacturer 2003 CEL0007 THC 155 0.51 0.51 1

0024 RECIP Caterpillar G3306-90 - 10.5:1 - Standard NGAS

CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0024 RECIP Caterpillar G3306-90 - 10.5:1 - Standard NGAS Manufacturer 2003 630-08-0 CO 79 0.34 0.34 1

0024 RECIP Caterpillar G3306-90 - 10.5:1 - Standard NGAS Manufacturer 2003 74-82-8 CH4 106 0.59 0.59 1

0024 RECIP Caterpillar G3306-90 - 10.5:1 - Standard NGAS Manufacturer 2003 CEL0002 NOx 1900 0.09 0.09 1

0024 RECIP Caterpillar G3306-90 - 10.5:1 - Standard NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

0024 RECIP Caterpillar G3306-90 - 10.5:1 - Standard NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

0024 RECIP Caterpillar G3306-90 - 10.5:1 - Standard NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

0024 RECIP Caterpillar G3306-90 - 10.5:1 - Standard NGAS Manufacturer 2003 CEL0006 VOC 18 0.27 0.27 1

0024 RECIP Caterpillar G3306-90 - 10.5:1 - Standard NGAS Manufacturer 2003 CEL0007 THC 124 0.51 0.51 1

0025 RECIP Caterpillar G3306-90 - 8:1 - Catalyst NGAS

CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0025 RECIP Caterpillar G3306-90 - 8:1 - Catalyst NGAS Manufacturer 2003 630-08-0 CO 1663 0.34 0.34 1

0025 RECIP Caterpillar G3306-90 - 8:1 - Catalyst NGAS Manufacturer 2003 74-82-8 CH4 90 0.59 0.59 1

63

Table 3.3 Compilation of combustion emission factors for estimating GHG and CAC emissions.

Fact

or

Equ

ipm

ent

Typ

e

Identifier 1 Identifier 2 Identifier 3 Fuel Type

Factor Reference Y

ear CAS

Number Compound Emission

Factor (ng/J) L

ower

U

ncer

tain

ty

Upp

er

Unc

erta

inty

U

ncer

tain

ty

Ref

eren

ce

0025 RECIP Caterpillar G3306-90 - 8:1 - Catalyst NGAS Manufacturer 2003 CEL0002 NOx 1395 0.09 0.09 1

0025 RECIP Caterpillar G3306-90 - 8:1 - Catalyst NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

0025 RECIP Caterpillar G3306-90 - 8:1 - Catalyst NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

0025 RECIP Caterpillar G3306-90 - 8:1 - Catalyst NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

0025 RECIP Caterpillar G3306-90 - 8:1 - Catalyst NGAS Manufacturer 2003 CEL0006 VOC 16 0.27 0.27 1

0025 RECIP Caterpillar G3306-90 - 8:1 - Catalyst NGAS Manufacturer 2003 CEL0007 THC 107 0.51 0.51 1

0026 RECIP Caterpillar G3306-90 - 8:1 - Standard NGAS

CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0026 RECIP Caterpillar G3306-90 - 8:1 - Standard NGAS Manufacturer 2003 630-08-0 CO 71 0.34 0.34 1

0026 RECIP Caterpillar G3306-90 - 8:1 - Standard NGAS Manufacturer 2003 74-82-8 CH4 58 0.59 0.59 1

0026 RECIP Caterpillar G3306-90 - 8:1 - Standard NGAS Manufacturer 2003 CEL0002 NOx 2589 0.09 0.09 1

0026 RECIP Caterpillar G3306-90 - 8:1 - Standard NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

0026 RECIP Caterpillar G3306-90 - 8:1 - Standard NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

0026 RECIP Caterpillar G3306-90 - 8:1 - Standard NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

0026 RECIP Caterpillar G3306-90 - 8:1 - Standard NGAS Manufacturer 2003 CEL0006 VOC 11 0.27 0.27 1

0026 RECIP Caterpillar G3306-90 - 8:1 - Standard NGAS Manufacturer 2003 CEL0007 THC 69 0.51 0.51 1

0027 RECIP Caterpillar G3306-NA - 10.5:1 NGAS CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0027 RECIP Caterpillar G3306-NA - 10.5:1 NGAS Manufacturer 2003 630-08-0 CO 82 0.34 0.34 1 0027 RECIP Caterpillar G3306-NA - 10.5:1 NGAS Manufacturer 2003 74-82-8 CH4 172 0.59 0.59 1 0027 RECIP Caterpillar G3306-NA - 10.5:1 NGAS Manufacturer 2003 CEL0002 NOx 1788 0.09 0.09 1 0027 RECIP Caterpillar G3306-NA - 10.5:1 NGAS U.S. EPA AP-42 - 2000 CEL0003 TPM 4.09 0.50 2.00 8

64

Table 3.3 Compilation of combustion emission factors for estimating GHG and CAC emissions.

Fact

or

Equ

ipm

ent

Typ

e

Identifier 1 Identifier 2 Identifier 3 Fuel Type

Factor Reference Y

ear CAS

Number Compound Emission

Factor (ng/J) L

ower

U

ncer

tain

ty

Upp

er

Unc

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U

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Ref

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ce

> Profile: 0016

0027 RECIP Caterpillar G3306-NA - 10.5:1 NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

0027 RECIP Caterpillar G3306-NA - 10.5:1 NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

0027 RECIP Caterpillar G3306-NA - 10.5:1 NGAS Manufacturer 2003 CEL0006 VOC 30 0.27 0.27 1 0027 RECIP Caterpillar G3306-NA - 10.5:1 NGAS Manufacturer 2003 CEL0007 THC 203 0.51 0.51 1

0028 RECIP Caterpillar G3306-NA - 8:1 NGAS CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0028 RECIP Caterpillar G3306-NA - 8:1 NGAS Manufacturer 2003 630-08-0 CO 76 0.34 0.34 1 0028 RECIP Caterpillar G3306-NA - 8:1 NGAS Manufacturer 2003 74-82-8 CH4 167 0.59 0.59 1 0028 RECIP Caterpillar G3306-NA - 8:1 NGAS Manufacturer 2003 CEL0002 NOx 1408 0.09 0.09 1

0028 RECIP Caterpillar G3306-NA - 8:1 NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

0028 RECIP Caterpillar G3306-NA - 8:1 NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

0028 RECIP Caterpillar G3306-NA - 8:1 NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

0028 RECIP Caterpillar G3306-NA - 8:1 NGAS Manufacturer 2003 CEL0006 VOC 30 0.27 0.27 1 0028 RECIP Caterpillar G3306-NA - 8:1 NGAS Manufacturer 2003 CEL0007 THC 198 0.51 0.51 1

0029 RECIP Caterpillar G3406-HS 32 HCR NGAS CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0029 RECIP Caterpillar G3406-HS 32 HCR NGAS Manufacturer 2003 630-08-0 CO 82 0.34 0.34 1 0029 RECIP Caterpillar G3406-HS 32 HCR NGAS Manufacturer 2003 74-82-8 CH4 118 0.59 0.59 1 0029 RECIP Caterpillar G3406-HS 32 HCR NGAS Manufacturer 2003 CEL0002 NOx 2081 0.09 0.09 1

0029 RECIP Caterpillar G3406-HS 32 HCR NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

0029 RECIP Caterpillar G3406-HS 32 HCR NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

0029 RECIP Caterpillar G3406-HS 32 HCR NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

0029 RECIP Caterpillar G3406-HS 32 HCR NGAS Manufacturer 2003 CEL0006 VOC 24 0.27 0.27 1 0029 RECIP Caterpillar G3406-HS 32 HCR NGAS Manufacturer 2003 CEL0007 THC 141 0.51 0.51 1

0030 RECIP Caterpillar G3406-HS 32 LCR - Catalyst NGAS

CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0030 RECIP Caterpillar G3406-HS 32 LCR NGAS Manufacturer 2003 630-08-0 CO 1191 0.34 0.34 1

65

Table 3.3 Compilation of combustion emission factors for estimating GHG and CAC emissions.

Fact

or

Equ

ipm

ent

Typ

e

Identifier 1 Identifier 2 Identifier 3 Fuel Type

Factor Reference Y

ear CAS

Number Compound Emission

Factor (ng/J) L

ower

U

ncer

tain

ty

Upp

er

Unc

erta

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U

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ty

Ref

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ce

- Catalyst

0030 RECIP Caterpillar G3406-HS 32 LCR - Catalyst NGAS Manufacturer 2003 74-82-8 CH4 162 0.59 0.59 1

0030 RECIP Caterpillar G3406-HS 32 LCR - Catalyst NGAS Manufacturer 2003 CEL0002 NOx 1237 0.09 0.09 1

0030 RECIP Caterpillar G3406-HS 32 LCR - Catalyst NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

0030 RECIP Caterpillar G3406-HS 32 LCR - Catalyst NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

0030 RECIP Caterpillar G3406-HS 32 LCR - Catalyst NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

0030 RECIP Caterpillar G3406-HS 32 LCR - Catalyst NGAS Manufacturer 2003 CEL0006 VOC 35 0.27 0.27 1

0030 RECIP Caterpillar G3406-HS 32 LCR - Catalyst NGAS Manufacturer 2003 CEL0007 THC 197 0.51 0.51 1

0031 RECIP Caterpillar G3406-HS 32 LCR - Standard NGAS

CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0031 RECIP Caterpillar G3406-HS 32 LCR - Standard NGAS Manufacturer 2003 630-08-0 CO 60 0.34 0.34 1

0031 RECIP Caterpillar G3406-HS 32 LCR - Standard NGAS Manufacturer 2003 74-82-8 CH4 143 0.59 0.59 1

0031 RECIP Caterpillar G3406-HS 32 LCR - Standard NGAS Manufacturer 2003 CEL0002 NOx 2079 0.09 0.09 1

0031 RECIP Caterpillar G3406-HS 32 LCR - Standard NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

0031 RECIP Caterpillar G3406-HS 32 LCR - Standard NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

0031 RECIP Caterpillar G3406-HS 32 LCR - Standard NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

0031 RECIP Caterpillar G3406-HS 32 LCR - Standard NGAS Manufacturer 2003 CEL0006 VOC 24 0.27 0.27 1

0031 RECIP Caterpillar G3406-HS 32 LCR - Standard NGAS Manufacturer 2003 CEL0007 THC 167 0.51 0.51 1

0032 RECIP Caterpillar G3406-HS 54 HCR NGAS CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0032 RECIP Caterpillar G3406-HS 54 HCR NGAS Manufacturer 2003 630-08-0 CO 90 0.34 0.34 1

66

Table 3.3 Compilation of combustion emission factors for estimating GHG and CAC emissions.

Fact

or

Equ

ipm

ent

Typ

e

Identifier 1 Identifier 2 Identifier 3 Fuel Type

Factor Reference Y

ear CAS

Number Compound Emission

Factor (ng/J) L

ower

U

ncer

tain

ty

Upp

er

Unc

erta

inty

U

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ty

Ref

eren

ce

0032 RECIP Caterpillar G3406-HS 54 HCR NGAS Manufacturer 2003 74-82-8 CH4 112 0.59 0.59 1 0032 RECIP Caterpillar G3406-HS 54 HCR NGAS Manufacturer 2003 CEL0002 NOx 1869 0.09 0.09 1

0032 RECIP Caterpillar G3406-HS 54 HCR NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

0032 RECIP Caterpillar G3406-HS 54 HCR NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

0032 RECIP Caterpillar G3406-HS 54 HCR NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

0032 RECIP Caterpillar G3406-HS 54 HCR NGAS Manufacturer 2003 CEL0006 VOC 22 0.27 0.27 1 0032 RECIP Caterpillar G3406-HS 54 HCR NGAS Manufacturer 2003 CEL0007 THC 134 0.51 0.51 1

0033 RECIP Caterpillar G3406-HS 54 LCR - Catalyst NGAS

CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0033 RECIP Caterpillar G3406-HS 54 LCR - Catalyst NGAS Manufacturer 2003 630-08-0 CO 1274 0.34 0.34 1

0033 RECIP Caterpillar G3406-HS 54 LCR - Catalyst NGAS Manufacturer 2003 74-82-8 CH4 169 0.59 0.59 1

0033 RECIP Caterpillar G3406-HS 54 LCR - Catalyst NGAS Manufacturer 2003 CEL0002 NOx 1308 0.09 0.09 1

0033 RECIP Caterpillar G3406-HS 54 LCR - Catalyst NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

0033 RECIP Caterpillar G3406-HS 54 LCR - Catalyst NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

0033 RECIP Caterpillar G3406-HS 54 LCR - Catalyst NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

0033 RECIP Caterpillar G3406-HS 54 LCR - Catalyst NGAS Manufacturer 2003 CEL0006 VOC 34 0.27 0.27 1

0033 RECIP Caterpillar G3406-HS 54 LCR - Catalyst NGAS Manufacturer 2003 CEL0007 THC 203 0.51 0.51 1

0034 RECIP Caterpillar G3406-HS 54 LCR - Standard NGAS

CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0034 RECIP Caterpillar G3406-HS 54 LCR - Standard NGAS Manufacturer 2003 630-08-0 CO 59 0.34 0.34 1

0034 RECIP Caterpillar G3406-HS 54 LCR - Standard NGAS Manufacturer 2003 74-82-8 CH4 153 0.59 0.59 1

0034 RECIP Caterpillar G3406-HS 54 LCR - Standard NGAS Manufacturer 2003 CEL0002 NOx 2319 0.09 0.09 1

67

Table 3.3 Compilation of combustion emission factors for estimating GHG and CAC emissions.

Fact

or

Equ

ipm

ent

Typ

e

Identifier 1 Identifier 2 Identifier 3 Fuel Type

Factor Reference Y

ear CAS

Number Compound Emission

Factor (ng/J) L

ower

U

ncer

tain

ty

Upp

er

Unc

erta

inty

U

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tain

ty

Ref

eren

ce

0034 RECIP Caterpillar G3406-HS 54 LCR - Standard NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

0034 RECIP Caterpillar G3406-HS 54 LCR - Standard NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

0034 RECIP Caterpillar G3406-HS 54 LCR - Standard NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

0034 RECIP Caterpillar G3406-HS 54 LCR - Standard NGAS Manufacturer 2003 CEL0006 VOC 24 0.27 0.27 1

0034 RECIP Caterpillar G3406-HS 54 LCR - Standard NGAS Manufacturer 2003 CEL0007 THC 177 0.51 0.51 1

0035 RECIP Caterpillar G3406-LS 32 HCR NGAS CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0035 RECIP Caterpillar G3406-LS 32 HCR NGAS Manufacturer 2003 630-08-0 CO 71 0.34 0.34 1 0035 RECIP Caterpillar G3406-LS 32 HCR NGAS Manufacturer 2003 74-82-8 CH4 153 0.59 0.59 1 0035 RECIP Caterpillar G3406-LS 32 HCR NGAS Manufacturer 2003 CEL0002 NOx 2420 0.09 0.09 1

0035 RECIP Caterpillar G3406-LS 32 HCR NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

0035 RECIP Caterpillar G3406-LS 32 HCR NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

0035 RECIP Caterpillar G3406-LS 32 HCR NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

0035 RECIP Caterpillar G3406-LS 32 HCR NGAS Manufacturer 2003 CEL0006 VOC 24 0.27 0.27 1 0035 RECIP Caterpillar G3406-LS 32 HCR NGAS Manufacturer 2003 CEL0007 THC 177 0.51 0.51 1

0036 RECIP Caterpillar G3406-LS 32 LCR NGAS CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0036 RECIP Caterpillar G3406-LS 32 LCR NGAS Manufacturer 2003 630-08-0 CO 60 0.34 0.34 1 0036 RECIP Caterpillar G3406-LS 32 LCR NGAS Manufacturer 2003 74-82-8 CH4 155 0.59 0.59 1 0036 RECIP Caterpillar G3406-LS 32 LCR NGAS Manufacturer 2003 CEL0002 NOx 2348 0.09 0.09 1

0036 RECIP Caterpillar G3406-LS 32 LCR NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

0036 RECIP Caterpillar G3406-LS 32 LCR NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

0036 RECIP Caterpillar G3406-LS 32 LCR NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

0036 RECIP Caterpillar G3406-LS 32 LCR NGAS Manufacturer 2003 CEL0006 VOC 24 0.27 0.27 1 0036 RECIP Caterpillar G3406-LS 32 LCR NGAS Manufacturer 2003 CEL0007 THC 179 0.51 0.51 1

68

Table 3.3 Compilation of combustion emission factors for estimating GHG and CAC emissions.

Fact

or

Equ

ipm

ent

Typ

e

Identifier 1 Identifier 2 Identifier 3 Fuel Type

Factor Reference Y

ear CAS

Number Compound Emission

Factor (ng/J) L

ower

U

ncer

tain

ty

Upp

er

Unc

erta

inty

U

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Ref

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ce

0037 RECIP Caterpillar G3406-LS 54 HCR NGAS CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0037 RECIP Caterpillar G3406-LS 54 HCR NGAS Manufacturer 2003 630-08-0 CO 70 0.34 0.34 1 0037 RECIP Caterpillar G3406-LS 54 HCR NGAS Manufacturer 2003 74-82-8 CH4 163 0.59 0.59 1 0037 RECIP Caterpillar G3406-LS 54 HCR NGAS Manufacturer 2003 CEL0002 NOx 2293 0.09 0.09 1

0037 RECIP Caterpillar G3406-LS 54 HCR NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

0037 RECIP Caterpillar G3406-LS 54 HCR NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

0037 RECIP Caterpillar G3406-LS 54 HCR NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

0037 RECIP Caterpillar G3406-LS 54 HCR NGAS Manufacturer 2003 CEL0006 VOC 23 0.27 0.27 1 0037 RECIP Caterpillar G3406-LS 54 HCR NGAS Manufacturer 2003 CEL0007 THC 186 0.51 0.51 1

0038 RECIP Caterpillar G3406-LS 54 LCR NGAS CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0038 RECIP Caterpillar G3406-LS 54 LCR NGAS Manufacturer 2003 630-08-0 CO 58 0.34 0.34 1 0038 RECIP Caterpillar G3406-LS 54 LCR NGAS Manufacturer 2003 74-82-8 CH4 151 0.59 0.59 1 0038 RECIP Caterpillar G3406-LS 54 LCR NGAS Manufacturer 2003 CEL0002 NOx 2288 0.09 0.09 1

0038 RECIP Caterpillar G3406-LS 54 LCR NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

0038 RECIP Caterpillar G3406-LS 54 LCR NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

0038 RECIP Caterpillar G3406-LS 54 LCR NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

0038 RECIP Caterpillar G3406-LS 54 LCR NGAS Manufacturer 2003 CEL0006 VOC 23 0.27 0.27 1 0038 RECIP Caterpillar G3406-LS 54 LCR NGAS Manufacturer 2003 CEL0007 THC 174 0.51 0.51 1

0039 RECIP Caterpillar G3406-NA HCR NGAS CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0039 RECIP Caterpillar G3406-NA HCR NGAS Manufacturer 2003 630-08-0 CO 420 0.34 0.34 1 0039 RECIP Caterpillar G3406-NA HCR NGAS Manufacturer 2003 74-82-8 CH4 151 0.59 0.59 1 0039 RECIP Caterpillar G3406-NA HCR NGAS Manufacturer 2003 CEL0002 NOx 1325 0.09 0.09 1

0039 RECIP Caterpillar G3406-NA HCR NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

0039 RECIP Caterpillar G3406-NA HCR NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

0039 RECIP Caterpillar G3406-NA HCR NGAS U.S. EPA AP-42 - 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

69

Table 3.3 Compilation of combustion emission factors for estimating GHG and CAC emissions.

Fact

or

Equ

ipm

ent

Typ

e

Identifier 1 Identifier 2 Identifier 3 Fuel Type

Factor Reference Y

ear CAS

Number Compound Emission

Factor (ng/J) L

ower

U

ncer

tain

ty

Upp

er

Unc

erta

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U

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Ref

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ce

> Profile: 0016 0039 RECIP Caterpillar G3406-NA HCR NGAS Manufacturer 2003 CEL0006 VOC 32 0.27 0.27 1 0039 RECIP Caterpillar G3406-NA HCR NGAS Manufacturer 2003 CEL0007 THC 183 0.51 0.51 1

0040 RECIP Caterpillar G3406-NA LCR NGAS CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0040 RECIP Caterpillar G3406-NA LCR NGAS Manufacturer 2003 630-08-0 CO 420 0.34 0.34 1 0040 RECIP Caterpillar G3406-NA LCR NGAS Manufacturer 2003 74-82-8 CH4 151 0.59 0.59 1 0040 RECIP Caterpillar G3406-NA LCR NGAS Manufacturer 2003 CEL0002 NOx 1325 0.09 0.09 1

0040 RECIP Caterpillar G3406-NA LCR NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

0040 RECIP Caterpillar G3406-NA LCR NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

0040 RECIP Caterpillar G3406-NA LCR NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

0040 RECIP Caterpillar G3406-NA LCR NGAS Manufacturer 2003 CEL0006 VOC 32 0.27 0.27 1 0040 RECIP Caterpillar G3406-NA LCR NGAS Manufacturer 2003 CEL0007 THC 183 0.51 0.51 1

0041 RECIP Caterpillar G3408-HS 32 HCR - Catalyst NGAS

CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0041 RECIP Caterpillar G3408-HS 32 HCR - Catalyst NGAS Manufacturer 2003 630-08-0 CO 1169 0.34 0.34 1

0041 RECIP Caterpillar G3408-HS 32 HCR - Catalyst NGAS Manufacturer 2003 74-82-8 CH4 204 0.59 0.59 1

0041 RECIP Caterpillar G3408-HS 32 HCR - Catalyst NGAS Manufacturer 2003 CEL0002 NOx 1225 0.09 0.09 1

0041 RECIP Caterpillar G3408-HS 32 HCR - Catalyst NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

0041 RECIP Caterpillar G3408-HS 32 HCR - Catalyst NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

0041 RECIP Caterpillar G3408-HS 32 HCR - Catalyst NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

0041 RECIP Caterpillar G3408-HS 32 HCR - Catalyst NGAS Manufacturer 2003 CEL0006 VOC 34 0.27 0.27 1

0041 RECIP Caterpillar G3408-HS 32 HCR - Catalyst NGAS Manufacturer 2003 CEL0007 THC 238 0.51 0.51 1

0042 RECIP Caterpillar G3408-HS 32 HCR - Standard NGAS

CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

70

Table 3.3 Compilation of combustion emission factors for estimating GHG and CAC emissions.

Fact

or

Equ

ipm

ent

Typ

e

Identifier 1 Identifier 2 Identifier 3 Fuel Type

Factor Reference Y

ear CAS

Number Compound Emission

Factor (ng/J) L

ower

U

ncer

tain

ty

Upp

er

Unc

erta

inty

U

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Ref

eren

ce

0042 RECIP Caterpillar G3408-HS 32 HCR - Standard NGAS Manufacturer 2003 630-08-0 CO 92 0.34 0.34 1

0042 RECIP Caterpillar G3408-HS 32 HCR - Standard NGAS Manufacturer 2003 74-82-8 CH4 196 0.59 0.59 1

0042 RECIP Caterpillar G3408-HS 32 HCR - Standard NGAS Manufacturer 2003 CEL0002 NOx 2229 0.09 0.09 1

0042 RECIP Caterpillar G3408-HS 32 HCR - Standard NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

0042 RECIP Caterpillar G3408-HS 32 HCR - Standard NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

0042 RECIP Caterpillar G3408-HS 32 HCR - Standard NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

0042 RECIP Caterpillar G3408-HS 32 HCR - Standard NGAS Manufacturer 2003 CEL0006 VOC 35 0.27 0.27 1

0042 RECIP Caterpillar G3408-HS 32 HCR - Standard NGAS Manufacturer 2003 CEL0007 THC 231 0.51 0.51 1

0043 RECIP Caterpillar G3408-HS 32 LCR - Catalyst NGAS

CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0043 RECIP Caterpillar G3408-HS 32 LCR - Catalyst NGAS Manufacturer 2003 630-08-0 CO 1386 0.34 0.34 1

0043 RECIP Caterpillar G3408-HS 32 LCR - Catalyst NGAS Manufacturer 2003 74-82-8 CH4 216 0.59 0.59 1

0043 RECIP Caterpillar G3408-HS 32 LCR - Catalyst NGAS Manufacturer 2003 CEL0002 NOx 1261 0.09 0.09 1

0043 RECIP Caterpillar G3408-HS 32 LCR - Catalyst NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

0043 RECIP Caterpillar G3408-HS 32 LCR - Catalyst NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

0043 RECIP Caterpillar G3408-HS 32 LCR - Catalyst NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

0043 RECIP Caterpillar G3408-HS 32 LCR - Catalyst NGAS Manufacturer 2003 CEL0006 VOC 45 0.27 0.27 1

0043 RECIP Caterpillar G3408-HS 32 LCR - Catalyst NGAS Manufacturer 2003 CEL0007 THC 261 0.51 0.51 1

0044 RECIP Caterpillar G3408-HS 32 LCR - Standard NGAS

CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

71

Table 3.3 Compilation of combustion emission factors for estimating GHG and CAC emissions.

Fact

or

Equ

ipm

ent

Typ

e

Identifier 1 Identifier 2 Identifier 3 Fuel Type

Factor Reference Y

ear CAS

Number Compound Emission

Factor (ng/J) L

ower

U

ncer

tain

ty

Upp

er

Unc

erta

inty

U

ncer

tain

ty

Ref

eren

ce

0044 RECIP Caterpillar G3408-HS 32 LCR - Standard NGAS Manufacturer 2003 630-08-0 CO 96 0.34 0.34 1

0044 RECIP Caterpillar G3408-HS 32 LCR - Standard NGAS Manufacturer 2003 74-82-8 CH4 167 0.59 0.59 1

0044 RECIP Caterpillar G3408-HS 32 LCR - Standard NGAS Manufacturer 2003 CEL0002 NOx 2676 0.09 0.09 1

0044 RECIP Caterpillar G3408-HS 32 LCR - Standard NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

0044 RECIP Caterpillar G3408-HS 32 LCR - Standard NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

0044 RECIP Caterpillar G3408-HS 32 LCR - Standard NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

0044 RECIP Caterpillar G3408-HS 32 LCR - Standard NGAS Manufacturer 2003 CEL0006 VOC 36 0.27 0.27 1

0044 RECIP Caterpillar G3408-HS 32 LCR - Standard NGAS Manufacturer 2003 CEL0007 THC 203 0.51 0.51 1

0045 RECIP Caterpillar G3408-HS 54 HCR NGAS CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0045 RECIP Caterpillar G3408-HS 54 HCR NGAS Manufacturer 2003 630-08-0 CO 102 0.34 0.34 1 0045 RECIP Caterpillar G3408-HS 54 HCR NGAS Manufacturer 2003 74-82-8 CH4 182 0.59 0.59 1 0045 RECIP Caterpillar G3408-HS 54 HCR NGAS Manufacturer 2003 CEL0002 NOx 2215 0.09 0.09 1

0045 RECIP Caterpillar G3408-HS 54 HCR NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

0045 RECIP Caterpillar G3408-HS 54 HCR NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

0045 RECIP Caterpillar G3408-HS 54 HCR NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

0045 RECIP Caterpillar G3408-HS 54 HCR NGAS Manufacturer 2003 CEL0006 VOC 34 0.27 0.27 1 0045 RECIP Caterpillar G3408-HS 54 HCR NGAS Manufacturer 2003 CEL0007 THC 216 0.51 0.51 1

0046 RECIP Caterpillar G3408-HS 54 LCR - Catalyst NGAS

CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0046 RECIP Caterpillar G3408-HS 54 LCR - Catalyst NGAS Manufacturer 2003 630-08-0 CO 1342 0.34 0.34 1

0046 RECIP Caterpillar G3408-HS 54 LCR - Catalyst NGAS Manufacturer 2003 74-82-8 CH4 220 0.59 0.59 1

0046 RECIP Caterpillar G3408-HS 54 LCR NGAS Manufacturer 2003 CEL0002 NOx 1309 0.09 0.09 1

72

Table 3.3 Compilation of combustion emission factors for estimating GHG and CAC emissions.

Fact

or

Equ

ipm

ent

Typ

e

Identifier 1 Identifier 2 Identifier 3 Fuel Type

Factor Reference Y

ear CAS

Number Compound Emission

Factor (ng/J) L

ower

U

ncer

tain

ty

Upp

er

Unc

erta

inty

U

ncer

tain

ty

Ref

eren

ce

- Catalyst

0046 RECIP Caterpillar G3408-HS 54 LCR - Catalyst NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

0046 RECIP Caterpillar G3408-HS 54 LCR - Catalyst NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

0046 RECIP Caterpillar G3408-HS 54 LCR - Catalyst NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

0046 RECIP Caterpillar G3408-HS 54 LCR - Catalyst NGAS Manufacturer 2003 CEL0006 VOC 44 0.27 0.27 1

0046 RECIP Caterpillar G3408-HS 54 LCR - Catalyst NGAS Manufacturer 2003 CEL0007 THC 264 0.51 0.51 1

0047 RECIP Caterpillar G3408-HS 54 LCR - Standard NGAS

CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0047 RECIP Caterpillar G3408-HS 54 LCR - Standard NGAS Manufacturer 2003 630-08-0 CO 94 0.34 0.34 1

0047 RECIP Caterpillar G3408-HS 54 LCR - Standard NGAS Manufacturer 2003 74-82-8 CH4 176 0.59 0.59 1

0047 RECIP Caterpillar G3408-HS 54 LCR - Standard NGAS Manufacturer 2003 CEL0002 NOx 2579 0.09 0.09 1

0047 RECIP Caterpillar G3408-HS 54 LCR - Standard NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

0047 RECIP Caterpillar G3408-HS 54 LCR - Standard NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

0047 RECIP Caterpillar G3408-HS 54 LCR - Standard NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

0047 RECIP Caterpillar G3408-HS 54 LCR - Standard NGAS Manufacturer 2003 CEL0006 VOC 35 0.27 0.27 1

0047 RECIP Caterpillar G3408-HS 54 LCR - Standard NGAS Manufacturer 2003 CEL0007 THC 211 0.51 0.51 1

0048 RECIP Caterpillar G3408-LS 32 HCR NGAS CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0048 RECIP Caterpillar G3408-LS 32 HCR NGAS Manufacturer 2003 630-08-0 CO 94 0.34 0.34 1 0048 RECIP Caterpillar G3408-LS 32 HCR NGAS Manufacturer 2003 74-82-8 CH4 175 0.59 0.59 1 0048 RECIP Caterpillar G3408-LS 32 HCR NGAS Manufacturer 2003 CEL0002 NOx 2234 0.09 0.09 1

0048 RECIP Caterpillar G3408-LS 32 HCR NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

73

Table 3.3 Compilation of combustion emission factors for estimating GHG and CAC emissions.

Fact

or

Equ

ipm

ent

Typ

e

Identifier 1 Identifier 2 Identifier 3 Fuel Type

Factor Reference Y

ear CAS

Number Compound Emission

Factor (ng/J) L

ower

U

ncer

tain

ty

Upp

er

Unc

erta

inty

U

ncer

tain

ty

Ref

eren

ce

0048 RECIP Caterpillar G3408-LS 32 HCR NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

0048 RECIP Caterpillar G3408-LS 32 HCR NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

0048 RECIP Caterpillar G3408-LS 32 HCR NGAS Manufacturer 2003 CEL0006 VOC 35 0.27 0.27 1 0048 RECIP Caterpillar G3408-LS 32 HCR NGAS Manufacturer 2003 CEL0007 THC 211 0.51 0.51 1

0049 RECIP Caterpillar G3408-LS 32 LCR NGAS CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0049 RECIP Caterpillar G3408-LS 32 LCR NGAS Manufacturer 2003 630-08-0 CO 69 0.34 0.34 1 0049 RECIP Caterpillar G3408-LS 32 LCR NGAS Manufacturer 2003 74-82-8 CH4 126 0.59 0.59 1 0049 RECIP Caterpillar G3408-LS 32 LCR NGAS Manufacturer 2003 CEL0002 NOx 2412 0.09 0.09 1

0049 RECIP Caterpillar G3408-LS 32 LCR NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

0049 RECIP Caterpillar G3408-LS 32 LCR NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

0049 RECIP Caterpillar G3408-LS 32 LCR NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

0049 RECIP Caterpillar G3408-LS 32 LCR NGAS Manufacturer 2003 CEL0006 VOC 23 0.27 0.27 1 0049 RECIP Caterpillar G3408-LS 32 LCR NGAS Manufacturer 2003 CEL0007 THC 149 0.51 0.51 1

0050 RECIP Caterpillar G3408-LS 54 HCR NGAS CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0050 RECIP Caterpillar G3408-LS 54 HCR NGAS Manufacturer 2003 630-08-0 CO 91 0.34 0.34 1 0050 RECIP Caterpillar G3408-LS 54 HCR NGAS Manufacturer 2003 74-82-8 CH4 182 0.59 0.59 1 0050 RECIP Caterpillar G3408-LS 54 HCR NGAS Manufacturer 2003 CEL0002 NOx 2071 0.09 0.09 1

0050 RECIP Caterpillar G3408-LS 54 HCR NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

0050 RECIP Caterpillar G3408-LS 54 HCR NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

0050 RECIP Caterpillar G3408-LS 54 HCR NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

0050 RECIP Caterpillar G3408-LS 54 HCR NGAS Manufacturer 2003 CEL0006 VOC 34 0.27 0.27 1 0050 RECIP Caterpillar G3408-LS 54 HCR NGAS Manufacturer 2003 CEL0007 THC 216 0.51 0.51 1

0051 RECIP Caterpillar G3408-LS 54 LCR NGAS CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0051 RECIP Caterpillar G3408-LS 54 LCR NGAS Manufacturer 2003 630-08-0 CO 78 0.34 0.34 1 0051 RECIP Caterpillar G3408-LS 54 LCR NGAS Manufacturer 2003 74-82-8 CH4 134 0.59 0.59 1

74

Table 3.3 Compilation of combustion emission factors for estimating GHG and CAC emissions.

Fact

or

Equ

ipm

ent

Typ

e

Identifier 1 Identifier 2 Identifier 3 Fuel Type

Factor Reference Y

ear CAS

Number Compound Emission

Factor (ng/J) L

ower

U

ncer

tain

ty

Upp

er

Unc

erta

inty

U

ncer

tain

ty

Ref

eren

ce

0051 RECIP Caterpillar G3408-LS 54 LCR NGAS Manufacturer 2003 CEL0002 NOx 2360 0.09 0.09 1

0051 RECIP Caterpillar G3408-LS 54 LCR NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

0051 RECIP Caterpillar G3408-LS 54 LCR NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

0051 RECIP Caterpillar G3408-LS 54 LCR NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

0051 RECIP Caterpillar G3408-LS 54 LCR NGAS Manufacturer 2003 CEL0006 VOC 22 0.27 0.27 1 0051 RECIP Caterpillar G3408-LS 54 LCR NGAS Manufacturer 2003 CEL0007 THC 157 0.51 0.51 1

0052 RECIP Caterpillar G3408-NA HCR NGAS CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0052 RECIP Caterpillar G3408-NA HCR NGAS Manufacturer 2003 630-08-0 CO 45 0.34 0.34 1 0052 RECIP Caterpillar G3408-NA HCR NGAS Manufacturer 2003 74-82-8 CH4 146 0.59 0.59 1 0052 RECIP Caterpillar G3408-NA HCR NGAS Manufacturer 2003 CEL0002 NOx 2201 0.09 0.09 1

0052 RECIP Caterpillar G3408-NA HCR NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

0052 RECIP Caterpillar G3408-NA HCR NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

0052 RECIP Caterpillar G3408-NA HCR NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

0052 RECIP Caterpillar G3408-NA HCR NGAS Manufacturer 2003 CEL0006 VOC 22 0.27 0.27 1 0052 RECIP Caterpillar G3408-NA HCR NGAS Manufacturer 2003 CEL0007 THC 168 0.51 0.51 1

0053 RECIP Caterpillar G3412-HS 32 HCR - Catalyst NGAS

CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0053 RECIP Caterpillar G3412-HS 32 HCR - Catalyst NGAS Manufacturer 2003 630-08-0 CO 2471 0.34 0.34 1

0053 RECIP Caterpillar G3412-HS 32 HCR - Catalyst NGAS Manufacturer 2003 74-82-8 CH4 150 0.59 0.59 1

0053 RECIP Caterpillar G3412-HS 32 HCR - Catalyst NGAS Manufacturer 2003 CEL0002 NOx 1091 0.09 0.09 1

0053 RECIP Caterpillar G3412-HS 32 HCR - Catalyst NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

0053 RECIP Caterpillar G3412-HS 32 HCR - Catalyst NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

0053 RECIP Caterpillar G3412-HS 32 HCR - Catalyst NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

75

Table 3.3 Compilation of combustion emission factors for estimating GHG and CAC emissions.

Fact

or

Equ

ipm

ent

Typ

e

Identifier 1 Identifier 2 Identifier 3 Fuel Type

Factor Reference Y

ear CAS

Number Compound Emission

Factor (ng/J) L

ower

U

ncer

tain

ty

Upp

er

Unc

erta

inty

U

ncer

tain

ty

Ref

eren

ce

0053 RECIP Caterpillar G3412-HS 32 HCR - Catalyst NGAS Manufacturer 2003 CEL0006 VOC 32 0.27 0.27 1

0053 RECIP Caterpillar G3412-HS 32 HCR - Catalyst NGAS Manufacturer 2003 CEL0007 THC 182 0.51 0.51 1

0054 RECIP Caterpillar G3412-HS 32 HCR - Standard NGAS

CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0054 RECIP Caterpillar G3412-HS 32 HCR - Standard NGAS Manufacturer 2003 630-08-0 CO 157 0.34 0.34 1

0054 RECIP Caterpillar G3412-HS 32 HCR - Standard NGAS Manufacturer 2003 74-82-8 CH4 123 0.59 0.59 1

0054 RECIP Caterpillar G3412-HS 32 HCR - Standard NGAS Manufacturer 2003 CEL0002 NOx 1836 0.09 0.09 1

0054 RECIP Caterpillar G3412-HS 32 HCR - Standard NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

0054 RECIP Caterpillar G3412-HS 32 HCR - Standard NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

0054 RECIP Caterpillar G3412-HS 32 HCR - Standard NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

0054 RECIP Caterpillar G3412-HS 32 HCR - Standard NGAS Manufacturer 2003 CEL0006 VOC 22 0.27 0.27 1

0054 RECIP Caterpillar G3412-HS 32 HCR - Standard NGAS Manufacturer 2003 CEL0007 THC 146 0.51 0.51 1

0055 RECIP Caterpillar G3412-HS 32 LCR NGAS CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0055 RECIP Caterpillar G3412-HS 32 LCR NGAS Manufacturer 2003 630-08-0 CO 203 0.34 0.34 1 0055 RECIP Caterpillar G3412-HS 32 LCR NGAS Manufacturer 2003 74-82-8 CH4 144 0.59 0.59 1 0055 RECIP Caterpillar G3412-HS 32 LCR NGAS Manufacturer 2003 CEL0002 NOx 2131 0.09 0.09 1

0055 RECIP Caterpillar G3412-HS 32 LCR NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

0055 RECIP Caterpillar G3412-HS 32 LCR NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

0055 RECIP Caterpillar G3412-HS 32 LCR NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

0055 RECIP Caterpillar G3412-HS 32 LCR NGAS Manufacturer 2003 CEL0006 VOC 24 0.27 0.27 1 0055 RECIP Caterpillar G3412-HS 32 LCR NGAS Manufacturer 2003 CEL0007 THC 168 0.51 0.51 1 0056 RECIP Caterpillar G3412-HS 54 HCR NGAS CHEMEX Labs -> 1996 10024-97-2 N2O 5.72 0.18 5.45 3

76

Table 3.3 Compilation of combustion emission factors for estimating GHG and CAC emissions.

Fact

or

Equ

ipm

ent

Typ

e

Identifier 1 Identifier 2 Identifier 3 Fuel Type

Factor Reference Y

ear CAS

Number Compound Emission

Factor (ng/J) L

ower

U

ncer

tain

ty

Upp

er

Unc

erta

inty

U

ncer

tain

ty

Ref

eren

ce

- Catalyst Profile: 0016

0056 RECIP Caterpillar G3412-HS 54 HCR - Catalyst NGAS Manufacturer 2003 630-08-0 CO 2084 0.34 0.34 1

0056 RECIP Caterpillar G3412-HS 54 HCR - Catalyst NGAS Manufacturer 2003 74-82-8 CH4 167 0.59 0.59 1

0056 RECIP Caterpillar G3412-HS 54 HCR - Catalyst NGAS Manufacturer 2003 CEL0002 NOx 886 0.09 0.09 1

0056 RECIP Caterpillar G3412-HS 54 HCR - Catalyst NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

0056 RECIP Caterpillar G3412-HS 54 HCR - Catalyst NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

0056 RECIP Caterpillar G3412-HS 54 HCR - Catalyst NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

0056 RECIP Caterpillar G3412-HS 54 HCR - Catalyst NGAS Manufacturer 2003 CEL0006 VOC 31 0.27 0.27 1

0056 RECIP Caterpillar G3412-HS 54 HCR - Catalyst NGAS Manufacturer 2003 CEL0007 THC 198 0.51 0.51 1

0057 RECIP Caterpillar G3412-HS 54 HCR - Standard NGAS

CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0057 RECIP Caterpillar G3412-HS 54 HCR - Standard NGAS Manufacturer 2003 630-08-0 CO 121 0.34 0.34 1

0057 RECIP Caterpillar G3412-HS 54 HCR - Standard NGAS Manufacturer 2003 74-82-8 CH4 132 0.59 0.59 1

0057 RECIP Caterpillar G3412-HS 54 HCR - Standard NGAS Manufacturer 2003 CEL0002 NOx 1840 0.09 0.09 1

0057 RECIP Caterpillar G3412-HS 54 HCR - Standard NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

0057 RECIP Caterpillar G3412-HS 54 HCR - Standard NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

0057 RECIP Caterpillar G3412-HS 54 HCR - Standard NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

0057 RECIP Caterpillar G3412-HS 54 HCR - Standard NGAS Manufacturer 2003 CEL0006 VOC 22 0.27 0.27 1

0057 RECIP Caterpillar G3412-HS 54 HCR - Standard NGAS Manufacturer 2003 CEL0007 THC 154 0.51 0.51 1

0058 RECIP Caterpillar G3412-HS 54 LCR NGAS CHEMEX Labs -> 1996 10024-97-2 N2O 5.72 0.18 5.45 3

77

Table 3.3 Compilation of combustion emission factors for estimating GHG and CAC emissions.

Fact

or

Equ

ipm

ent

Typ

e

Identifier 1 Identifier 2 Identifier 3 Fuel Type

Factor Reference Y

ear CAS

Number Compound Emission

Factor (ng/J) L

ower

U

ncer

tain

ty

Upp

er

Unc

erta

inty

U

ncer

tain

ty

Ref

eren

ce

Profile: 0016 0058 RECIP Caterpillar G3412-HS 54 LCR NGAS Manufacturer 2003 630-08-0 CO 128 0.34 0.34 1 0058 RECIP Caterpillar G3412-HS 54 LCR NGAS Manufacturer 2003 74-82-8 CH4 58 0.59 0.59 1 0058 RECIP Caterpillar G3412-HS 54 LCR NGAS Manufacturer 2003 CEL0002 NOx 2159 0.09 0.09 1

0058 RECIP Caterpillar G3412-HS 54 LCR NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

0058 RECIP Caterpillar G3412-HS 54 LCR NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

0058 RECIP Caterpillar G3412-HS 54 LCR NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

0058 RECIP Caterpillar G3412-HS 54 LCR NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0006 VOC 12.7 0.27 0.27 1

0058 RECIP Caterpillar G3412-HS 54 LCR NGAS Manufacturer 2003 CEL0007 THC 58 0.51 0.51 1

0059 RECIP Caterpillar G3412-LS 32 HCR - Catalyst NGAS

CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0059 RECIP Caterpillar G3412-LS 32 HCR - Catalyst NGAS Manufacturer 2003 630-08-0 CO 3082 0.34 0.34 1

0059 RECIP Caterpillar G3412-LS 32 HCR - Catalyst NGAS Manufacturer 2003 74-82-8 CH4 166 0.59 0.59 1

0059 RECIP Caterpillar G3412-LS 32 HCR - Catalyst NGAS Manufacturer 2003 CEL0002 NOx 1359 0.09 0.09 1

0059 RECIP Caterpillar G3412-LS 32 HCR - Catalyst NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

0059 RECIP Caterpillar G3412-LS 32 HCR - Catalyst NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

0059 RECIP Caterpillar G3412-LS 32 HCR - Catalyst NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

0059 RECIP Caterpillar G3412-LS 32 HCR - Catalyst NGAS Manufacturer 2003 CEL0006 VOC 33 0.27 0.27 1

0059 RECIP Caterpillar G3412-LS 32 HCR - Catalyst NGAS Manufacturer 2003 CEL0007 THC 199 0.51 0.51 1

0060 RECIP Caterpillar G3412-LS 32 HCR - Standard NGAS

CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0060 RECIP Caterpillar G3412-LS 32 HCR - Standard NGAS Manufacturer 2003 630-08-0 CO 1074 0.34 0.34 1

0060 RECIP Caterpillar G3412-LS 32 HCR NGAS Manufacturer 2003 74-82-8 CH4 149 0.59 0.59 1

78

Table 3.3 Compilation of combustion emission factors for estimating GHG and CAC emissions.

Fact

or

Equ

ipm

ent

Typ

e

Identifier 1 Identifier 2 Identifier 3 Fuel Type

Factor Reference Y

ear CAS

Number Compound Emission

Factor (ng/J) L

ower

U

ncer

tain

ty

Upp

er

Unc

erta

inty

U

ncer

tain

ty

Ref

eren

ce

- Standard

0060 RECIP Caterpillar G3412-LS 32 HCR - Standard NGAS Manufacturer 2003 CEL0002 NOx 1932 0.09 0.09 1

0060 RECIP Caterpillar G3412-LS 32 HCR - Standard NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

0060 RECIP Caterpillar G3412-LS 32 HCR - Standard NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

0060 RECIP Caterpillar G3412-LS 32 HCR - Standard NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

0060 RECIP Caterpillar G3412-LS 32 HCR - Standard NGAS Manufacturer 2003 CEL0006 VOC 23 0.27 0.27 1

0060 RECIP Caterpillar G3412-LS 32 HCR - Standard NGAS Manufacturer 2003 CEL0007 THC 171 0.51 0.51 1

0061 RECIP Caterpillar G3412-LS 32 LCR - Catalyst NGAS

CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0061 RECIP Caterpillar G3412-LS 32 LCR - Catalyst NGAS Manufacturer 2003 630-08-0 CO 1571 0.34 0.34 1

0061 RECIP Caterpillar G3412-LS 32 LCR - Catalyst NGAS Manufacturer 2003 74-82-8 CH4 152 0.59 0.59 1

0061 RECIP Caterpillar G3412-LS 32 LCR - Catalyst NGAS Manufacturer 2003 CEL0002 NOx 1246 0.09 0.09 1

0061 RECIP Caterpillar G3412-LS 32 LCR - Catalyst NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

0061 RECIP Caterpillar G3412-LS 32 LCR - Catalyst NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

0061 RECIP Caterpillar G3412-LS 32 LCR - Catalyst NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

0061 RECIP Caterpillar G3412-LS 32 LCR - Catalyst NGAS Manufacturer 2003 CEL0006 VOC 22 0.27 0.27 1

0061 RECIP Caterpillar G3412-LS 32 LCR - Catalyst NGAS Manufacturer 2003 CEL0007 THC 173 0.51 0.51 1

0062 RECIP Caterpillar G3412-LS 32 LCR - Standard NGAS

CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0062 RECIP Caterpillar G3412-LS 32 LCR - Standard NGAS Manufacturer 2003 630-08-0 CO 715 0.34 0.34 1

0062 RECIP Caterpillar G3412-LS 32 LCR NGAS Manufacturer 2003 74-82-8 CH4 145 0.59 0.59 1

79

Table 3.3 Compilation of combustion emission factors for estimating GHG and CAC emissions.

Fact

or

Equ

ipm

ent

Typ

e

Identifier 1 Identifier 2 Identifier 3 Fuel Type

Factor Reference Y

ear CAS

Number Compound Emission

Factor (ng/J) L

ower

U

ncer

tain

ty

Upp

er

Unc

erta

inty

U

ncer

tain

ty

Ref

eren

ce

- Standard

0062 RECIP Caterpillar G3412-LS 32 LCR - Standard NGAS Manufacturer 2003 CEL0002 NOx 2111 0.09 0.09 1

0062 RECIP Caterpillar G3412-LS 32 LCR - Standard NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

0062 RECIP Caterpillar G3412-LS 32 LCR - Standard NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

0062 RECIP Caterpillar G3412-LS 32 LCR - Standard NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

0062 RECIP Caterpillar G3412-LS 32 LCR - Standard NGAS Manufacturer 2003 CEL0006 VOC 22 0.27 0.27 1

0062 RECIP Caterpillar G3412-LS 32 LCR - Standard NGAS Manufacturer 2003 CEL0007 THC 168 0.51 0.51 1

0063 RECIP Caterpillar G3412-LS 54 HCR - Catalyst NGAS

CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0063 RECIP Caterpillar G3412-LS 54 HCR - Catalyst NGAS Manufacturer 2003 630-08-0 CO 4071 0.34 0.34 1

0063 RECIP Caterpillar G3412-LS 54 HCR - Catalyst NGAS Manufacturer 2003 74-82-8 CH4 209 0.59 0.59 1

0063 RECIP Caterpillar G3412-LS 54 HCR - Catalyst NGAS Manufacturer 2003 CEL0002 NOx 1242 0.09 0.09 1

0063 RECIP Caterpillar G3412-LS 54 HCR - Catalyst NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

0063 RECIP Caterpillar G3412-LS 54 HCR - Catalyst NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

0063 RECIP Caterpillar G3412-LS 54 HCR - Catalyst NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

0063 RECIP Caterpillar G3412-LS 54 HCR - Catalyst NGAS Manufacturer 2003 CEL0006 VOC 31 0.27 0.27 1

0063 RECIP Caterpillar G3412-LS 54 HCR - Catalyst NGAS Manufacturer 2003 CEL0007 THC 240 0.51 0.51 1

0064 RECIP Caterpillar G3412-LS 54 HCR - Standard NGAS

CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0064 RECIP Caterpillar G3412-LS 54 HCR - Standard NGAS Manufacturer 2003 630-08-0 CO 829 0.34 0.34 1

0064 RECIP Caterpillar G3412-LS 54 HCR NGAS Manufacturer 2003 74-82-8 CH4 155 0.59 0.59 1

80

Table 3.3 Compilation of combustion emission factors for estimating GHG and CAC emissions.

Fact

or

Equ

ipm

ent

Typ

e

Identifier 1 Identifier 2 Identifier 3 Fuel Type

Factor Reference Y

ear CAS

Number Compound Emission

Factor (ng/J) L

ower

U

ncer

tain

ty

Upp

er

Unc

erta

inty

U

ncer

tain

ty

Ref

eren

ce

- Standard

0064 RECIP Caterpillar G3412-LS 54 HCR - Standard NGAS Manufacturer 2003 CEL0002 NOx 1978 0.09 0.09 1

0064 RECIP Caterpillar G3412-LS 54 HCR - Standard NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

0064 RECIP Caterpillar G3412-LS 54 HCR - Standard NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

0064 RECIP Caterpillar G3412-LS 54 HCR - Standard NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

0064 RECIP Caterpillar G3412-LS 54 HCR - Standard NGAS Manufacturer 2003 CEL0006 VOC 33 0.27 0.27 1

0064 RECIP Caterpillar G3412-LS 54 HCR - Standard NGAS Manufacturer 2003 CEL0007 THC 188 0.51 0.51 1

0065 RECIP Caterpillar G3412-LS 54 LCR - Catalyst NGAS

CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0065 RECIP Caterpillar G3412-LS 54 LCR - Catalyst NGAS Manufacturer 2003 630-08-0 CO 2224 0.34 0.34 1

0065 RECIP Caterpillar G3412-LS 54 LCR - Catalyst NGAS Manufacturer 2003 74-82-8 CH4 152 0.59 0.59 1

0065 RECIP Caterpillar G3412-LS 54 LCR - Catalyst NGAS Manufacturer 2003 CEL0002 NOx 1497 0.09 0.09 1

0065 RECIP Caterpillar G3412-LS 54 LCR - Catalyst NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

0065 RECIP Caterpillar G3412-LS 54 LCR - Catalyst NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

0065 RECIP Caterpillar G3412-LS 54 LCR - Catalyst NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

0065 RECIP Caterpillar G3412-LS 54 LCR - Catalyst NGAS Manufacturer 2003 CEL0006 VOC 33 0.27 0.27 1

0065 RECIP Caterpillar G3412-LS 54 LCR - Catalyst NGAS Manufacturer 2003 CEL0007 THC 184 0.51 0.51 1

0066 RECIP Caterpillar G3412-LS 54 LCR - Standard NGAS

CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0066 RECIP Caterpillar G3412-LS 54 LCR - Standard NGAS Manufacturer 2003 630-08-0 CO 842 0.34 0.34 1

0066 RECIP Caterpillar G3412-LS 54 LCR NGAS Manufacturer 2003 74-82-8 CH4 146 0.59 0.59 1

81

Table 3.3 Compilation of combustion emission factors for estimating GHG and CAC emissions.

Fact

or

Equ

ipm

ent

Typ

e

Identifier 1 Identifier 2 Identifier 3 Fuel Type

Factor Reference Y

ear CAS

Number Compound Emission

Factor (ng/J) L

ower

U

ncer

tain

ty

Upp

er

Unc

erta

inty

U

ncer

tain

ty

Ref

eren

ce

- Standard

0066 RECIP Caterpillar G3412-LS 54 LCR - Standard NGAS Manufacturer 2003 CEL0002 NOx 2122 0.09 0.09 1

0066 RECIP Caterpillar G3412-LS 54 LCR - Standard NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

0066 RECIP Caterpillar G3412-LS 54 LCR - Standard NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

0066 RECIP Caterpillar G3412-LS 54 LCR - Standard NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

0066 RECIP Caterpillar G3412-LS 54 LCR - Standard NGAS Manufacturer 2003 CEL0006 VOC 22 0.27 0.27 1

0066 RECIP Caterpillar G3412-LS 54 LCR - Standard NGAS Manufacturer 2003 CEL0007 THC 168 0.51 0.51 1

0067 RECIP Caterpillar G3412-NA HCR NGAS CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0067 RECIP Caterpillar G3412-NA HCR NGAS Manufacturer 2003 630-08-0 CO 1681 0.34 0.34 1 0067 RECIP Caterpillar G3412-NA HCR NGAS Manufacturer 2003 74-82-8 CH4 269 0.59 0.59 1 0067 RECIP Caterpillar G3412-NA HCR NGAS Manufacturer 2003 CEL0002 NOx 980 0.09 0.09 1

0067 RECIP Caterpillar G3412-NA HCR NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

0067 RECIP Caterpillar G3412-NA HCR NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

0067 RECIP Caterpillar G3412-NA HCR NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

0067 RECIP Caterpillar G3412-NA HCR NGAS Manufacturer 2003 CEL0006 VOC 43 0.27 0.27 1 0067 RECIP Caterpillar G3412-NA HCR NGAS Manufacturer 2003 CEL0007 THC 312 0.51 0.51 1

0068 RECIP Caterpillar G342 SI-NA - HCR NGAS

CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0068 RECIP Caterpillar G342 SI-NA - HCR NGAS Manufacturer 2003 630-08-0 CO 1595 0.34 0.34 1

0068 RECIP Caterpillar G342 SI-NA - HCR NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 74-82-8 CH4 99 0.59 0.59 1

0068 RECIP Caterpillar G342 SI-NA - HCR NGAS Manufacturer 2003 CEL0002 NOx 1502 0.09 0.09 1

0068 RECIP Caterpillar G342 SI-NA - HCR NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

82

Table 3.3 Compilation of combustion emission factors for estimating GHG and CAC emissions.

Fact

or

Equ

ipm

ent

Typ

e

Identifier 1 Identifier 2 Identifier 3 Fuel Type

Factor Reference Y

ear CAS

Number Compound Emission

Factor (ng/J) L

ower

U

ncer

tain

ty

Upp

er

Unc

erta

inty

U

ncer

tain

ty

Ref

eren

ce

0068 RECIP Caterpillar G342 SI-NA - HCR NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

0068 RECIP Caterpillar G342 SI-NA - HCR NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

0068 RECIP Caterpillar G342 SI-NA - HCR NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0006 VOC 12.7 0.27 0.27 1

0068 RECIP Caterpillar G342 SI-NA - HCR NGAS Manufacturer 2003 CEL0007 THC 210 0.51 0.51 1

0069 RECIP Caterpillar G342 SI-NA - LCR NGAS CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0069 RECIP Caterpillar G342 SI-NA - LCR NGAS Manufacturer 2003 630-08-0 CO 83 0.34 0.34 1

0069 RECIP Caterpillar G342 SI-NA - LCR NGAS U.S. EPA AP-42 -> Profile: 0016 2000 74-82-8 CH4 99 0.59 0.59 1

0069 RECIP Caterpillar G342 SI-NA - LCR NGAS Manufacturer 2003 CEL0002 NOx 2124 0.09 0.09 1

0069 RECIP Caterpillar G342 SI-NA - LCR NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

0069 RECIP Caterpillar G342 SI-NA - LCR NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

0069 RECIP Caterpillar G342 SI-NA - LCR NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

0069 RECIP Caterpillar G342 SI-NA - LCR NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0006 VOC 12.7 0.27 0.27 1

0069 RECIP Caterpillar G342 SI-NA - LCR NGAS Manufacturer 2003 CEL0007 THC 83 0.51 0.51 1

0070 RECIP Caterpillar G342 SI-TA-SC - HCR 32 - Catalyst NGAS

CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0070 RECIP Caterpillar G342 SI-TA-SC - HCR 32 - Catalyst NGAS Manufacturer 2003 630-08-0 CO 1089 0.34 0.34 1

0070 RECIP Caterpillar G342 SI-TA-SC - HCR 32 - Catalyst NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 74-82-8 CH4 99 0.59 0.59 1

0070 RECIP Caterpillar G342 SI-TA-SC - HCR 32 - Catalyst NGAS Manufacturer 2003 CEL0002 NOx 1034 0.09 0.09 1

0070 RECIP Caterpillar G342 SI-TA-SC - HCR 32 - Catalyst NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

0070 RECIP Caterpillar G342 SI-TA-SC - HCR 32 - Catalyst NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

0070 RECIP Caterpillar G342 SI-TA-SC - NGAS U.S. EPA AP-42 - 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

83

Table 3.3 Compilation of combustion emission factors for estimating GHG and CAC emissions.

Fact

or

Equ

ipm

ent

Typ

e

Identifier 1 Identifier 2 Identifier 3 Fuel Type

Factor Reference Y

ear CAS

Number Compound Emission

Factor (ng/J) L

ower

U

ncer

tain

ty

Upp

er

Unc

erta

inty

U

ncer

tain

ty

Ref

eren

ce

HCR 32 - Catalyst > Profile: 0016

0070 RECIP Caterpillar G342 SI-TA-SC - HCR 32 - Catalyst NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0006 VOC 12.7 0.27 0.27 1

0070 RECIP Caterpillar G342 SI-TA-SC - HCR 32 - Catalyst NGAS Manufacturer 2003 CEL0007 THC 176 0.51 0.51 1

0071 RECIP Caterpillar G342 SI-TA-SC - HCR 32 - Standard NGAS

CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0071 RECIP Caterpillar G342 SI-TA-SC - HCR 32 - Standard NGAS Manufacturer 2003 630-08-0 CO 125 0.34 0.34 1

0071 RECIP Caterpillar G342 SI-TA-SC - HCR 32 - Standard NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 74-82-8 CH4 99 0.59 0.59 1

0071 RECIP Caterpillar G342 SI-TA-SC - HCR 32 - Standard NGAS Manufacturer 2003 CEL0002 NOx 1756 0.09 0.09 1

0071 RECIP Caterpillar G342 SI-TA-SC - HCR 32 - Standard NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

0071 RECIP Caterpillar G342 SI-TA-SC - HCR 32 - Standard NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

0071 RECIP Caterpillar G342 SI-TA-SC - HCR 32 - Standard NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

0071 RECIP Caterpillar G342 SI-TA-SC - HCR 32 - Standard NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0006 VOC 12.7 0.27 0.27 1

0071 RECIP Caterpillar G342 SI-TA-SC - HCR 32 - Standard NGAS Manufacturer 2003 CEL0007 THC 91 0.51 0.51 1

0072 RECIP Caterpillar G342 SI-TA-SC - LCR 32 NGAS

CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0072 RECIP Caterpillar G342 SI-TA-SC - LCR 32 NGAS Manufacturer 2003 630-08-0 CO 84 0.34 0.34 1

0072 RECIP Caterpillar G342 SI-TA-SC - LCR 32 NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 74-82-8 CH4 99 0.59 0.59 1

0072 RECIP Caterpillar G342 SI-TA-SC - LCR 32 NGAS Manufacturer 2003 CEL0002 NOx 1926 0.09 0.09 1

0072 RECIP Caterpillar G342 SI-TA-SC - LCR 32 NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

0072 RECIP Caterpillar G342 SI-TA-SC - LCR 32 NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

0072 RECIP Caterpillar G342 SI-TA-SC - NGAS U.S. EPA AP-42 - 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

84

Table 3.3 Compilation of combustion emission factors for estimating GHG and CAC emissions.

Fact

or

Equ

ipm

ent

Typ

e

Identifier 1 Identifier 2 Identifier 3 Fuel Type

Factor Reference Y

ear CAS

Number Compound Emission

Factor (ng/J) L

ower

U

ncer

tain

ty

Upp

er

Unc

erta

inty

U

ncer

tain

ty

Ref

eren

ce

LCR 32 > Profile: 0016

0072 RECIP Caterpillar G342 SI-TA-SC - LCR 32 NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0006 VOC 12.7 0.27 0.27 1

0072 RECIP Caterpillar G342 SI-TA-SC - LCR 32 NGAS Manufacturer 2003 CEL0007 THC 105 0.51 0.51 1

0073 RECIP Caterpillar G342 SI-TA-SC - LCR 54 - Catalyst NGAS

CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0073 RECIP Caterpillar G342 SI-TA-SC - LCR 54 - Catalyst NGAS Manufacturer 2003 630-08-0 CO 1129 0.34 0.34 1

0073 RECIP Caterpillar G342 SI-TA-SC - LCR 54 - Catalyst NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 74-82-8 CH4 99 0.59 0.59 1

0073 RECIP Caterpillar G342 SI-TA-SC - LCR 54 - Catalyst NGAS Manufacturer 2003 CEL0002 NOx 1034 0.09 0.09 1

0073 RECIP Caterpillar G342 SI-TA-SC - LCR 54 - Catalyst NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

0073 RECIP Caterpillar G342 SI-TA-SC - LCR 54 - Catalyst NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

0073 RECIP Caterpillar G342 SI-TA-SC - LCR 54 - Catalyst NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

0073 RECIP Caterpillar G342 SI-TA-SC - LCR 54 - Catalyst NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0006 VOC 12.7 0.27 0.27 1

0073 RECIP Caterpillar G342 SI-TA-SC - LCR 54 - Catalyst NGAS Manufacturer 2003 CEL0007 THC 84 0.51 0.51 1

0074 RECIP Caterpillar G342 SI-TA-SC - LCR 54 - Standard NGAS

CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0074 RECIP Caterpillar G342 SI-TA-SC - LCR 54 - Standard NGAS Manufacturer 2003 630-08-0 CO 84 0.34 0.34 1

0074 RECIP Caterpillar G342 SI-TA-SC - LCR 54 - Standard NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 74-82-8 CH4 99 0.59 0.59 1

0074 RECIP Caterpillar G342 SI-TA-SC - LCR 54 - Standard NGAS Manufacturer 2003 CEL0002 NOx 2163 0.09 0.09 1

0074 RECIP Caterpillar G342 SI-TA-SC - LCR 54 - Standard NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

0074 RECIP Caterpillar G342 SI-TA-SC - LCR 54 - Standard NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

0074 RECIP Caterpillar G342 SI-TA-SC - NGAS U.S. EPA AP-42 - 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

85

Table 3.3 Compilation of combustion emission factors for estimating GHG and CAC emissions.

Fact

or

Equ

ipm

ent

Typ

e

Identifier 1 Identifier 2 Identifier 3 Fuel Type

Factor Reference Y

ear CAS

Number Compound Emission

Factor (ng/J) L

ower

U

ncer

tain

ty

Upp

er

Unc

erta

inty

U

ncer

tain

ty

Ref

eren

ce

LCR 54 - Standard > Profile: 0016

0074 RECIP Caterpillar G342 SI-TA-SC - LCR 54 - Standard NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0006 VOC 12.7 0.27 0.27 1

0074 RECIP Caterpillar G342 SI-TA-SC - LCR 54 - Standard NGAS Manufacturer 2003 CEL0007 THC 84 0.51 0.51 1

0075 RECIP Caterpillar G342 SI-TAA - HCR NGAS

CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0075 RECIP Caterpillar G342 SI-TAA - HCR NGAS Manufacturer 2003 630-08-0 CO 125 0.34 0.34 1

0075 RECIP Caterpillar G342 SI-TAA - HCR NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 74-82-8 CH4 99 0.59 0.59 1

0075 RECIP Caterpillar G342 SI-TAA - HCR NGAS Manufacturer 2003 CEL0002 NOx 1763 0.09 0.09 1

0075 RECIP Caterpillar G342 SI-TAA - HCR NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

0075 RECIP Caterpillar G342 SI-TAA - HCR NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

0075 RECIP Caterpillar G342 SI-TAA - HCR NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

0075 RECIP Caterpillar G342 SI-TAA - HCR NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0006 VOC 12.7 0.27 0.27 1

0075 RECIP Caterpillar G342 SI-TAA - HCR NGAS Manufacturer 2003 CEL0007 THC 91 0.51 0.51 1

0076 RECIP Caterpillar G342 SI-TAA - LCR NGAS

CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0076 RECIP Caterpillar G342 SI-TAA - LCR NGAS Manufacturer 2003 630-08-0 CO 84 0.34 0.34 1

0076 RECIP Caterpillar G342 SI-TAA - LCR NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 74-82-8 CH4 99 0.59 0.59 1

0076 RECIP Caterpillar G342 SI-TAA - LCR NGAS Manufacturer 2003 CEL0002 NOx 1926 0.09 0.09 1

0076 RECIP Caterpillar G342 SI-TAA - LCR NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

0076 RECIP Caterpillar G342 SI-TAA - LCR NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

0076 RECIP Caterpillar G342 SI-TAA - NGAS U.S. EPA AP-42 - 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

86

Table 3.3 Compilation of combustion emission factors for estimating GHG and CAC emissions.

Fact

or

Equ

ipm

ent

Typ

e

Identifier 1 Identifier 2 Identifier 3 Fuel Type

Factor Reference Y

ear CAS

Number Compound Emission

Factor (ng/J) L

ower

U

ncer

tain

ty

Upp

er

Unc

erta

inty

U

ncer

tain

ty

Ref

eren

ce

LCR > Profile: 0016

0076 RECIP Caterpillar G342 SI-TAA - LCR NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0006 VOC 12.7 0.27 0.27 1

0076 RECIP Caterpillar G342 SI-TAA - LCR NGAS Manufacturer 2003 CEL0007 THC 105 0.51 0.51 1

0077 RECIP Caterpillar G3508 HS 130 TA NGAS CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0077 RECIP Caterpillar G3508 HS 130 TA NGAS Manufacturer 2003 630-08-0 CO 45 0.34 0.34 1 0077 RECIP Caterpillar G3508 HS 130 TA NGAS Manufacturer 2003 74-82-8 CH4 113 0.59 0.59 1 0077 RECIP Caterpillar G3508 HS 130 TA NGAS Manufacturer 2003 CEL0002 NOx 2193 0.09 0.09 1

0077 RECIP Caterpillar G3508 HS 130 TA NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

0077 RECIP Caterpillar G3508 HS 130 TA NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

0077 RECIP Caterpillar G3508 HS 130 TA NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

0077 RECIP Caterpillar G3508 HS 130 TA NGAS Manufacturer 2003 CEL0006 VOC 23 0.27 0.27 1 0077 RECIP Caterpillar G3508 HS 130 TA NGAS Manufacturer 2003 CEL0007 THC 136 0.51 0.51 1

0078 RECIP Caterpillar G3508 HS 90 TA NGAS CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0078 RECIP Caterpillar G3508 HS 90 TA NGAS Manufacturer 2003 630-08-0 CO 79 0.34 0.34 1 0078 RECIP Caterpillar G3508 HS 90 TA NGAS Manufacturer 2003 74-82-8 CH4 113 0.59 0.59 1 0078 RECIP Caterpillar G3508 HS 90 TA NGAS Manufacturer 2003 CEL0002 NOx 2365 0.09 0.09 1

0078 RECIP Caterpillar G3508 HS 90 TA NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

0078 RECIP Caterpillar G3508 HS 90 TA NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

0078 RECIP Caterpillar G3508 HS 90 TA NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

0078 RECIP Caterpillar G3508 HS 90 TA NGAS Manufacturer 2003 CEL0006 VOC 23 0.27 0.27 1 0078 RECIP Caterpillar G3508 HS 90 TA NGAS Manufacturer 2003 CEL0007 THC 136 0.51 0.51 1

0079 RECIP Caterpillar G3508 NA NGAS CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0079 RECIP Caterpillar G3508 NA NGAS Manufacturer 2003 630-08-0 CO 1217 0.34 0.34 1 0079 RECIP Caterpillar G3508 NA NGAS Manufacturer 2003 74-82-8 CH4 206 0.59 0.59 1 0079 RECIP Caterpillar G3508 NA NGAS Manufacturer 2003 CEL0002 NOx 1412 0.09 0.09 1

87

Table 3.3 Compilation of combustion emission factors for estimating GHG and CAC emissions.

Fact

or

Equ

ipm

ent

Typ

e

Identifier 1 Identifier 2 Identifier 3 Fuel Type

Factor Reference Y

ear CAS

Number Compound Emission

Factor (ng/J) L

ower

U

ncer

tain

ty

Upp

er

Unc

erta

inty

U

ncer

tain

ty

Ref

eren

ce

0079 RECIP Caterpillar G3508 NA NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

0079 RECIP Caterpillar G3508 NA NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

0079 RECIP Caterpillar G3508 NA NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

0079 RECIP Caterpillar G3508 NA NGAS Manufacturer 2003 CEL0006 VOC 33 0.27 0.27 1 0079 RECIP Caterpillar G3508 NA NGAS Manufacturer 2003 CEL0007 THC 239 0.51 0.51 1

0080 RECIP Caterpillar G3512 HS 130 LE NGAS CHEMEX Labs -> Profile: 0014 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0080 RECIP Caterpillar G3512 HS 130 LE NGAS Manufacturer 2003 630-08-0 CO 200 0.34 0.34 1 0080 RECIP Caterpillar G3512 HS 130 LE NGAS Manufacturer 2003 74-82-8 CH4 364 0.59 0.59 1 0080 RECIP Caterpillar G3512 HS 130 LE NGAS Manufacturer 2003 CEL0002 NOx 588 0.09 0.09 1

0080 RECIP Caterpillar G3512 HS 130 LE NGAS U.S. EPA AP-42 -> Profile: 0014 2000 CEL0003 TPM 0.0332 0.67 1.50 7

0080 RECIP Caterpillar G3512 HS 130 LE NGAS U.S. EPA AP-42 -> Profile: 0014 2000 CEL0004 PM10 0.0332 0.67 1.50 7

0080 RECIP Caterpillar G3512 HS 130 LE NGAS U.S. EPA AP-42 -> Profile: 0014 2000 CEL0005 PM2.5 0.0332 0.67 1.50 7

0080 RECIP Caterpillar G3512 HS 130 LE NGAS Manufacturer 2003 CEL0006 VOC 59 0.27 0.27 1 0080 RECIP Caterpillar G3512 HS 130 LE NGAS Manufacturer 2003 CEL0007 THC 423 0.51 0.51 1

0081 RECIP Caterpillar G3512 HS 130 TA NGAS CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0081 RECIP Caterpillar G3512 HS 130 TA NGAS Manufacturer 2003 630-08-0 CO 90 0.34 0.34 1 0081 RECIP Caterpillar G3512 HS 130 TA NGAS Manufacturer 2003 74-82-8 CH4 101 0.59 0.59 1 0081 RECIP Caterpillar G3512 HS 130 TA NGAS Manufacturer 2003 CEL0002 NOx 2341 0.09 0.09 1

0081 RECIP Caterpillar G3512 HS 130 TA NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

0081 RECIP Caterpillar G3512 HS 130 TA NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

0081 RECIP Caterpillar G3512 HS 130 TA NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

0081 RECIP Caterpillar G3512 HS 130 TA NGAS Manufacturer 2003 CEL0006 VOC 23 0.27 0.27 1 0081 RECIP Caterpillar G3512 HS 130 TA NGAS Manufacturer 2003 CEL0007 THC 124 0.51 0.51 1

0082 RECIP Caterpillar G3512 HS 90 LE NGAS CHEMEX Labs -> Profile: 0014 1996 10024-97-2 N2O 5.72 0.18 5.45 3

88

Table 3.3 Compilation of combustion emission factors for estimating GHG and CAC emissions.

Fact

or

Equ

ipm

ent

Typ

e

Identifier 1 Identifier 2 Identifier 3 Fuel Type

Factor Reference Y

ear CAS

Number Compound Emission

Factor (ng/J) L

ower

U

ncer

tain

ty

Upp

er

Unc

erta

inty

U

ncer

tain

ty

Ref

eren

ce

0082 RECIP Caterpillar G3512 HS 90 LE NGAS Manufacturer 2003 630-08-0 CO 237 0.34 0.34 1 0082 RECIP Caterpillar G3512 HS 90 LE NGAS Manufacturer 2003 74-82-8 CH4 362 0.59 0.59 1 0082 RECIP Caterpillar G3512 HS 90 LE NGAS Manufacturer 2003 CEL0002 NOx 625 0.09 0.09 1

0082 RECIP Caterpillar G3512 HS 90 LE NGAS U.S. EPA AP-42 -> Profile: 0014 2000 CEL0003 TPM 0.0332 0.67 1.50 7

0082 RECIP Caterpillar G3512 HS 90 LE NGAS U.S. EPA AP-42 -> Profile: 0014 2000 CEL0004 PM10 0.0332 0.67 1.50 7

0082 RECIP Caterpillar G3512 HS 90 LE NGAS U.S. EPA AP-42 -> Profile: 0014 2000 CEL0005 PM2.5 0.0332 0.67 1.50 7

0082 RECIP Caterpillar G3512 HS 90 LE NGAS Manufacturer 2003 CEL0006 VOC 62 0.27 0.27 1 0082 RECIP Caterpillar G3512 HS 90 LE NGAS Manufacturer 2003 CEL0007 THC 425 0.51 0.51 1

0083 RECIP Caterpillar G3512 HS 90 TA NGAS CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0083 RECIP Caterpillar G3512 HS 90 TA NGAS Manufacturer 2003 630-08-0 CO 79 0.34 0.34 1 0083 RECIP Caterpillar G3512 HS 90 TA NGAS Manufacturer 2003 74-82-8 CH4 125 0.59 0.59 1 0083 RECIP Caterpillar G3512 HS 90 TA NGAS Manufacturer 2003 CEL0002 NOx 2501 0.09 0.09 1

0083 RECIP Caterpillar G3512 HS 90 TA NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

0083 RECIP Caterpillar G3512 HS 90 TA NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

0083 RECIP Caterpillar G3512 HS 90 TA NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

0083 RECIP Caterpillar G3512 HS 90 TA NGAS Manufacturer 2003 CEL0006 VOC 23 0.27 0.27 1 0083 RECIP Caterpillar G3512 HS 90 TA NGAS Manufacturer 2003 CEL0007 THC 147 0.51 0.51 1

0084 RECIP Caterpillar G3512 LS 130 LE NGAS CHEMEX Labs -> Profile: 0014 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0084 RECIP Caterpillar G3512 LS 130 LE NGAS Manufacturer 2003 630-08-0 CO 227 0.34 0.34 1 0084 RECIP Caterpillar G3512 LS 130 LE NGAS Manufacturer 2003 74-82-8 CH4 371 0.59 0.59 1 0084 RECIP Caterpillar G3512 LS 130 LE NGAS Manufacturer 2003 CEL0002 NOx 215 0.09 0.09 1

0084 RECIP Caterpillar G3512 LS 130 LE NGAS U.S. EPA AP-42 -> Profile: 0014 2000 CEL0003 TPM 0.0332 0.67 1.50 7

0084 RECIP Caterpillar G3512 LS 130 LE NGAS U.S. EPA AP-42 -> Profile: 0014 2000 CEL0004 PM10 0.0332 0.67 1.50 7

0084 RECIP Caterpillar G3512 LS 130 LE NGAS U.S. EPA AP-42 -> Profile: 0014 2000 CEL0005 PM2.5 0.0332 0.67 1.50 7

0084 RECIP Caterpillar G3512 LS 130 LE NGAS Manufacturer 2003 CEL0006 VOC 72 0.27 0.27 1

89

Table 3.3 Compilation of combustion emission factors for estimating GHG and CAC emissions.

Fact

or

Equ

ipm

ent

Typ

e

Identifier 1 Identifier 2 Identifier 3 Fuel Type

Factor Reference Y

ear CAS

Number Compound Emission

Factor (ng/J) L

ower

U

ncer

tain

ty

Upp

er

Unc

erta

inty

U

ncer

tain

ty

Ref

eren

ce

0084 RECIP Caterpillar G3512 LS 130 LE NGAS Manufacturer 2003 CEL0007 THC 443 0.51 0.51 1

0085 RECIP Caterpillar G3512 LS 130 TA NGAS CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0085 RECIP Caterpillar G3512 LS 130 TA NGAS Manufacturer 2003 630-08-0 CO 77 0.34 0.34 1 0085 RECIP Caterpillar G3512 LS 130 TA NGAS Manufacturer 2003 74-82-8 CH4 100 0.59 0.59 1 0085 RECIP Caterpillar G3512 LS 130 TA NGAS Manufacturer 2003 CEL0002 NOx 2545 0.09 0.09 1

0085 RECIP Caterpillar G3512 LS 130 TA NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

0085 RECIP Caterpillar G3512 LS 130 TA NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

0085 RECIP Caterpillar G3512 LS 130 TA NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

0085 RECIP Caterpillar G3512 LS 130 TA NGAS Manufacturer 2003 CEL0006 VOC 22 0.27 0.27 1 0085 RECIP Caterpillar G3512 LS 130 TA NGAS Manufacturer 2003 CEL0007 THC 122 0.51 0.51 1

0086 RECIP Caterpillar G3512 LS 90 LE NGAS CHEMEX Labs -> Profile: 0014 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0086 RECIP Caterpillar G3512 LS 90 LE NGAS Manufacturer 2003 630-08-0 CO 278 0.34 0.34 1 0086 RECIP Caterpillar G3512 LS 90 LE NGAS Manufacturer 2003 74-82-8 CH4 519 0.59 0.59 1 0086 RECIP Caterpillar G3512 LS 90 LE NGAS Manufacturer 2003 CEL0002 NOx 229 0.09 0.09 1

0086 RECIP Caterpillar G3512 LS 90 LE NGAS U.S. EPA AP-42 -> Profile: 0014 2000 CEL0003 TPM 0.0332 0.67 1.50 7

0086 RECIP Caterpillar G3512 LS 90 LE NGAS U.S. EPA AP-42 -> Profile: 0014 2000 CEL0004 PM10 0.0332 0.67 1.50 7

0086 RECIP Caterpillar G3512 LS 90 LE NGAS U.S. EPA AP-42 -> Profile: 0014 2000 CEL0005 PM2.5 0.0332 0.67 1.50 7

0086 RECIP Caterpillar G3512 LS 90 LE NGAS Manufacturer 2003 CEL0006 VOC 72 0.27 0.27 1 0086 RECIP Caterpillar G3512 LS 90 LE NGAS Manufacturer 2003 CEL0007 THC 592 0.51 0.51 1

0087 RECIP Caterpillar G3512 LS 90 TA NGAS CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0087 RECIP Caterpillar G3512 LS 90 TA NGAS Manufacturer 2003 630-08-0 CO 79 0.34 0.34 1 0087 RECIP Caterpillar G3512 LS 90 TA NGAS Manufacturer 2003 74-82-8 CH4 112 0.59 0.59 1 0087 RECIP Caterpillar G3512 LS 90 TA NGAS Manufacturer 2003 CEL0002 NOx 2362 0.09 0.09 1

0087 RECIP Caterpillar G3512 LS 90 TA NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

0087 RECIP Caterpillar G3512 LS 90 TA NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

90

Table 3.3 Compilation of combustion emission factors for estimating GHG and CAC emissions.

Fact

or

Equ

ipm

ent

Typ

e

Identifier 1 Identifier 2 Identifier 3 Fuel Type

Factor Reference Y

ear CAS

Number Compound Emission

Factor (ng/J) L

ower

U

ncer

tain

ty

Upp

er

Unc

erta

inty

U

ncer

tain

ty

Ref

eren

ce

0087 RECIP Caterpillar G3512 LS 90 TA NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

0087 RECIP Caterpillar G3512 LS 90 TA NGAS Manufacturer 2003 CEL0006 VOC 22 0.27 0.27 1 0087 RECIP Caterpillar G3512 LS 90 TA NGAS Manufacturer 2003 CEL0007 THC 135 0.51 0.51 1

0088 RECIP Caterpillar G3512 NA NGAS CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0088 RECIP Caterpillar G3512 NA NGAS Manufacturer 2003 630-08-0 CO 1331 0.34 0.34 1 0088 RECIP Caterpillar G3512 NA NGAS Manufacturer 2003 74-82-8 CH4 236 0.59 0.59 1 0088 RECIP Caterpillar G3512 NA NGAS Manufacturer 2003 CEL0002 NOx 1310 0.09 0.09 1

0088 RECIP Caterpillar G3512 NA NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

0088 RECIP Caterpillar G3512 NA NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

0088 RECIP Caterpillar G3512 NA NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

0088 RECIP Caterpillar G3512 NA NGAS Manufacturer 2003 CEL0006 VOC 43 0.27 0.27 1 0088 RECIP Caterpillar G3512 NA NGAS Manufacturer 2003 CEL0007 THC 279 0.51 0.51 1

0089 RECIP Caterpillar G3516 HS 130 LE NGAS CHEMEX Labs -> Profile: 0014 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0089 RECIP Caterpillar G3516 HS 130 LE NGAS Manufacturer 2003 630-08-0 CO 210 0.34 0.34 1 0089 RECIP Caterpillar G3516 HS 130 LE NGAS Manufacturer 2003 74-82-8 CH4 321 0.59 0.59 1 0089 RECIP Caterpillar G3516 HS 130 LE NGAS Manufacturer 2003 CEL0002 NOx 618 0.09 0.09 1

0089 RECIP Caterpillar G3516 HS 130 LE NGAS U.S. EPA AP-42 -> Profile: 0014 2000 CEL0003 TPM 0.0332 0.67 1.50 7

0089 RECIP Caterpillar G3516 HS 130 LE NGAS U.S. EPA AP-42 -> Profile: 0014 2000 CEL0004 PM10 0.0332 0.67 1.50 7

0089 RECIP Caterpillar G3516 HS 130 LE NGAS U.S. EPA AP-42 -> Profile: 0014 2000 CEL0005 PM2.5 0.0332 0.67 1.50 7

0089 RECIP Caterpillar G3516 HS 130 LE NGAS Manufacturer 2003 CEL0006 VOC 62 0.27 0.27 1 0089 RECIP Caterpillar G3516 HS 130 LE NGAS Manufacturer 2003 CEL0007 THC 383 0.51 0.51 1

0090 RECIP Caterpillar G3516 HS 130 TA NGAS CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0090 RECIP Caterpillar G3516 HS 130 TA NGAS Manufacturer 2003 630-08-0 CO 90 0.34 0.34 1 0090 RECIP Caterpillar G3516 HS 130 TA NGAS Manufacturer 2003 74-82-8 CH4 79 0.59 0.59 1 0090 RECIP Caterpillar G3516 HS 130 TA NGAS Manufacturer 2003 CEL0002 NOx 2274 0.09 0.09 1 0090 RECIP Caterpillar G3516 HS 130 TA NGAS U.S. EPA AP-42 - 2000 CEL0003 TPM 4.09 0.50 2.00 8

91

Table 3.3 Compilation of combustion emission factors for estimating GHG and CAC emissions.

Fact

or

Equ

ipm

ent

Typ

e

Identifier 1 Identifier 2 Identifier 3 Fuel Type

Factor Reference Y

ear CAS

Number Compound Emission

Factor (ng/J) L

ower

U

ncer

tain

ty

Upp

er

Unc

erta

inty

U

ncer

tain

ty

Ref

eren

ce

> Profile: 0016

0090 RECIP Caterpillar G3516 HS 130 TA NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

0090 RECIP Caterpillar G3516 HS 130 TA NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

0090 RECIP Caterpillar G3516 HS 130 TA NGAS Manufacturer 2003 CEL0006 VOC 11 0.27 0.27 1 0090 RECIP Caterpillar G3516 HS 130 TA NGAS Manufacturer 2003 CEL0007 THC 90 0.51 0.51 1

0091 RECIP Caterpillar G3516 HS 90 LE NGAS CHEMEX Labs -> Profile: 0014 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0091 RECIP Caterpillar G3516 HS 90 LE NGAS Manufacturer 2003 630-08-0 CO 210 0.34 0.34 1 0091 RECIP Caterpillar G3516 HS 90 LE NGAS Manufacturer 2003 74-82-8 CH4 272 0.59 0.59 1 0091 RECIP Caterpillar G3516 HS 90 LE NGAS Manufacturer 2003 CEL0002 NOx 618 0.09 0.09 1

0091 RECIP Caterpillar G3516 HS 90 LE NGAS U.S. EPA AP-42 -> Profile: 0014 2000 CEL0003 TPM 0.0332 0.67 1.50 7

0091 RECIP Caterpillar G3516 HS 90 LE NGAS U.S. EPA AP-42 -> Profile: 0014 2000 CEL0004 PM10 0.0332 0.67 1.50 7

0091 RECIP Caterpillar G3516 HS 90 LE NGAS U.S. EPA AP-42 -> Profile: 0014 2000 CEL0005 PM2.5 0.0332 0.67 1.50 7

0091 RECIP Caterpillar G3516 HS 90 LE NGAS Manufacturer 2003 CEL0006 VOC 49 0.27 0.27 1 0091 RECIP Caterpillar G3516 HS 90 LE NGAS Manufacturer 2003 CEL0007 THC 321 0.51 0.51 1

0092 RECIP Caterpillar G3516 HS 90 TA NGAS CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0092 RECIP Caterpillar G3516 HS 90 TA NGAS Manufacturer 2003 630-08-0 CO 89 0.34 0.34 1 0092 RECIP Caterpillar G3516 HS 90 TA NGAS Manufacturer 2003 74-82-8 CH4 67 0.59 0.59 1 0092 RECIP Caterpillar G3516 HS 90 TA NGAS Manufacturer 2003 CEL0002 NOx 2010 0.09 0.09 1

0092 RECIP Caterpillar G3516 HS 90 TA NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

0092 RECIP Caterpillar G3516 HS 90 TA NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

0092 RECIP Caterpillar G3516 HS 90 TA NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

0092 RECIP Caterpillar G3516 HS 90 TA NGAS Manufacturer 2003 CEL0006 VOC 11 0.27 0.27 1 0092 RECIP Caterpillar G3516 HS 90 TA NGAS Manufacturer 2003 CEL0007 THC 78 0.51 0.51 1

0093 RECIP Caterpillar G3516 LS 130 LE NGAS CHEMEX Labs -> Profile: 0014 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0093 RECIP Caterpillar G3516 LS 130 LE NGAS Manufacturer 2003 630-08-0 CO 210 0.34 0.34 1

92

Table 3.3 Compilation of combustion emission factors for estimating GHG and CAC emissions.

Fact

or

Equ

ipm

ent

Typ

e

Identifier 1 Identifier 2 Identifier 3 Fuel Type

Factor Reference Y

ear CAS

Number Compound Emission

Factor (ng/J) L

ower

U

ncer

tain

ty

Upp

er

Unc

erta

inty

U

ncer

tain

ty

Ref

eren

ce

0093 RECIP Caterpillar G3516 LS 130 LE NGAS Manufacturer 2003 74-82-8 CH4 519 0.59 0.59 1 0093 RECIP Caterpillar G3516 LS 130 LE NGAS Manufacturer 2003 CEL0002 NOx 223 0.09 0.09 1

0093 RECIP Caterpillar G3516 LS 130 LE NGAS U.S. EPA AP-42 -> Profile: 0014 2000 CEL0003 TPM 0.0332 0.67 1.50 7

0093 RECIP Caterpillar G3516 LS 130 LE NGAS U.S. EPA AP-42 -> Profile: 0014 2000 CEL0004 PM10 0.0332 0.67 1.50 7

0093 RECIP Caterpillar G3516 LS 130 LE NGAS U.S. EPA AP-42 -> Profile: 0014 2000 CEL0005 PM2.5 0.0332 0.67 1.50 7

0093 RECIP Caterpillar G3516 LS 130 LE NGAS Manufacturer 2003 CEL0006 VOC 74 0.27 0.27 1 0093 RECIP Caterpillar G3516 LS 130 LE NGAS Manufacturer 2003 CEL0007 THC 594 0.51 0.51 1

0094 RECIP Caterpillar G3516 LS 90 LE NGAS CHEMEX Labs -> Profile: 0014 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0094 RECIP Caterpillar G3516 LS 90 LE NGAS Manufacturer 2003 630-08-0 CO 223 0.34 0.34 1 0094 RECIP Caterpillar G3516 LS 90 LE NGAS Manufacturer 2003 74-82-8 CH4 571 0.59 0.59 1 0094 RECIP Caterpillar G3516 LS 90 LE NGAS Manufacturer 2003 CEL0002 NOx 248 0.09 0.09 1

0094 RECIP Caterpillar G3516 LS 90 LE NGAS U.S. EPA AP-42 -> Profile: 0014 2000 CEL0003 TPM 0.0332 0.67 1.50 7

0094 RECIP Caterpillar G3516 LS 90 LE NGAS U.S. EPA AP-42 -> Profile: 0014 2000 CEL0004 PM10 0.0332 0.67 1.50 7

0094 RECIP Caterpillar G3516 LS 90 LE NGAS U.S. EPA AP-42 -> Profile: 0014 2000 CEL0005 PM2.5 0.0332 0.67 1.50 7

0094 RECIP Caterpillar G3516 LS 90 LE NGAS Manufacturer 2003 CEL0006 VOC 87 0.27 0.27 1 0094 RECIP Caterpillar G3516 LS 90 LE NGAS Manufacturer 2003 CEL0007 THC 658 0.51 0.51 1

0095 RECIP Caterpillar G3516 NA NGAS CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0095 RECIP Caterpillar G3516 NA NGAS Manufacturer 2003 630-08-0 CO 3493 0.34 0.34 1 0095 RECIP Caterpillar G3516 NA NGAS Manufacturer 2003 74-82-8 CH4 222 0.59 0.59 1 0095 RECIP Caterpillar G3516 NA NGAS Manufacturer 2003 CEL0002 NOx 1076 0.09 0.09 1

0095 RECIP Caterpillar G3516 NA NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

0095 RECIP Caterpillar G3516 NA NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

0095 RECIP Caterpillar G3516 NA NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

0095 RECIP Caterpillar G3516 NA NGAS Manufacturer 2003 CEL0006 VOC 42 0.27 0.27 1 0095 RECIP Caterpillar G3516 NA NGAS Manufacturer 2003 CEL0007 THC 264 0.51 0.51 1

93

Table 3.3 Compilation of combustion emission factors for estimating GHG and CAC emissions.

Fact

or

Equ

ipm

ent

Typ

e

Identifier 1 Identifier 2 Identifier 3 Fuel Type

Factor Reference Y

ear CAS

Number Compound Emission

Factor (ng/J) L

ower

U

ncer

tain

ty

Upp

er

Unc

erta

inty

U

ncer

tain

ty

Ref

eren

ce

0096 RECIP Caterpillar G3606 SITA 130 NGAS CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0096 RECIP Caterpillar G3606 SITA 130 NGAS Manufacturer 2003 630-08-0 CO 225 0.34 0.34 1 0096 RECIP Caterpillar G3606 SITA 130 NGAS Manufacturer 2003 74-82-8 CH4 486 0.59 0.59 1 0096 RECIP Caterpillar G3606 SITA 130 NGAS Manufacturer 2003 CEL0002 NOx 121 0.09 0.09 1

0096 RECIP Caterpillar G3606 SITA 130 NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

0096 RECIP Caterpillar G3606 SITA 130 NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

0096 RECIP Caterpillar G3606 SITA 130 NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

0096 RECIP Caterpillar G3606 SITA 130 NGAS Manufacturer 2003 CEL0006 VOC 85 0.27 0.27 1 0096 RECIP Caterpillar G3606 SITA 130 NGAS Manufacturer 2003 CEL0007 THC 571 0.51 0.51 1

0097 RECIP Caterpillar G3608 SITA 130 NGAS CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0097 RECIP Caterpillar G3608 SITA 130 NGAS Manufacturer 2003 630-08-0 CO 233 0.34 0.34 1 0097 RECIP Caterpillar G3608 SITA 130 NGAS Manufacturer 2003 74-82-8 CH4 491 0.59 0.59 1 0097 RECIP Caterpillar G3608 SITA 130 NGAS Manufacturer 2003 CEL0002 NOx 123 0.09 0.09 1

0097 RECIP Caterpillar G3608 SITA 130 NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

0097 RECIP Caterpillar G3608 SITA 130 NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

0097 RECIP Caterpillar G3608 SITA 130 NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

0097 RECIP Caterpillar G3608 SITA 130 NGAS Manufacturer 2003 CEL0006 VOC 86 0.27 0.27 1 0097 RECIP Caterpillar G3608 SITA 130 NGAS Manufacturer 2003 CEL0007 THC 577 0.51 0.51 1

0098 RECIP Caterpillar G3612 SITA 130 NGAS CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0098 RECIP Caterpillar G3612 SITA 130 NGAS Manufacturer 2003 630-08-0 CO 234 0.34 0.34 1 0098 RECIP Caterpillar G3612 SITA 130 NGAS Manufacturer 2003 74-82-8 CH4 493 0.59 0.59 1 0098 RECIP Caterpillar G3612 SITA 130 NGAS Manufacturer 2003 CEL0002 NOx 86 0.09 0.09 1

0098 RECIP Caterpillar G3612 SITA 130 NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

0098 RECIP Caterpillar G3612 SITA 130 NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

0098 RECIP Caterpillar G3612 SITA 130 NGAS U.S. EPA AP-42 - 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

94

Table 3.3 Compilation of combustion emission factors for estimating GHG and CAC emissions.

Fact

or

Equ

ipm

ent

Typ

e

Identifier 1 Identifier 2 Identifier 3 Fuel Type

Factor Reference Y

ear CAS

Number Compound Emission

Factor (ng/J) L

ower

U

ncer

tain

ty

Upp

er

Unc

erta

inty

U

ncer

tain

ty

Ref

eren

ce

> Profile: 0016 0098 RECIP Caterpillar G3612 SITA 130 NGAS Manufacturer 2003 CEL0006 VOC 86 0.27 0.27 1 0098 RECIP Caterpillar G3612 SITA 130 NGAS Manufacturer 2003 CEL0007 THC 579 0.51 0.51 1

0099 RECIP Caterpillar G3616 SITA 130 NGAS CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0099 RECIP Caterpillar G3616 SITA 130 NGAS Manufacturer 2003 630-08-0 CO 236 0.34 0.34 1 0099 RECIP Caterpillar G3616 SITA 130 NGAS Manufacturer 2003 74-82-8 CH4 559 0.59 0.59 1 0099 RECIP Caterpillar G3616 SITA 130 NGAS Manufacturer 2003 CEL0002 NOx 87 0.09 0.09 1

0099 RECIP Caterpillar G3616 SITA 130 NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

0099 RECIP Caterpillar G3616 SITA 130 NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

0099 RECIP Caterpillar G3616 SITA 130 NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

0099 RECIP Caterpillar G3616 SITA 130 NGAS Manufacturer 2003 CEL0006 VOC 99 0.27 0.27 1 0099 RECIP Caterpillar G3616 SITA 130 NGAS Manufacturer 2003 CEL0007 THC 658 0.51 0.51 1

0100 RECIP Caterpillar G379 SI-NA - HCR NGAS

CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0100 RECIP Caterpillar G379 SI-NA - HCR NGAS Manufacturer 2003 630-08-0 CO 866 0.34 0.34 1

0100 RECIP Caterpillar G379 SI-NA - HCR NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 74-82-8 CH4 99 0.59 0.59 1

0100 RECIP Caterpillar G379 SI-NA - HCR NGAS Manufacturer 2003 CEL0002 NOx 953 0.09 0.09 1

0100 RECIP Caterpillar G379 SI-NA - HCR NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

0100 RECIP Caterpillar G379 SI-NA - HCR NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

0100 RECIP Caterpillar G379 SI-NA - HCR NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

0100 RECIP Caterpillar G379 SI-NA - HCR NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0006 VOC 12.7 0.27 0.27 1

0100 RECIP Caterpillar G379 SI-NA - HCR NGAS Manufacturer 2003 CEL0007 THC 340 0.51 0.51 1

0101 RECIP Caterpillar G379 SI-NA - LCR NGAS CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

95

Table 3.3 Compilation of combustion emission factors for estimating GHG and CAC emissions.

Fact

or

Equ

ipm

ent

Typ

e

Identifier 1 Identifier 2 Identifier 3 Fuel Type

Factor Reference Y

ear CAS

Number Compound Emission

Factor (ng/J) L

ower

U

ncer

tain

ty

Upp

er

Unc

erta

inty

U

ncer

tain

ty

Ref

eren

ce

0101 RECIP Caterpillar G379 SI-NA - LCR NGAS Manufacturer 2003 630-08-0 CO 1129 0.34 0.34 1

0101 RECIP Caterpillar G379 SI-NA - LCR NGAS U.S. EPA AP-42 -> Profile: 0016 2000 74-82-8 CH4 99 0.59 0.59 1

0101 RECIP Caterpillar G379 SI-NA - LCR NGAS Manufacturer 2003 CEL0002 NOx 1119 0.09 0.09 1

0101 RECIP Caterpillar G379 SI-NA - LCR NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

0101 RECIP Caterpillar G379 SI-NA - LCR NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

0101 RECIP Caterpillar G379 SI-NA - LCR NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

0101 RECIP Caterpillar G379 SI-NA - LCR NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0006 VOC 12.7 0.27 0.27 1

0101 RECIP Caterpillar G379 SI-NA - LCR NGAS Manufacturer 2003 CEL0007 THC 79 0.51 0.51 1

0102 RECIP Caterpillar G379 SI-TA-SC - HCR 32 - Catalyst NGAS

CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0102 RECIP Caterpillar G379 SI-TA-SC - HCR 32 - Catalyst NGAS Manufacturer 2003 630-08-0 CO 1255 0.34 0.34 1

0102 RECIP Caterpillar G379 SI-TA-SC - HCR 32 - Catalyst NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 74-82-8 CH4 99 0.59 0.59 1

0102 RECIP Caterpillar G379 SI-TA-SC - HCR 32 - Catalyst NGAS Manufacturer 2003 CEL0002 NOx 1210 0.09 0.09 1

0102 RECIP Caterpillar G379 SI-TA-SC - HCR 32 - Catalyst NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

0102 RECIP Caterpillar G379 SI-TA-SC - HCR 32 - Catalyst NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

0102 RECIP Caterpillar G379 SI-TA-SC - HCR 32 - Catalyst NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

0102 RECIP Caterpillar G379 SI-TA-SC - HCR 32 - Catalyst NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0006 VOC 12.7 0.27 0.27 1

0102 RECIP Caterpillar G379 SI-TA-SC - HCR 32 - Catalyst NGAS Manufacturer 2003 CEL0007 THC 215 0.51 0.51 1

0103 RECIP Caterpillar G379 SI-TA-SC - HCR 32 - Standard NGAS

CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0103 RECIP Caterpillar G379 SI-TA-SC - HCR 32 - Standard NGAS Manufacturer 2003 630-08-0 CO 126 0.34 0.34 1

0103 RECIP Caterpillar G379 SI-TA-SC - NGAS U.S. EPA AP-42 - 2000 74-82-8 CH4 99 0.59 0.59 1

96

Table 3.3 Compilation of combustion emission factors for estimating GHG and CAC emissions.

Fact

or

Equ

ipm

ent

Typ

e

Identifier 1 Identifier 2 Identifier 3 Fuel Type

Factor Reference Y

ear CAS

Number Compound Emission

Factor (ng/J) L

ower

U

ncer

tain

ty

Upp

er

Unc

erta

inty

U

ncer

tain

ty

Ref

eren

ce

HCR 32 - Standard > Profile: 0016

0103 RECIP Caterpillar G379 SI-TA-SC - HCR 32 - Standard NGAS Manufacturer 2003 CEL0002 NOx 1765 0.09 0.09 1

0103 RECIP Caterpillar G379 SI-TA-SC - HCR 32 - Standard NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

0103 RECIP Caterpillar G379 SI-TA-SC - HCR 32 - Standard NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

0103 RECIP Caterpillar G379 SI-TA-SC - HCR 32 - Standard NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

0103 RECIP Caterpillar G379 SI-TA-SC - HCR 32 - Standard NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0006 VOC 12.7 0.27 0.27 1

0103 RECIP Caterpillar G379 SI-TA-SC - HCR 32 - Standard NGAS Manufacturer 2003 CEL0007 THC 103 0.51 0.51 1

0104 RECIP Caterpillar G379 SI-TA-SC - LCR 32 NGAS

CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0104 RECIP Caterpillar G379 SI-TA-SC - LCR 32 NGAS Manufacturer 2003 630-08-0 CO 84 0.34 0.34 1

0104 RECIP Caterpillar G379 SI-TA-SC - LCR 32 NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 74-82-8 CH4 99 0.59 0.59 1

0104 RECIP Caterpillar G379 SI-TA-SC - LCR 32 NGAS Manufacturer 2003 CEL0002 NOx 1979 0.09 0.09 1

0104 RECIP Caterpillar G379 SI-TA-SC - LCR 32 NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

0104 RECIP Caterpillar G379 SI-TA-SC - LCR 32 NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

0104 RECIP Caterpillar G379 SI-TA-SC - LCR 32 NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

0104 RECIP Caterpillar G379 SI-TA-SC - LCR 32 NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0006 VOC 12.7 0.27 0.27 1

0104 RECIP Caterpillar G379 SI-TA-SC - LCR 32 NGAS Manufacturer 2003 CEL0007 THC 105 0.51 0.51 1

0105 RECIP Caterpillar G379 SI-TA-SC - LCR 54 - Catalyst NGAS

CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0105 RECIP Caterpillar G379 SI-TA-SC - LCR 54 - Catalyst NGAS Manufacturer 2003 630-08-0 CO 1148 0.34 0.34 1

0105 RECIP Caterpillar G379 SI-TA-SC - NGAS U.S. EPA AP-42 - 2000 74-82-8 CH4 99 0.59 0.59 1

97

Table 3.3 Compilation of combustion emission factors for estimating GHG and CAC emissions.

Fact

or

Equ

ipm

ent

Typ

e

Identifier 1 Identifier 2 Identifier 3 Fuel Type

Factor Reference Y

ear CAS

Number Compound Emission

Factor (ng/J) L

ower

U

ncer

tain

ty

Upp

er

Unc

erta

inty

U

ncer

tain

ty

Ref

eren

ce

LCR 54 - Catalyst > Profile: 0016

0105 RECIP Caterpillar G379 SI-TA-SC - LCR 54 - Catalyst NGAS Manufacturer 2003 CEL0002 NOx 1052 0.09 0.09 1

0105 RECIP Caterpillar G379 SI-TA-SC - LCR 54 - Catalyst NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

0105 RECIP Caterpillar G379 SI-TA-SC - LCR 54 - Catalyst NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

0105 RECIP Caterpillar G379 SI-TA-SC - LCR 54 - Catalyst NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

0105 RECIP Caterpillar G379 SI-TA-SC - LCR 54 - Catalyst NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0006 VOC 12.7 0.27 0.27 1

0105 RECIP Caterpillar G379 SI-TA-SC - LCR 54 - Catalyst NGAS Manufacturer 2003 CEL0007 THC 86 0.51 0.51 1

0106 RECIP Caterpillar G379 SI-TA-SC - LCR 54 - Standard NGAS

CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0106 RECIP Caterpillar G379 SI-TA-SC - LCR 54 - Standard NGAS Manufacturer 2003 630-08-0 CO 89 0.34 0.34 1

0106 RECIP Caterpillar G379 SI-TA-SC - LCR 54 - Standard NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 74-82-8 CH4 99 0.59 0.59 1

0106 RECIP Caterpillar G379 SI-TA-SC - LCR 54 - Standard NGAS Manufacturer 2003 CEL0002 NOx 2321 0.09 0.09 1

0106 RECIP Caterpillar G379 SI-TA-SC - LCR 54 - Standard NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

0106 RECIP Caterpillar G379 SI-TA-SC - LCR 54 - Standard NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

0106 RECIP Caterpillar G379 SI-TA-SC - LCR 54 - Standard NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

0106 RECIP Caterpillar G379 SI-TA-SC - LCR 54 - Standard NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0006 VOC 12.7 0.27 0.27 1

0106 RECIP Caterpillar G379 SI-TA-SC - LCR 54 - Standard NGAS Manufacturer 2003 CEL0007 THC 89 0.51 0.51 1

0107 RECIP Caterpillar G379 SI-TAA - HCR NGAS

CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0107 RECIP Caterpillar G379 SI-TAA - HCR NGAS Manufacturer 2003 630-08-0 CO 123 0.34 0.34 1

0107 RECIP Caterpillar G379 SI-TAA - NGAS U.S. EPA AP-42 - 2000 74-82-8 CH4 99 0.59 0.59 1

98

Table 3.3 Compilation of combustion emission factors for estimating GHG and CAC emissions.

Fact

or

Equ

ipm

ent

Typ

e

Identifier 1 Identifier 2 Identifier 3 Fuel Type

Factor Reference Y

ear CAS

Number Compound Emission

Factor (ng/J) L

ower

U

ncer

tain

ty

Upp

er

Unc

erta

inty

U

ncer

tain

ty

Ref

eren

ce

HCR > Profile: 0016

0107 RECIP Caterpillar G379 SI-TAA - HCR NGAS Manufacturer 2003 CEL0002 NOx 1722 0.09 0.09 1

0107 RECIP Caterpillar G379 SI-TAA - HCR NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

0107 RECIP Caterpillar G379 SI-TAA - HCR NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

0107 RECIP Caterpillar G379 SI-TAA - HCR NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

0107 RECIP Caterpillar G379 SI-TAA - HCR NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0006 VOC 12.7 0.27 0.27 1

0107 RECIP Caterpillar G379 SI-TAA - HCR NGAS Manufacturer 2003 CEL0007 THC 101 0.51 0.51 1

0108 RECIP Caterpillar G379 SI-TAA - LCR NGAS

CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0108 RECIP Caterpillar G379 SI-TAA - LCR NGAS Manufacturer 2003 630-08-0 CO 84 0.34 0.34 1

0108 RECIP Caterpillar G379 SI-TAA - LCR NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 74-82-8 CH4 99 0.59 0.59 1

0108 RECIP Caterpillar G379 SI-TAA - LCR NGAS Manufacturer 2003 CEL0002 NOx 1979 0.09 0.09 1

0108 RECIP Caterpillar G379 SI-TAA - LCR NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

0108 RECIP Caterpillar G379 SI-TAA - LCR NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

0108 RECIP Caterpillar G379 SI-TAA - LCR NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

0108 RECIP Caterpillar G379 SI-TAA - LCR NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0006 VOC 12.7 0.27 0.27 1

0108 RECIP Caterpillar G379 SI-TAA - LCR NGAS Manufacturer 2003 CEL0007 THC 105 0.51 0.51 1

0109 RECIP Caterpillar G398 SI-NA - HCR NGAS

CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0109 RECIP Caterpillar G398 SI-NA - HCR NGAS Manufacturer 2003 630-08-0 CO 1522 0.34 0.34 1

0109 RECIP Caterpillar G398 SI-NA - NGAS U.S. EPA AP-42 - 2000 74-82-8 CH4 99 0.59 0.59 1

99

Table 3.3 Compilation of combustion emission factors for estimating GHG and CAC emissions.

Fact

or

Equ

ipm

ent

Typ

e

Identifier 1 Identifier 2 Identifier 3 Fuel Type

Factor Reference Y

ear CAS

Number Compound Emission

Factor (ng/J) L

ower

U

ncer

tain

ty

Upp

er

Unc

erta

inty

U

ncer

tain

ty

Ref

eren

ce

HCR > Profile: 0016

0109 RECIP Caterpillar G398 SI-NA - HCR NGAS Manufacturer 2003 CEL0002 NOx 1411 0.09 0.09 1

0109 RECIP Caterpillar G398 SI-NA - HCR NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

0109 RECIP Caterpillar G398 SI-NA - HCR NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

0109 RECIP Caterpillar G398 SI-NA - HCR NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

0109 RECIP Caterpillar G398 SI-NA - HCR NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0006 VOC 12.7 0.27 0.27 1

0109 RECIP Caterpillar G398 SI-NA - HCR NGAS Manufacturer 2003 CEL0007 THC 222 0.51 0.51 1

0110 RECIP Caterpillar G398 SI-NA - LCR NGAS CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0110 RECIP Caterpillar G398 SI-NA - LCR NGAS Manufacturer 2003 630-08-0 CO 1135 0.34 0.34 1

0110 RECIP Caterpillar G398 SI-NA - LCR NGAS U.S. EPA AP-42 -> Profile: 0016 2000 74-82-8 CH4 99 0.59 0.59 1

0110 RECIP Caterpillar G398 SI-NA - LCR NGAS Manufacturer 2003 CEL0002 NOx 1125 0.09 0.09 1

0110 RECIP Caterpillar G398 SI-NA - LCR NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

0110 RECIP Caterpillar G398 SI-NA - LCR NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

0110 RECIP Caterpillar G398 SI-NA - LCR NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

0110 RECIP Caterpillar G398 SI-NA - LCR NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0006 VOC 12.7 0.27 0.27 1

0110 RECIP Caterpillar G398 SI-NA - LCR NGAS Manufacturer 2003 CEL0007 THC 79 0.51 0.51 1

0111 RECIP Caterpillar G398 SI-TA-SC - HCR 32 - Catalyst NGAS

CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0111 RECIP Caterpillar G398 SI-TA-SC - HCR 32 - Catalyst NGAS Manufacturer 2003 630-08-0 CO 1065 0.34 0.34 1

0111 RECIP Caterpillar G398 SI-TA-SC - HCR 32 - Catalyst NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 74-82-8 CH4 99 0.59 0.59 1

0111 RECIP Caterpillar G398 SI-TA-SC - HCR 32 - Catalyst NGAS Manufacturer 2003 CEL0002 NOx 1011 0.09 0.09 1

100

Table 3.3 Compilation of combustion emission factors for estimating GHG and CAC emissions.

Fact

or

Equ

ipm

ent

Typ

e

Identifier 1 Identifier 2 Identifier 3 Fuel Type

Factor Reference Y

ear CAS

Number Compound Emission

Factor (ng/J) L

ower

U

ncer

tain

ty

Upp

er

Unc

erta

inty

U

ncer

tain

ty

Ref

eren

ce

0111 RECIP Caterpillar G398 SI-TA-SC - HCR 32 - Catalyst NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

0111 RECIP Caterpillar G398 SI-TA-SC - HCR 32 - Catalyst NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

0111 RECIP Caterpillar G398 SI-TA-SC - HCR 32 - Catalyst NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

0111 RECIP Caterpillar G398 SI-TA-SC - HCR 32 - Catalyst NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0006 VOC 12.7 0.27 0.27 1

0111 RECIP Caterpillar G398 SI-TA-SC - HCR 32 - Catalyst NGAS Manufacturer 2003 CEL0007 THC 172 0.51 0.51 1

0112 RECIP Caterpillar G398 SI-TA-SC - HCR 32 - Standard NGAS

CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0112 RECIP Caterpillar G398 SI-TA-SC - HCR 32 - Standard NGAS Manufacturer 2003 630-08-0 CO 119 0.34 0.34 1

0112 RECIP Caterpillar G398 SI-TA-SC - HCR 32 - Standard NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 74-82-8 CH4 99 0.59 0.59 1

0112 RECIP Caterpillar G398 SI-TA-SC - HCR 32 - Standard NGAS Manufacturer 2003 CEL0002 NOx 1650 0.09 0.09 1

0112 RECIP Caterpillar G398 SI-TA-SC - HCR 32 - Standard NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

0112 RECIP Caterpillar G398 SI-TA-SC - HCR 32 - Standard NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

0112 RECIP Caterpillar G398 SI-TA-SC - HCR 32 - Standard NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

0112 RECIP Caterpillar G398 SI-TA-SC - HCR 32 - Standard NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0006 VOC 12.7 0.27 0.27 1

0112 RECIP Caterpillar G398 SI-TA-SC - HCR 32 - Standard NGAS Manufacturer 2003 CEL0007 THC 98 0.51 0.51 1

0113 RECIP Caterpillar G398 SI-TA-SC - HCR 32 LE NGAS

CHEMEX Labs -> Profile: 0014 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0113 RECIP Caterpillar G398 SI-TA-SC - HCR 32 LE NGAS Manufacturer 2003 630-08-0 CO 168 0.34 0.34 1

0113 RECIP Caterpillar G398 SI-TA-SC - HCR 32 LE NGAS

U.S. EPA AP-42 -> Profile: 0014 2000 74-82-8 CH4 538 0.59 0.59 1

0113 RECIP Caterpillar G398 SI-TA-SC - HCR 32 LE NGAS Manufacturer 2003 CEL0002 NOx 526 0.09 0.09 1

101

Table 3.3 Compilation of combustion emission factors for estimating GHG and CAC emissions.

Fact

or

Equ

ipm

ent

Typ

e

Identifier 1 Identifier 2 Identifier 3 Fuel Type

Factor Reference Y

ear CAS

Number Compound Emission

Factor (ng/J) L

ower

U

ncer

tain

ty

Upp

er

Unc

erta

inty

U

ncer

tain

ty

Ref

eren

ce

0113 RECIP Caterpillar G398 SI-TA-SC - HCR 32 LE NGAS

U.S. EPA AP-42 -> Profile: 0014 2000 CEL0003 TPM 0.0332 0.67 1.50 7

0113 RECIP Caterpillar G398 SI-TA-SC - HCR 32 LE NGAS

U.S. EPA AP-42 -> Profile: 0014 2000 CEL0004 PM10 0.0332 0.67 1.50 7

0113 RECIP Caterpillar G398 SI-TA-SC - HCR 32 LE NGAS

U.S. EPA AP-42 -> Profile: 0014 2000 CEL0005 PM2.5 0.0332 0.67 1.50 7

0113 RECIP Caterpillar G398 SI-TA-SC - HCR 32 LE NGAS

U.S. EPA AP-42 -> Profile: 0014 2000 CEL0006 VOC 51 0.27 0.27 1

0113 RECIP Caterpillar G398 SI-TA-SC - HCR 32 LE NGAS Manufacturer 2003 CEL0007 THC 147 0.51 0.51 1

0114 RECIP Caterpillar G398 SI-TA-SC - HCR 54 LE NGAS

CHEMEX Labs -> Profile: 0014 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0114 RECIP Caterpillar G398 SI-TA-SC - HCR 54 LE NGAS Manufacturer 2003 630-08-0 CO 152 0.34 0.34 1

0114 RECIP Caterpillar G398 SI-TA-SC - HCR 54 LE NGAS

U.S. EPA AP-42 -> Profile: 0014 2000 74-82-8 CH4 538 0.59 0.59 1

0114 RECIP Caterpillar G398 SI-TA-SC - HCR 54 LE NGAS Manufacturer 2003 CEL0002 NOx 506 0.09 0.09 1

0114 RECIP Caterpillar G398 SI-TA-SC - HCR 54 LE NGAS

U.S. EPA AP-42 -> Profile: 0014 2000 CEL0003 TPM 0.0332 0.67 1.50 7

0114 RECIP Caterpillar G398 SI-TA-SC - HCR 54 LE NGAS

U.S. EPA AP-42 -> Profile: 0014 2000 CEL0004 PM10 0.0332 0.67 1.50 7

0114 RECIP Caterpillar G398 SI-TA-SC - HCR 54 LE NGAS

U.S. EPA AP-42 -> Profile: 0014 2000 CEL0005 PM2.5 0.0332 0.67 1.50 7

0114 RECIP Caterpillar G398 SI-TA-SC - HCR 54 LE NGAS

U.S. EPA AP-42 -> Profile: 0014 2000 CEL0006 VOC 51 0.27 0.27 1

0114 RECIP Caterpillar G398 SI-TA-SC - HCR 54 LE NGAS Manufacturer 2003 CEL0007 THC 132 0.51 0.51 1

0115 RECIP Caterpillar G398 SI-TA-SC - LCR 32 NGAS

CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0115 RECIP Caterpillar G398 SI-TA-SC - LCR 32 NGAS Manufacturer 2003 630-08-0 CO 85 0.34 0.34 1

0115 RECIP Caterpillar G398 SI-TA-SC - LCR 32 NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 74-82-8 CH4 99 0.59 0.59 1

0115 RECIP Caterpillar G398 SI-TA-SC - LCR 32 NGAS Manufacturer 2003 CEL0002 NOx 1947 0.09 0.09 1

102

Table 3.3 Compilation of combustion emission factors for estimating GHG and CAC emissions.

Fact

or

Equ

ipm

ent

Typ

e

Identifier 1 Identifier 2 Identifier 3 Fuel Type

Factor Reference Y

ear CAS

Number Compound Emission

Factor (ng/J) L

ower

U

ncer

tain

ty

Upp

er

Unc

erta

inty

U

ncer

tain

ty

Ref

eren

ce

0115 RECIP Caterpillar G398 SI-TA-SC - LCR 32 NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

0115 RECIP Caterpillar G398 SI-TA-SC - LCR 32 NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

0115 RECIP Caterpillar G398 SI-TA-SC - LCR 32 NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

0115 RECIP Caterpillar G398 SI-TA-SC - LCR 32 NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0006 VOC 12.7 0.27 0.27 1

0115 RECIP Caterpillar G398 SI-TA-SC - LCR 32 NGAS Manufacturer 2003 CEL0007 THC 117 0.51 0.51 1

0116 RECIP Caterpillar G398 SI-TA-SC - LCR 54 - Catalyst NGAS

CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0116 RECIP Caterpillar G398 SI-TA-SC - LCR 54 - Catalyst NGAS Manufacturer 2003 630-08-0 CO 1077 0.34 0.34 1

0116 RECIP Caterpillar G398 SI-TA-SC - LCR 54 - Catalyst NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 74-82-8 CH4 99 0.59 0.59 1

0116 RECIP Caterpillar G398 SI-TA-SC - LCR 54 - Catalyst NGAS Manufacturer 2003 CEL0002 NOx 986 0.09 0.09 1

0116 RECIP Caterpillar G398 SI-TA-SC - LCR 54 - Catalyst NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

0116 RECIP Caterpillar G398 SI-TA-SC - LCR 54 - Catalyst NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

0116 RECIP Caterpillar G398 SI-TA-SC - LCR 54 - Catalyst NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

0116 RECIP Caterpillar G398 SI-TA-SC - LCR 54 - Catalyst NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0006 VOC 12.7 0.27 0.27 1

0116 RECIP Caterpillar G398 SI-TA-SC - LCR 54 - Catalyst NGAS Manufacturer 2003 CEL0007 THC 81 0.51 0.51 1

0117 RECIP Caterpillar G398 SI-TA-SC - LCR 54 - Standard NGAS

CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0117 RECIP Caterpillar G398 SI-TA-SC - LCR 54 - Standard NGAS Manufacturer 2003 630-08-0 CO 84 0.34 0.34 1

0117 RECIP Caterpillar G398 SI-TA-SC - LCR 54 - Standard NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 74-82-8 CH4 99 0.59 0.59 1

0117 RECIP Caterpillar G398 SI-TA-SC - LCR 54 - Standard NGAS Manufacturer 2003 CEL0002 NOx 2156 0.09 0.09 1

103

Table 3.3 Compilation of combustion emission factors for estimating GHG and CAC emissions.

Fact

or

Equ

ipm

ent

Typ

e

Identifier 1 Identifier 2 Identifier 3 Fuel Type

Factor Reference Y

ear CAS

Number Compound Emission

Factor (ng/J) L

ower

U

ncer

tain

ty

Upp

er

Unc

erta

inty

U

ncer

tain

ty

Ref

eren

ce

0117 RECIP Caterpillar G398 SI-TA-SC - LCR 54 - Standard NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

0117 RECIP Caterpillar G398 SI-TA-SC - LCR 54 - Standard NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

0117 RECIP Caterpillar G398 SI-TA-SC - LCR 54 - Standard NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

0117 RECIP Caterpillar G398 SI-TA-SC - LCR 54 - Standard NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0006 VOC 12.7 0.27 0.27 1

0117 RECIP Caterpillar G398 SI-TA-SC - LCR 54 - Standard NGAS Manufacturer 2003 CEL0007 THC 84 0.51 0.51 1

0118 RECIP Caterpillar G398 SI-TAA - HCR NGAS

CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0118 RECIP Caterpillar G398 SI-TAA - HCR NGAS Manufacturer 2003 630-08-0 CO 122 0.34 0.34 1

0118 RECIP Caterpillar G398 SI-TAA - HCR NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 74-82-8 CH4 99 0.59 0.59 1

0118 RECIP Caterpillar G398 SI-TAA - HCR NGAS Manufacturer 2003 CEL0002 NOx 1689 0.09 0.09 1

0118 RECIP Caterpillar G398 SI-TAA - HCR NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

0118 RECIP Caterpillar G398 SI-TAA - HCR NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

0118 RECIP Caterpillar G398 SI-TAA - HCR NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

0118 RECIP Caterpillar G398 SI-TAA - HCR NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0006 VOC 12.7 0.27 0.27 1

0118 RECIP Caterpillar G398 SI-TAA - HCR NGAS Manufacturer 2003 CEL0007 THC 100 0.51 0.51 1

0119 RECIP Caterpillar G398 SI-TAA - HCR LE NGAS

CHEMEX Labs -> Profile: 0014 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0119 RECIP Caterpillar G398 SI-TAA - HCR LE NGAS Manufacturer 2003 630-08-0 CO 168 0.34 0.34 1

0119 RECIP Caterpillar G398 SI-TAA - HCR LE NGAS

U.S. EPA AP-42 -> Profile: 0014 2000 74-82-8 CH4 538 0.59 0.59 1

0119 RECIP Caterpillar G398 SI-TAA - HCR LE NGAS Manufacturer 2003 CEL0002 NOx 526 0.09 0.09 1

104

Table 3.3 Compilation of combustion emission factors for estimating GHG and CAC emissions.

Fact

or

Equ

ipm

ent

Typ

e

Identifier 1 Identifier 2 Identifier 3 Fuel Type

Factor Reference Y

ear CAS

Number Compound Emission

Factor (ng/J) L

ower

U

ncer

tain

ty

Upp

er

Unc

erta

inty

U

ncer

tain

ty

Ref

eren

ce

0119 RECIP Caterpillar G398 SI-TAA - HCR LE NGAS

U.S. EPA AP-42 -> Profile: 0014 2000 CEL0003 TPM 0.0332 0.67 1.50 7

0119 RECIP Caterpillar G398 SI-TAA - HCR LE NGAS

U.S. EPA AP-42 -> Profile: 0014 2000 CEL0004 PM10 0.0332 0.67 1.50 7

0119 RECIP Caterpillar G398 SI-TAA - HCR LE NGAS

U.S. EPA AP-42 -> Profile: 0014 2000 CEL0005 PM2.5 0.0332 0.67 1.50 7

0119 RECIP Caterpillar G398 SI-TAA - HCR LE NGAS

U.S. EPA AP-42 -> Profile: 0014 2000 CEL0006 VOC 51 0.27 0.27 1

0119 RECIP Caterpillar G398 SI-TAA - HCR LE NGAS Manufacturer 2003 CEL0007 THC 147 0.51 0.51 1

0120 RECIP Caterpillar G398 SI-TAA - LCR NGAS

CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0120 RECIP Caterpillar G398 SI-TAA - LCR NGAS Manufacturer 2003 630-08-0 CO 85 0.34 0.34 1

0120 RECIP Caterpillar G398 SI-TAA - LCR NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 74-82-8 CH4 99 0.59 0.59 1

0120 RECIP Caterpillar G398 SI-TAA - LCR NGAS Manufacturer 2003 CEL0002 NOx 1947 0.09 0.09 1

0120 RECIP Caterpillar G398 SI-TAA - LCR NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

0120 RECIP Caterpillar G398 SI-TAA - LCR NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

0120 RECIP Caterpillar G398 SI-TAA - LCR NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

0120 RECIP Caterpillar G398 SI-TAA - LCR NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0006 VOC 12.7 0.27 0.27 1

0120 RECIP Caterpillar G398 SI-TAA - LCR NGAS Manufacturer 2003 CEL0007 THC 117 0.51 0.51 1

0121 RECIP Caterpillar G399 SI-NA - HCR NGAS

CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0121 RECIP Caterpillar G399 SI-NA - HCR NGAS Manufacturer 2003 630-08-0 CO 1504 0.34 0.34 1

0121 RECIP Caterpillar G399 SI-NA - HCR NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 74-82-8 CH4 99 0.59 0.59 1

0121 RECIP Caterpillar G399 SI-NA - HCR NGAS Manufacturer 2003 CEL0002 NOx 1374 0.09 0.09 1

105

Table 3.3 Compilation of combustion emission factors for estimating GHG and CAC emissions.

Fact

or

Equ

ipm

ent

Typ

e

Identifier 1 Identifier 2 Identifier 3 Fuel Type

Factor Reference Y

ear CAS

Number Compound Emission

Factor (ng/J) L

ower

U

ncer

tain

ty

Upp

er

Unc

erta

inty

U

ncer

tain

ty

Ref

eren

ce

0121 RECIP Caterpillar G399 SI-NA - HCR NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

0121 RECIP Caterpillar G399 SI-NA - HCR NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

0121 RECIP Caterpillar G399 SI-NA - HCR NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

0121 RECIP Caterpillar G399 SI-NA - HCR NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0006 VOC 12.7 0.27 0.27 1

0121 RECIP Caterpillar G399 SI-NA - HCR NGAS Manufacturer 2003 CEL0007 THC 195 0.51 0.51 1

0122 RECIP Caterpillar G399 SI-NA - LCR NGAS CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0122 RECIP Caterpillar G399 SI-NA - LCR NGAS Manufacturer 2003 630-08-0 CO 1135 0.34 0.34 1

0122 RECIP Caterpillar G399 SI-NA - LCR NGAS U.S. EPA AP-42 -> Profile: 0016 2000 74-82-8 CH4 99 0.59 0.59 1

0122 RECIP Caterpillar G399 SI-NA - LCR NGAS Manufacturer 2003 CEL0002 NOx 1106 0.09 0.09 1

0122 RECIP Caterpillar G399 SI-NA - LCR NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

0122 RECIP Caterpillar G399 SI-NA - LCR NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

0122 RECIP Caterpillar G399 SI-NA - LCR NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

0122 RECIP Caterpillar G399 SI-NA - LCR NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0006 VOC 12.7 0.27 0.27 1

0122 RECIP Caterpillar G399 SI-NA - LCR NGAS Manufacturer 2003 CEL0007 THC 79 0.51 0.51 1

0123 RECIP Caterpillar G399 SI-TA-SC - HCR 32 - Catalyst NGAS

CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0123 RECIP Caterpillar G399 SI-TA-SC - HCR 32 - Catalyst NGAS Manufacturer 2003 630-08-0 CO 1190 0.34 0.34 1

0123 RECIP Caterpillar G399 SI-TA-SC - HCR 32 - Catalyst NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 74-82-8 CH4 99 0.59 0.59 1

0123 RECIP Caterpillar G399 SI-TA-SC - HCR 32 - Catalyst NGAS Manufacturer 2003 CEL0002 NOx 1146 0.09 0.09 1

0123 RECIP Caterpillar G399 SI-TA-SC - HCR 32 - Catalyst NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

0123 RECIP Caterpillar G399 SI-TA-SC - NGAS U.S. EPA AP-42 - 2000 CEL0004 PM10 4.09 0.50 2.00 8

106

Table 3.3 Compilation of combustion emission factors for estimating GHG and CAC emissions.

Fact

or

Equ

ipm

ent

Typ

e

Identifier 1 Identifier 2 Identifier 3 Fuel Type

Factor Reference Y

ear CAS

Number Compound Emission

Factor (ng/J) L

ower

U

ncer

tain

ty

Upp

er

Unc

erta

inty

U

ncer

tain

ty

Ref

eren

ce

HCR 32 - Catalyst > Profile: 0016

0123 RECIP Caterpillar G399 SI-TA-SC - HCR 32 - Catalyst NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

0123 RECIP Caterpillar G399 SI-TA-SC - HCR 32 - Catalyst NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0006 VOC 12.7 0.27 0.27 1

0123 RECIP Caterpillar G399 SI-TA-SC - HCR 32 - Catalyst NGAS Manufacturer 2003 CEL0007 THC 110 0.51 0.51 1

0124 RECIP Caterpillar G399 SI-TA-SC - HCR 32 - Standard NGAS

CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0124 RECIP Caterpillar G399 SI-TA-SC - HCR 32 - Standard NGAS Manufacturer 2003 630-08-0 CO 167 0.34 0.34 1

0124 RECIP Caterpillar G399 SI-TA-SC - HCR 32 - Standard NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 74-82-8 CH4 99 0.59 0.59 1

0124 RECIP Caterpillar G399 SI-TA-SC - HCR 32 - Standard NGAS Manufacturer 2003 CEL0002 NOx 1396 0.09 0.09 1

0124 RECIP Caterpillar G399 SI-TA-SC - HCR 32 - Standard NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

0124 RECIP Caterpillar G399 SI-TA-SC - HCR 32 - Standard NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

0124 RECIP Caterpillar G399 SI-TA-SC - HCR 32 - Standard NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

0124 RECIP Caterpillar G399 SI-TA-SC - HCR 32 - Standard NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0006 VOC 12.7 0.27 0.27 1

0124 RECIP Caterpillar G399 SI-TA-SC - HCR 32 - Standard NGAS Manufacturer 2003 CEL0007 THC 100 0.51 0.51 1

0125 RECIP Caterpillar G399 SI-TA-SC - HCR 32 LE NGAS

CHEMEX Labs -> Profile: 0014 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0125 RECIP Caterpillar G399 SI-TA-SC - HCR 32 LE NGAS Manufacturer 2003 630-08-0 CO 157 0.34 0.34 1

0125 RECIP Caterpillar G399 SI-TA-SC - HCR 32 LE NGAS

U.S. EPA AP-42 -> Profile: 0014 2000 74-82-8 CH4 538 0.59 0.59 1

0125 RECIP Caterpillar G399 SI-TA-SC - HCR 32 LE NGAS Manufacturer 2003 CEL0002 NOx 524 0.09 0.09 1

0125 RECIP Caterpillar G399 SI-TA-SC - HCR 32 LE NGAS

U.S. EPA AP-42 -> Profile: 0014 2000 CEL0003 TPM 0.0332 0.67 1.50 7

0125 RECIP Caterpillar G399 SI-TA-SC - NGAS U.S. EPA AP-42 - 2000 CEL0004 PM10 0.0332 0.67 1.50 7

107

Table 3.3 Compilation of combustion emission factors for estimating GHG and CAC emissions.

Fact

or

Equ

ipm

ent

Typ

e

Identifier 1 Identifier 2 Identifier 3 Fuel Type

Factor Reference Y

ear CAS

Number Compound Emission

Factor (ng/J) L

ower

U

ncer

tain

ty

Upp

er

Unc

erta

inty

U

ncer

tain

ty

Ref

eren

ce

HCR 32 LE > Profile: 0014

0125 RECIP Caterpillar G399 SI-TA-SC - HCR 32 LE NGAS

U.S. EPA AP-42 -> Profile: 0014 2000 CEL0005 PM2.5 0.0332 0.67 1.50 7

0125 RECIP Caterpillar G399 SI-TA-SC - HCR 32 LE NGAS

U.S. EPA AP-42 -> Profile: 0014 2000 CEL0006 VOC 51 0.27 0.27 1

0125 RECIP Caterpillar G399 SI-TA-SC - HCR 32 LE NGAS Manufacturer 2003 CEL0007 THC 115 0.51 0.51 1

0126 RECIP Caterpillar G399 SI-TA-SC - LCR 32 NGAS

CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0126 RECIP Caterpillar G399 SI-TA-SC - LCR 32 NGAS Manufacturer 2003 630-08-0 CO 85 0.34 0.34 1

0126 RECIP Caterpillar G399 SI-TA-SC - LCR 32 NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 74-82-8 CH4 99 0.59 0.59 1

0126 RECIP Caterpillar G399 SI-TA-SC - LCR 32 NGAS Manufacturer 2003 CEL0002 NOx 1967 0.09 0.09 1

0126 RECIP Caterpillar G399 SI-TA-SC - LCR 32 NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

0126 RECIP Caterpillar G399 SI-TA-SC - LCR 32 NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

0126 RECIP Caterpillar G399 SI-TA-SC - LCR 32 NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

0126 RECIP Caterpillar G399 SI-TA-SC - LCR 32 NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0006 VOC 12.7 0.27 0.27 1

0126 RECIP Caterpillar G399 SI-TA-SC - LCR 32 NGAS Manufacturer 2003 CEL0007 THC 117 0.51 0.51 1

0127 RECIP Caterpillar G399 SI-TA-SC - LCR 54 - Catalyst NGAS

CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0127 RECIP Caterpillar G399 SI-TA-SC - LCR 54 - Catalyst NGAS Manufacturer 2003 630-08-0 CO 845 0.34 0.34 1

0127 RECIP Caterpillar G399 SI-TA-SC - LCR 54 - Catalyst NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 74-82-8 CH4 99 0.59 0.59 1

0127 RECIP Caterpillar G399 SI-TA-SC - LCR 54 - Catalyst NGAS Manufacturer 2003 CEL0002 NOx 1002 0.09 0.09 1

0127 RECIP Caterpillar G399 SI-TA-SC - LCR 54 - Catalyst NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

0127 RECIP Caterpillar G399 SI-TA-SC - NGAS U.S. EPA AP-42 - 2000 CEL0004 PM10 4.09 0.50 2.00 8

108

Table 3.3 Compilation of combustion emission factors for estimating GHG and CAC emissions.

Fact

or

Equ

ipm

ent

Typ

e

Identifier 1 Identifier 2 Identifier 3 Fuel Type

Factor Reference Y

ear CAS

Number Compound Emission

Factor (ng/J) L

ower

U

ncer

tain

ty

Upp

er

Unc

erta

inty

U

ncer

tain

ty

Ref

eren

ce

LCR 54 - Catalyst > Profile: 0016

0127 RECIP Caterpillar G399 SI-TA-SC - LCR 54 - Catalyst NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

0127 RECIP Caterpillar G399 SI-TA-SC - LCR 54 - Catalyst NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0006 VOC 12.7 0.27 0.27 1

0127 RECIP Caterpillar G399 SI-TA-SC - LCR 54 - Catalyst NGAS Manufacturer 2003 CEL0007 THC 83 0.51 0.51 1

0128 RECIP Caterpillar G399 SI-TA-SC - LCR 54 - Standard NGAS

CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0128 RECIP Caterpillar G399 SI-TA-SC - LCR 54 - Standard NGAS Manufacturer 2003 630-08-0 CO 86 0.34 0.34 1

0128 RECIP Caterpillar G399 SI-TA-SC - LCR 54 - Standard NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 74-82-8 CH4 99 0.59 0.59 1

0128 RECIP Caterpillar G399 SI-TA-SC - LCR 54 - Standard NGAS Manufacturer 2003 CEL0002 NOx 2222 0.09 0.09 1

0128 RECIP Caterpillar G399 SI-TA-SC - LCR 54 - Standard NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

0128 RECIP Caterpillar G399 SI-TA-SC - LCR 54 - Standard NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

0128 RECIP Caterpillar G399 SI-TA-SC - LCR 54 - Standard NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

0128 RECIP Caterpillar G399 SI-TA-SC - LCR 54 - Standard NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0006 VOC 12.7 0.27 0.27 1

0128 RECIP Caterpillar G399 SI-TA-SC - LCR 54 - Standard NGAS Manufacturer 2003 CEL0007 THC 86 0.51 0.51 1

0129 RECIP Caterpillar G399 SI-TA-SC - LCR 54 LE NGAS

CHEMEX Labs -> Profile: 0014 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0129 RECIP Caterpillar G399 SI-TA-SC - LCR 54 LE NGAS Manufacturer 2003 630-08-0 CO 154 0.34 0.34 1

0129 RECIP Caterpillar G399 SI-TA-SC - LCR 54 LE NGAS

U.S. EPA AP-42 -> Profile: 0014 2000 74-82-8 CH4 538 0.59 0.59 1

0129 RECIP Caterpillar G399 SI-TA-SC - LCR 54 LE NGAS Manufacturer 2003 CEL0002 NOx 515 0.09 0.09 1

0129 RECIP Caterpillar G399 SI-TA-SC - LCR 54 LE NGAS

U.S. EPA AP-42 -> Profile: 0014 2000 CEL0003 TPM 0.0332 0.67 1.50 7

0129 RECIP Caterpillar G399 SI-TA-SC - NGAS U.S. EPA AP-42 - 2000 CEL0004 PM10 0.0332 0.67 1.50 7

109

Table 3.3 Compilation of combustion emission factors for estimating GHG and CAC emissions.

Fact

or

Equ

ipm

ent

Typ

e

Identifier 1 Identifier 2 Identifier 3 Fuel Type

Factor Reference Y

ear CAS

Number Compound Emission

Factor (ng/J) L

ower

U

ncer

tain

ty

Upp

er

Unc

erta

inty

U

ncer

tain

ty

Ref

eren

ce

LCR 54 LE > Profile: 0014

0129 RECIP Caterpillar G399 SI-TA-SC - LCR 54 LE NGAS

U.S. EPA AP-42 -> Profile: 0014 2000 CEL0005 PM2.5 0.0332 0.67 1.50 7

0129 RECIP Caterpillar G399 SI-TA-SC - LCR 54 LE NGAS

U.S. EPA AP-42 -> Profile: 0014 2000 CEL0006 VOC 51 0.27 0.27 1

0129 RECIP Caterpillar G399 SI-TA-SC - LCR 54 LE NGAS Manufacturer 2003 CEL0007 THC 134 0.51 0.51 1

0130 RECIP Caterpillar G399 SI-TAA - HCR NGAS

CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0130 RECIP Caterpillar G399 SI-TAA - HCR NGAS Manufacturer 2003 630-08-0 CO 167 0.34 0.34 1

0130 RECIP Caterpillar G399 SI-TAA - HCR NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 74-82-8 CH4 99 0.59 0.59 1

0130 RECIP Caterpillar G399 SI-TAA - HCR NGAS Manufacturer 2003 CEL0002 NOx 1389 0.09 0.09 1

0130 RECIP Caterpillar G399 SI-TAA - HCR NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

0130 RECIP Caterpillar G399 SI-TAA - HCR NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

0130 RECIP Caterpillar G399 SI-TAA - HCR NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

0130 RECIP Caterpillar G399 SI-TAA - HCR NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0006 VOC 12.7 0.27 0.27 1

0130 RECIP Caterpillar G399 SI-TAA - HCR NGAS Manufacturer 2003 CEL0007 THC 100 0.51 0.51 1

0131 RECIP Caterpillar G399 SI-TAA - HCR LE NGAS

CHEMEX Labs -> Profile: 0014 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0131 RECIP Caterpillar G399 SI-TAA - HCR LE NGAS Manufacturer 2003 630-08-0 CO 157 0.34 0.34 1

0131 RECIP Caterpillar G399 SI-TAA - HCR LE NGAS

U.S. EPA AP-42 -> Profile: 0014 2000 74-82-8 CH4 538 0.59 0.59 1

0131 RECIP Caterpillar G399 SI-TAA - HCR LE NGAS Manufacturer 2003 CEL0002 NOx 524 0.09 0.09 1

0131 RECIP Caterpillar G399 SI-TAA - HCR LE NGAS

U.S. EPA AP-42 -> Profile: 0014 2000 CEL0003 TPM 0.0332 0.67 1.50 7

0131 RECIP Caterpillar G399 SI-TAA - NGAS U.S. EPA AP-42 - 2000 CEL0004 PM10 0.0332 0.67 1.50 7

110

Table 3.3 Compilation of combustion emission factors for estimating GHG and CAC emissions.

Fact

or

Equ

ipm

ent

Typ

e

Identifier 1 Identifier 2 Identifier 3 Fuel Type

Factor Reference Y

ear CAS

Number Compound Emission

Factor (ng/J) L

ower

U

ncer

tain

ty

Upp

er

Unc

erta

inty

U

ncer

tain

ty

Ref

eren

ce

HCR LE > Profile: 0014

0131 RECIP Caterpillar G399 SI-TAA - HCR LE NGAS

U.S. EPA AP-42 -> Profile: 0014 2000 CEL0005 PM2.5 0.0332 0.67 1.50 7

0131 RECIP Caterpillar G399 SI-TAA - HCR LE NGAS

U.S. EPA AP-42 -> Profile: 0014 2000 CEL0006 VOC 51 0.27 0.27 1

0131 RECIP Caterpillar G399 SI-TAA - HCR LE NGAS Manufacturer 2003 CEL0007 THC 115 0.51 0.51 1

0132 RECIP Caterpillar G399 SI-TAA - LCR NGAS

CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0132 RECIP Caterpillar G399 SI-TAA - LCR NGAS Manufacturer 2003 630-08-0 CO 85 0.34 0.34 1

0132 RECIP Caterpillar G399 SI-TAA - LCR NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 74-82-8 CH4 99 0.59 0.59 1

0132 RECIP Caterpillar G399 SI-TAA - LCR NGAS Manufacturer 2003 CEL0002 NOx 1967 0.09 0.09 1

0132 RECIP Caterpillar G399 SI-TAA - LCR NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

0132 RECIP Caterpillar G399 SI-TAA - LCR NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

0132 RECIP Caterpillar G399 SI-TAA - LCR NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

0132 RECIP Caterpillar G399 SI-TAA - LCR NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0006 VOC 12.7 0.27 0.27 1

0132 RECIP Caterpillar G399 SI-TAA - LCR NGAS Manufacturer 2003 CEL0007 THC 117 0.51 0.51 1

0133 RECIP Cooper Energy Services - Ajax DPC-115LE NGAS

CHEMEX Labs -> Profile: 0012 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0133 RECIP Cooper Energy Services - Ajax DPC-115LE NGAS Manufacturer 2003 630-08-0 CO 208 0.34 0.34 1

0133 RECIP Cooper Energy Services - Ajax DPC-115LE NGAS

U.S. EPA AP-42 -> Profile: 0012 2000 74-82-8 CH4 624 0.59 0.59 1

0133 RECIP Cooper Energy Services - Ajax DPC-115LE NGAS Manufacturer 2003 CEL0002 NOx 208 0.09 0.09 1

0133 RECIP Cooper Energy Services - Ajax DPC-115LE NGAS

U.S. EPA AP-42 -> Profile: 0012 2000 CEL0003 TPM 16.5 1.00 1.00 6

0133 RECIP Cooper Energy DPC-115LE NGAS U.S. EPA AP-42 - 2000 CEL0004 PM10 16.5 1.00 1.00 6

111

Table 3.3 Compilation of combustion emission factors for estimating GHG and CAC emissions.

Fact

or

Equ

ipm

ent

Typ

e

Identifier 1 Identifier 2 Identifier 3 Fuel Type

Factor Reference Y

ear CAS

Number Compound Emission

Factor (ng/J) L

ower

U

ncer

tain

ty

Upp

er

Unc

erta

inty

U

ncer

tain

ty

Ref

eren

ce

Services - Ajax > Profile: 0012

0133 RECIP Cooper Energy Services - Ajax DPC-115LE NGAS

U.S. EPA AP-42 -> Profile: 0012 2000 CEL0005 PM2.5 16.5 1.00 1.00 6

0133 RECIP Cooper Energy Services - Ajax DPC-115LE NGAS Manufacturer 2003 CEL0006 VOC 730 0.27 0.27 1

0133 RECIP Cooper Energy Services - Ajax DPC-115LE NGAS CH4 + VOC 2003 CEL0007 THC 1354 0.31 0.31 1

0134 RECIP Cooper Energy Services - Ajax DPC-140 NGAS

CHEMEX Labs -> Profile: 0012 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0134 RECIP Cooper Energy Services - Ajax DPC-140 NGAS Manufacturer 2003 630-08-0 CO 234 0.34 0.34 1

0134 RECIP Cooper Energy Services - Ajax DPC-140 NGAS

U.S. EPA AP-42 -> Profile: 0012 2000 74-82-8 CH4 624 0.59 0.59 1

0134 RECIP Cooper Energy Services - Ajax DPC-140 NGAS Manufacturer 2003 CEL0002 NOx 469 0.09 0.09 1

0134 RECIP Cooper Energy Services - Ajax DPC-140 NGAS

U.S. EPA AP-42 -> Profile: 0012 2000 CEL0003 TPM 16.5 1.00 1.00 6

0134 RECIP Cooper Energy Services - Ajax DPC-140 NGAS

U.S. EPA AP-42 -> Profile: 0012 2000 CEL0004 PM10 16.5 1.00 1.00 6

0134 RECIP Cooper Energy Services - Ajax DPC-140 NGAS

U.S. EPA AP-42 -> Profile: 0012 2000 CEL0005 PM2.5 16.5 1.00 1.00 6

0134 RECIP Cooper Energy Services - Ajax DPC-140 NGAS Manufacturer 2003 CEL0006 VOC 117 0.27 0.27 1

0134 RECIP Cooper Energy Services - Ajax DPC-140 NGAS CH4 + VOC 2003 CEL0007 THC 741 0.50 0.50 1

0135 RECIP Cooper Energy Services - Ajax DPC-140LE NGAS

CHEMEX Labs -> Profile: 0012 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0135 RECIP Cooper Energy Services - Ajax DPC-140LE NGAS Manufacturer 2003 630-08-0 CO 141 0.34 0.34 1

0135 RECIP Cooper Energy Services - Ajax DPC-140LE NGAS

U.S. EPA AP-42 -> Profile: 0012 2000 74-82-8 CH4 624 0.59 0.59 1

0135 RECIP Cooper Energy Services - Ajax DPC-140LE NGAS Manufacturer 2003 CEL0002 NOx 216 0.09 0.09 1

0135 RECIP Cooper Energy Services - Ajax DPC-140LE NGAS

U.S. EPA AP-42 -> Profile: 0012 2000 CEL0003 TPM 16.5 1.00 1.00 6

0135 RECIP Cooper Energy DPC-140LE NGAS U.S. EPA AP-42 - 2000 CEL0004 PM10 16.5 1.00 1.00 6

112

Table 3.3 Compilation of combustion emission factors for estimating GHG and CAC emissions.

Fact

or

Equ

ipm

ent

Typ

e

Identifier 1 Identifier 2 Identifier 3 Fuel Type

Factor Reference Y

ear CAS

Number Compound Emission

Factor (ng/J) L

ower

U

ncer

tain

ty

Upp

er

Unc

erta

inty

U

ncer

tain

ty

Ref

eren

ce

Services - Ajax > Profile: 0012

0135 RECIP Cooper Energy Services - Ajax DPC-140LE NGAS

U.S. EPA AP-42 -> Profile: 0012 2000 CEL0005 PM2.5 16.5 1.00 1.00 6

0135 RECIP Cooper Energy Services - Ajax DPC-140LE NGAS Manufacturer 2003 CEL0006 VOC 541 0.27 0.27 1

0135 RECIP Cooper Energy Services - Ajax DPC-140LE NGAS CH4 + VOC 2003 CEL0007 THC 1165 0.34 0.34 1

0136 RECIP Cooper Energy Services - Ajax DPC-180 NGAS

CHEMEX Labs -> Profile: 0012 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0136 RECIP Cooper Energy Services - Ajax DPC-180 NGAS Manufacturer 2003 630-08-0 CO 107 0.34 0.34 1

0136 RECIP Cooper Energy Services - Ajax DPC-180 NGAS

U.S. EPA AP-42 -> Profile: 0012 2000 74-82-8 CH4 624 0.59 0.59 1

0136 RECIP Cooper Energy Services - Ajax DPC-180 NGAS Manufacturer 2003 CEL0002 NOx 536 0.09 0.09 1

0136 RECIP Cooper Energy Services - Ajax DPC-180 NGAS

U.S. EPA AP-42 -> Profile: 0012 2000 CEL0003 TPM 16.5 1.00 1.00 6

0136 RECIP Cooper Energy Services - Ajax DPC-180 NGAS

U.S. EPA AP-42 -> Profile: 0012 2000 CEL0004 PM10 16.5 1.00 1.00 6

0136 RECIP Cooper Energy Services - Ajax DPC-180 NGAS

U.S. EPA AP-42 -> Profile: 0012 2000 CEL0005 PM2.5 16.5 1.00 1.00 6

0136 RECIP Cooper Energy Services - Ajax DPC-180 NGAS Manufacturer 2003 CEL0006 VOC 214 0.27 0.27 1

0136 RECIP Cooper Energy Services - Ajax DPC-180 NGAS CH4 + VOC 2003 CEL0007 THC 838 0.44 0.44 1

0137 RECIP Cooper Energy Services - Ajax DPC-2201LE NGAS

CHEMEX Labs -> Profile: 0012 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0137 RECIP Cooper Energy Services - Ajax DPC-2201LE NGAS Manufacturer 2003 630-08-0 CO 171 0.34 0.34 1

0137 RECIP Cooper Energy Services - Ajax DPC-2201LE NGAS Manufacturer 2003 74-82-8 CH4 534 0.59 0.59 1

0137 RECIP Cooper Energy Services - Ajax DPC-2201LE NGAS Manufacturer 2003 CEL0002 NOx 577 0.09 0.09 1

0137 RECIP Cooper Energy Services - Ajax DPC-2201LE NGAS

U.S. EPA AP-42 -> Profile: 0012 2000 CEL0003 TPM 16.5 1.00 1.00 6

0137 RECIP Cooper Energy DPC-2201LE NGAS U.S. EPA AP-42 - 2000 CEL0004 PM10 16.5 1.00 1.00 6

113

Table 3.3 Compilation of combustion emission factors for estimating GHG and CAC emissions.

Fact

or

Equ

ipm

ent

Typ

e

Identifier 1 Identifier 2 Identifier 3 Fuel Type

Factor Reference Y

ear CAS

Number Compound Emission

Factor (ng/J) L

ower

U

ncer

tain

ty

Upp

er

Unc

erta

inty

U

ncer

tain

ty

Ref

eren

ce

Services - Ajax > Profile: 0012

0137 RECIP Cooper Energy Services - Ajax DPC-2201LE NGAS

U.S. EPA AP-42 -> Profile: 0012 2000 CEL0005 PM2.5 16.5 1.00 1.00 6

0137 RECIP Cooper Energy Services - Ajax DPC-2201LE NGAS Manufacturer 2003 CEL0006 VOC 107 0.27 0.27 1

0137 RECIP Cooper Energy Services - Ajax DPC-2201LE NGAS Manufacturer 2003 CEL0007 THC 641 0.51 0.51 1

0138 RECIP Cooper Energy Services - Ajax DPC-230 NGAS

CHEMEX Labs -> Profile: 0012 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0138 RECIP Cooper Energy Services - Ajax DPC-230 NGAS Manufacturer 2003 630-08-0 CO 244 0.34 0.34 1

0138 RECIP Cooper Energy Services - Ajax DPC-230 NGAS

U.S. EPA AP-42 -> Profile: 0012 2000 74-82-8 CH4 624 0.59 0.59 1

0138 RECIP Cooper Energy Services - Ajax DPC-230 NGAS Manufacturer 2003 CEL0002 NOx 342 0.09 0.09 1

0138 RECIP Cooper Energy Services - Ajax DPC-230 NGAS

U.S. EPA AP-42 -> Profile: 0012 2000 CEL0003 TPM 16.5 1.00 1.00 6

0138 RECIP Cooper Energy Services - Ajax DPC-230 NGAS

U.S. EPA AP-42 -> Profile: 0012 2000 CEL0004 PM10 16.5 1.00 1.00 6

0138 RECIP Cooper Energy Services - Ajax DPC-230 NGAS

U.S. EPA AP-42 -> Profile: 0012 2000 CEL0005 PM2.5 16.5 1.00 1.00 6

0138 RECIP Cooper Energy Services - Ajax DPC-230 NGAS Manufacturer 2003 CEL0006 VOC 975 0.27 0.27 1

0138 RECIP Cooper Energy Services - Ajax DPC-230 NGAS CH4 + VOC 2003 CEL0007 THC 1599 0.28 0.28 1

0139 RECIP Cooper Energy Services - Ajax DPC-230LE NGAS

CHEMEX Labs -> Profile: 0012 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0139 RECIP Cooper Energy Services - Ajax DPC-230LE NGAS Manufacturer 2003 630-08-0 CO 208 0.34 0.34 1

0139 RECIP Cooper Energy Services - Ajax DPC-230LE NGAS

U.S. EPA AP-42 -> Profile: 0012 2000 74-82-8 CH4 624 0.59 0.59 1

0139 RECIP Cooper Energy Services - Ajax DPC-230LE NGAS Manufacturer 2003 CEL0002 NOx 208 0.09 0.09 1

0139 RECIP Cooper Energy Services - Ajax DPC-230LE NGAS

U.S. EPA AP-42 -> Profile: 0012 2000 CEL0003 TPM 16.5 1.00 1.00 6

0139 RECIP Cooper Energy DPC-230LE NGAS U.S. EPA AP-42 - 2000 CEL0004 PM10 16.5 1.00 1.00 6

114

Table 3.3 Compilation of combustion emission factors for estimating GHG and CAC emissions.

Fact

or

Equ

ipm

ent

Typ

e

Identifier 1 Identifier 2 Identifier 3 Fuel Type

Factor Reference Y

ear CAS

Number Compound Emission

Factor (ng/J) L

ower

U

ncer

tain

ty

Upp

er

Unc

erta

inty

U

ncer

tain

ty

Ref

eren

ce

Services - Ajax > Profile: 0012

0139 RECIP Cooper Energy Services - Ajax DPC-230LE NGAS

U.S. EPA AP-42 -> Profile: 0012 2000 CEL0005 PM2.5 16.5 1.00 1.00 6

0139 RECIP Cooper Energy Services - Ajax DPC-230LE NGAS Manufacturer 2003 CEL0006 VOC 730 0.27 0.27 1

0139 RECIP Cooper Energy Services - Ajax DPC-230LE NGAS CH4 + VOC 2003 CEL0007 THC 1354 0.31 0.31 1

0140 RECIP Cooper Energy Services - Ajax DPC-280 NGAS

CHEMEX Labs -> Profile: 0012 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0140 RECIP Cooper Energy Services - Ajax DPC-280 NGAS Manufacturer 2003 630-08-0 CO 218 0.34 0.34 1

0140 RECIP Cooper Energy Services - Ajax DPC-280 NGAS

U.S. EPA AP-42 -> Profile: 0012 2000 74-82-8 CH4 624 0.59 0.59 1

0140 RECIP Cooper Energy Services - Ajax DPC-280 NGAS Manufacturer 2003 CEL0002 NOx 524 0.09 0.09 1

0140 RECIP Cooper Energy Services - Ajax DPC-280 NGAS

U.S. EPA AP-42 -> Profile: 0012 2000 CEL0003 TPM 16.5 1.00 1.00 6

0140 RECIP Cooper Energy Services - Ajax DPC-280 NGAS

U.S. EPA AP-42 -> Profile: 0012 2000 CEL0004 PM10 16.5 1.00 1.00 6

0140 RECIP Cooper Energy Services - Ajax DPC-280 NGAS

U.S. EPA AP-42 -> Profile: 0012 2000 CEL0005 PM2.5 16.5 1.00 1.00 6

0140 RECIP Cooper Energy Services - Ajax DPC-280 NGAS Manufacturer 2003 CEL0006 VOC 568 0.27 0.27 1

0140 RECIP Cooper Energy Services - Ajax DPC-280 NGAS CH4 + VOC 2003 CEL0007 THC 1192 0.33 0.33 1

0141 RECIP Cooper Energy Services - Ajax DPC-2802LE NGAS

CHEMEX Labs -> Profile: 0012 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0141 RECIP Cooper Energy Services - Ajax DPC-2802LE NGAS Manufacturer 2003 630-08-0 CO 104 0.34 0.34 1

0141 RECIP Cooper Energy Services - Ajax DPC-2802LE NGAS Manufacturer 2003 74-82-8 CH4 563 0.59 0.59 1

0141 RECIP Cooper Energy Services - Ajax DPC-2802LE NGAS Manufacturer 2003 CEL0002 NOx 573 0.09 0.09 1

0141 RECIP Cooper Energy Services - Ajax DPC-2802LE NGAS

U.S. EPA AP-42 -> Profile: 0012 2000 CEL0003 TPM 16.5 1.00 1.00 6

0141 RECIP Cooper Energy DPC-2802LE NGAS U.S. EPA AP-42 - 2000 CEL0004 PM10 16.5 1.00 1.00 6

115

Table 3.3 Compilation of combustion emission factors for estimating GHG and CAC emissions.

Fact

or

Equ

ipm

ent

Typ

e

Identifier 1 Identifier 2 Identifier 3 Fuel Type

Factor Reference Y

ear CAS

Number Compound Emission

Factor (ng/J) L

ower

U

ncer

tain

ty

Upp

er

Unc

erta

inty

U

ncer

tain

ty

Ref

eren

ce

Services - Ajax > Profile: 0012

0141 RECIP Cooper Energy Services - Ajax DPC-2802LE NGAS

U.S. EPA AP-42 -> Profile: 0012 2000 CEL0005 PM2.5 16.5 1.00 1.00 6

0141 RECIP Cooper Energy Services - Ajax DPC-2802LE NGAS Manufacturer 2003 CEL0006 VOC 115 0.27 0.27 1

0141 RECIP Cooper Energy Services - Ajax DPC-2802LE NGAS Manufacturer 2003 CEL0007 THC 677 0.51 0.51 1

0142 RECIP Cooper Energy Services - Ajax DPC-280LE NGAS

CHEMEX Labs -> Profile: 0012 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0142 RECIP Cooper Energy Services - Ajax DPC-280LE NGAS Manufacturer 2003 630-08-0 CO 141 0.34 0.34 1

0142 RECIP Cooper Energy Services - Ajax DPC-280LE NGAS

U.S. EPA AP-42 -> Profile: 0012 2000 74-82-8 CH4 624 0.59 0.59 1

0142 RECIP Cooper Energy Services - Ajax DPC-280LE NGAS Manufacturer 2003 CEL0002 NOx 216 0.09 0.09 1

0142 RECIP Cooper Energy Services - Ajax DPC-280LE NGAS

U.S. EPA AP-42 -> Profile: 0012 2000 CEL0003 TPM 16.5 1.00 1.00 6

0142 RECIP Cooper Energy Services - Ajax DPC-280LE NGAS

U.S. EPA AP-42 -> Profile: 0012 2000 CEL0004 PM10 16.5 1.00 1.00 6

0142 RECIP Cooper Energy Services - Ajax DPC-280LE NGAS

U.S. EPA AP-42 -> Profile: 0012 2000 CEL0005 PM2.5 16.5 1.00 1.00 6

0142 RECIP Cooper Energy Services - Ajax DPC-280LE NGAS Manufacturer 2003 CEL0006 VOC 541 0.27 0.27 1

0142 RECIP Cooper Energy Services - Ajax DPC-280LE NGAS CH4 + VOC 2003 CEL0007 THC 1165 0.34 0.34 1

0143 RECIP Cooper Energy Services - Ajax DPC-360 NGAS

CHEMEX Labs -> Profile: 0012 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0143 RECIP Cooper Energy Services - Ajax DPC-360 NGAS Manufacturer 2003 630-08-0 CO 129 0.34 0.34 1

0143 RECIP Cooper Energy Services - Ajax DPC-360 NGAS

U.S. EPA AP-42 -> Profile: 0012 2000 74-82-8 CH4 624 0.59 0.59 1

0143 RECIP Cooper Energy Services - Ajax DPC-360 NGAS Manufacturer 2003 CEL0002 NOx 536 0.09 0.09 1

0143 RECIP Cooper Energy Services - Ajax DPC-360 NGAS

U.S. EPA AP-42 -> Profile: 0012 2000 CEL0003 TPM 16.5 1.00 1.00 6

0143 RECIP Cooper Energy DPC-360 NGAS U.S. EPA AP-42 - 2000 CEL0004 PM10 16.5 1.00 1.00 6

116

Table 3.3 Compilation of combustion emission factors for estimating GHG and CAC emissions.

Fact

or

Equ

ipm

ent

Typ

e

Identifier 1 Identifier 2 Identifier 3 Fuel Type

Factor Reference Y

ear CAS

Number Compound Emission

Factor (ng/J) L

ower

U

ncer

tain

ty

Upp

er

Unc

erta

inty

U

ncer

tain

ty

Ref

eren

ce

Services - Ajax > Profile: 0012

0143 RECIP Cooper Energy Services - Ajax DPC-360 NGAS

U.S. EPA AP-42 -> Profile: 0012 2000 CEL0005 PM2.5 16.5 1.00 1.00 6

0143 RECIP Cooper Energy Services - Ajax DPC-360 NGAS Manufacturer 2003 CEL0006 VOC 965 0.27 0.27 1

0143 RECIP Cooper Energy Services - Ajax DPC-360 NGAS CH4 + VOC 2003 CEL0007 THC 1589 0.28 0.28 1

0144 RECIP Waukesha 12V-AT25GL - HS Turbo NGAS

CHEMEX Labs -> Profile: 0014 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0144 RECIP Waukesha 12V-AT25GL - HS Turbo NGAS Manufacturer 2003 630-08-0 CO 266 0.34 0.34 1

0144 RECIP Waukesha 12V-AT25GL - HS Turbo NGAS

U.S. EPA AP-42 -> Profile: 0014 2000 74-82-8 CH4 538 0.59 0.59 1

0144 RECIP Waukesha 12V-AT25GL - HS Turbo NGAS Manufacturer 2003 CEL0002 NOx 177 0.09 0.09 1

0144 RECIP Waukesha 12V-AT25GL - HS Turbo NGAS

U.S. EPA AP-42 -> Profile: 0014 2000 CEL0003 TPM 0.0332 0.67 1.50 7

0144 RECIP Waukesha 12V-AT25GL - HS Turbo NGAS

U.S. EPA AP-42 -> Profile: 0014 2000 CEL0004 PM10 0.0332 0.67 1.50 7

0144 RECIP Waukesha 12V-AT25GL - HS Turbo NGAS

U.S. EPA AP-42 -> Profile: 0014 2000 CEL0005 PM2.5 0.0332 0.67 1.50 7

0144 RECIP Waukesha 12V-AT25GL - HS Turbo NGAS Manufacturer 2003 CEL0006 VOC 118 0.27 0.27 1

0144 RECIP Waukesha 12V-AT25GL - HS Turbo NGAS CH4 + VOC 2003 CEL0007 THC 656 0.48 0.48 1

0145 RECIP Waukesha 12V-AT25GL - LS Turbo NGAS

CHEMEX Labs -> Profile: 0014 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0145 RECIP Waukesha 12V-AT25GL - LS Turbo NGAS Manufacturer 2003 630-08-0 CO 266 0.34 0.34 1

0145 RECIP Waukesha 12V-AT25GL - LS Turbo NGAS

U.S. EPA AP-42 -> Profile: 0014 2000 74-82-8 CH4 538 0.59 0.59 1

0145 RECIP Waukesha 12V-AT25GL - LS Turbo NGAS Manufacturer 2003 CEL0002 NOx 177 0.09 0.09 1

0145 RECIP Waukesha 12V-AT25GL - LS Turbo NGAS

U.S. EPA AP-42 -> Profile: 0014 2000 CEL0003 TPM 0.0332 0.67 1.50 7

0145 RECIP Waukesha 12V-AT25GL - LS NGAS U.S. EPA AP-42 - 2000 CEL0004 PM10 0.0332 0.67 1.50 7

117

Table 3.3 Compilation of combustion emission factors for estimating GHG and CAC emissions.

Fact

or

Equ

ipm

ent

Typ

e

Identifier 1 Identifier 2 Identifier 3 Fuel Type

Factor Reference Y

ear CAS

Number Compound Emission

Factor (ng/J) L

ower

U

ncer

tain

ty

Upp

er

Unc

erta

inty

U

ncer

tain

ty

Ref

eren

ce

Turbo > Profile: 0014

0145 RECIP Waukesha 12V-AT25GL - LS Turbo NGAS

U.S. EPA AP-42 -> Profile: 0014 2000 CEL0005 PM2.5 0.0332 0.67 1.50 7

0145 RECIP Waukesha 12V-AT25GL - LS Turbo NGAS Manufacturer 2003 CEL0006 VOC 118 0.27 0.27 1

0145 RECIP Waukesha 12V-AT25GL - LS Turbo NGAS CH4 + VOC 2003 CEL0007 THC 656 0.48 0.48 1

0146 RECIP Waukesha 12V-AT27GL NGAS CHEMEX Labs -> Profile: 0014 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0146 RECIP Waukesha 12V-AT27GL NGAS Manufacturer 2003 630-08-0 CO 274 0.34 0.34 1

0146 RECIP Waukesha 12V-AT27GL NGAS U.S. EPA AP-42 -> Profile: 0014 2000 74-82-8 CH4 538 0.59 0.59 1

0146 RECIP Waukesha 12V-AT27GL NGAS Manufacturer 2003 CEL0002 NOx 183 0.09 0.09 1

0146 RECIP Waukesha 12V-AT27GL NGAS U.S. EPA AP-42 -> Profile: 0014 2000 CEL0003 TPM 0.0332 0.67 1.50 7

0146 RECIP Waukesha 12V-AT27GL NGAS U.S. EPA AP-42 -> Profile: 0014 2000 CEL0004 PM10 0.0332 0.67 1.50 7

0146 RECIP Waukesha 12V-AT27GL NGAS U.S. EPA AP-42 -> Profile: 0014 2000 CEL0005 PM2.5 0.0332 0.67 1.50 7

0146 RECIP Waukesha 12V-AT27GL NGAS Manufacturer 2003 CEL0006 VOC 122 0.27 0.27 1 0146 RECIP Waukesha 12V-AT27GL NGAS CH4 + VOC 2003 CEL0007 THC 660 0.48 0.48 1

0147 RECIP Waukesha 2895 GL Standard NGAS CHEMEX Labs -> Profile: 0014 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0147 RECIP Waukesha 2895 GL Standard NGAS Manufacturer 2003 630-08-0 CO 306 0.34 0.34 1 0147 RECIP Waukesha 2895 GL Standard NGAS Manufacturer 2003 74-82-8 CH4 520 0.59 0.59 1 0147 RECIP Waukesha 2895 GL Standard NGAS Manufacturer 2003 CEL0002 NOx 173 0.09 0.09 1

0147 RECIP Waukesha 2895 GL Standard NGAS U.S. EPA AP-42 -> Profile: 0014 2000 CEL0003 TPM 0.0332 0.67 1.50 7

0147 RECIP Waukesha 2895 GL Standard NGAS U.S. EPA AP-42 -> Profile: 0014 2000 CEL0004 PM10 0.0332 0.67 1.50 7

0147 RECIP Waukesha 2895 GL Standard NGAS U.S. EPA AP-42 -> Profile: 0014 2000 CEL0005 PM2.5 0.0332 0.67 1.50 7

0147 RECIP Waukesha 2895 GL Standard NGAS Manufacturer 2003 CEL0006 VOC 116 0.27 0.27 1 0147 RECIP Waukesha 2895 GL Standard NGAS Manufacturer 2003 CEL0007 THC 636 0.51 0.51 1

0148 RECIP Waukesha 3521 GL Standard NGAS CHEMEX Labs -> Profile: 0014 1996 10024-97-2 N2O 5.72 0.18 5.45 3

118

Table 3.3 Compilation of combustion emission factors for estimating GHG and CAC emissions.

Fact

or

Equ

ipm

ent

Typ

e

Identifier 1 Identifier 2 Identifier 3 Fuel Type

Factor Reference Y

ear CAS

Number Compound Emission

Factor (ng/J) L

ower

U

ncer

tain

ty

Upp

er

Unc

erta

inty

U

ncer

tain

ty

Ref

eren

ce

0148 RECIP Waukesha 3521 GL Standard NGAS Manufacturer 2003 630-08-0 CO 306 0.34 0.34 1 0148 RECIP Waukesha 3521 GL Standard NGAS Manufacturer 2003 74-82-8 CH4 520 0.59 0.59 1 0148 RECIP Waukesha 3521 GL Standard NGAS Manufacturer 2003 CEL0002 NOx 173 0.09 0.09 1

0148 RECIP Waukesha 3521 GL Standard NGAS U.S. EPA AP-42 -> Profile: 0014 2000 CEL0003 TPM 0.0332 0.67 1.50 7

0148 RECIP Waukesha 3521 GL Standard NGAS U.S. EPA AP-42 -> Profile: 0014 2000 CEL0004 PM10 0.0332 0.67 1.50 7

0148 RECIP Waukesha 3521 GL Standard NGAS U.S. EPA AP-42 -> Profile: 0014 2000 CEL0005 PM2.5 0.0332 0.67 1.50 7

0148 RECIP Waukesha 3521 GL Standard NGAS Manufacturer 2003 CEL0006 VOC 116 0.27 0.27 1 0148 RECIP Waukesha 3521 GL Standard NGAS Manufacturer 2003 CEL0007 THC 636 0.51 0.51 1

0149 RECIP Waukesha 5108 GL Standard NGAS CHEMEX Labs -> Profile: 0014 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0149 RECIP Waukesha 5108 GL Standard NGAS Manufacturer 2003 630-08-0 CO 306 0.34 0.34 1 0149 RECIP Waukesha 5108 GL Standard NGAS Manufacturer 2003 74-82-8 CH4 520 0.59 0.59 1 0149 RECIP Waukesha 5108 GL Standard NGAS Manufacturer 2003 CEL0002 NOx 173 0.09 0.09 1

0149 RECIP Waukesha 5108 GL Standard NGAS U.S. EPA AP-42 -> Profile: 0014 2000 CEL0003 TPM 0.0332 0.67 1.50 7

0149 RECIP Waukesha 5108 GL Standard NGAS U.S. EPA AP-42 -> Profile: 0014 2000 CEL0004 PM10 0.0332 0.67 1.50 7

0149 RECIP Waukesha 5108 GL Standard NGAS U.S. EPA AP-42 -> Profile: 0014 2000 CEL0005 PM2.5 0.0332 0.67 1.50 7

0149 RECIP Waukesha 5108 GL Standard NGAS Manufacturer 2003 CEL0006 VOC 116 0.27 0.27 1 0149 RECIP Waukesha 5108 GL Standard NGAS Manufacturer 2003 CEL0007 THC 636 0.51 0.51 1

0150 RECIP Waukesha 5790 GL Standard NGAS CHEMEX Labs -> Profile: 0014 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0150 RECIP Waukesha 5790 GL Standard NGAS Manufacturer 2003 630-08-0 CO 306 0.34 0.34 1 0150 RECIP Waukesha 5790 GL Standard NGAS Manufacturer 2003 74-82-8 CH4 520 0.59 0.59 1 0150 RECIP Waukesha 5790 GL Standard NGAS Manufacturer 2003 CEL0002 NOx 173 0.09 0.09 1

0150 RECIP Waukesha 5790 GL Standard NGAS U.S. EPA AP-42 -> Profile: 0014 2000 CEL0003 TPM 0.0332 0.67 1.50 7

0150 RECIP Waukesha 5790 GL Standard NGAS U.S. EPA AP-42 -> Profile: 0014 2000 CEL0004 PM10 0.0332 0.67 1.50 7

0150 RECIP Waukesha 5790 GL Standard NGAS U.S. EPA AP-42 -> Profile: 0014 2000 CEL0005 PM2.5 0.0332 0.67 1.50 7

0150 RECIP Waukesha 5790 GL Standard NGAS Manufacturer 2003 CEL0006 VOC 116 0.27 0.27 1

119

Table 3.3 Compilation of combustion emission factors for estimating GHG and CAC emissions.

Fact

or

Equ

ipm

ent

Typ

e

Identifier 1 Identifier 2 Identifier 3 Fuel Type

Factor Reference Y

ear CAS

Number Compound Emission

Factor (ng/J) L

ower

U

ncer

tain

ty

Upp

er

Unc

erta

inty

U

ncer

tain

ty

Ref

eren

ce

0150 RECIP Waukesha 5790 GL Standard NGAS Manufacturer 2003 CEL0007 THC 636 0.51 0.51 1

0151 RECIP Waukesha 7042 GL Standard NGAS CHEMEX Labs -> Profile: 0014 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0151 RECIP Waukesha 7042 GL Standard NGAS Manufacturer 2003 630-08-0 CO 306 0.34 0.34 1 0151 RECIP Waukesha 7042 GL Standard NGAS Manufacturer 2003 74-82-8 CH4 520 0.59 0.59 1 0151 RECIP Waukesha 7042 GL Standard NGAS Manufacturer 2003 CEL0002 NOx 173 0.09 0.09 1

0151 RECIP Waukesha 7042 GL Standard NGAS U.S. EPA AP-42 -> Profile: 0014 2000 CEL0003 TPM 0.0332 0.67 1.50 7

0151 RECIP Waukesha 7042 GL Standard NGAS U.S. EPA AP-42 -> Profile: 0014 2000 CEL0004 PM10 0.0332 0.67 1.50 7

0151 RECIP Waukesha 7042 GL Standard NGAS U.S. EPA AP-42 -> Profile: 0014 2000 CEL0005 PM2.5 0.0332 0.67 1.50 7

0151 RECIP Waukesha 7042 GL Standard NGAS Manufacturer 2003 CEL0006 VOC 116 0.27 0.27 1 0151 RECIP Waukesha 7042 GL Standard NGAS Manufacturer 2003 CEL0007 THC 636 0.51 0.51 1

0152 RECIP Waukesha 8L-AT25GL NGAS CHEMEX Labs -> Profile: 0014 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0152 RECIP Waukesha 8L-AT25GL NGAS Manufacturer 2003 630-08-0 CO 264 0.34 0.34 1

0152 RECIP Waukesha 8L-AT25GL NGAS U.S. EPA AP-42 -> Profile: 0014 2000 74-82-8 CH4 538 0.59 0.59 1

0152 RECIP Waukesha 8L-AT25GL NGAS Manufacturer 2003 CEL0002 NOx 176 0.09 0.09 1

0152 RECIP Waukesha 8L-AT25GL NGAS U.S. EPA AP-42 -> Profile: 0014 2000 CEL0003 TPM 0.0332 0.67 1.50 7

0152 RECIP Waukesha 8L-AT25GL NGAS U.S. EPA AP-42 -> Profile: 0014 2000 CEL0004 PM10 0.0332 0.67 1.50 7

0152 RECIP Waukesha 8L-AT25GL NGAS U.S. EPA AP-42 -> Profile: 0014 2000 CEL0005 PM2.5 0.0332 0.67 1.50 7

0152 RECIP Waukesha 8L-AT25GL NGAS Manufacturer 2003 CEL0006 VOC 117 0.27 0.27 1 0152 RECIP Waukesha 8L-AT25GL NGAS CH4 + VOC 2003 CEL0007 THC 655 0.48 0.48 1

0153 RECIP Waukesha 8L-AT27GL NGAS CHEMEX Labs -> Profile: 0014 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0153 RECIP Waukesha 8L-AT27GL NGAS Manufacturer 2003 630-08-0 CO 271 0.34 0.34 1

0153 RECIP Waukesha 8L-AT27GL NGAS U.S. EPA AP-42 -> Profile: 0014 2000 74-82-8 CH4 538 0.59 0.59 1

0153 RECIP Waukesha 8L-AT27GL NGAS Manufacturer 2003 CEL0002 NOx 181 0.09 0.09 1

0153 RECIP Waukesha 8L-AT27GL NGAS U.S. EPA AP-42 -> Profile: 0014 2000 CEL0003 TPM 0.0332 0.67 1.50 7

120

Table 3.3 Compilation of combustion emission factors for estimating GHG and CAC emissions.

Fact

or

Equ

ipm

ent

Typ

e

Identifier 1 Identifier 2 Identifier 3 Fuel Type

Factor Reference Y

ear CAS

Number Compound Emission

Factor (ng/J) L

ower

U

ncer

tain

ty

Upp

er

Unc

erta

inty

U

ncer

tain

ty

Ref

eren

ce

0153 RECIP Waukesha 8L-AT27GL NGAS U.S. EPA AP-42 -> Profile: 0014 2000 CEL0004 PM10 0.0332 0.67 1.50 7

0153 RECIP Waukesha 8L-AT27GL NGAS U.S. EPA AP-42 -> Profile: 0014 2000 CEL0005 PM2.5 0.0332 0.67 1.50 7

0153 RECIP Waukesha 8L-AT27GL NGAS Manufacturer 2003 CEL0006 VOC 121 0.27 0.27 1 0153 RECIP Waukesha 8L-AT27GL NGAS CH4 + VOC 2003 CEL0007 THC 659 0.48 0.48 1

0154 RECIP Waukesha 9390 GL Standard NGAS CHEMEX Labs -> Profile: 0014 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0154 RECIP Waukesha 9390 GL Standard NGAS Manufacturer 2003 630-08-0 CO 311 0.34 0.34 1 0154 RECIP Waukesha 9390 GL Standard NGAS Manufacturer 2003 74-82-8 CH4 528 0.59 0.59 1 0154 RECIP Waukesha 9390 GL Standard NGAS Manufacturer 2003 CEL0002 NOx 176 0.09 0.09 1

0154 RECIP Waukesha 9390 GL Standard NGAS U.S. EPA AP-42 -> Profile: 0014 2000 CEL0003 TPM 0.0332 0.67 1.50 7

0154 RECIP Waukesha 9390 GL Standard NGAS U.S. EPA AP-42 -> Profile: 0014 2000 CEL0004 PM10 0.0332 0.67 1.50 7

0154 RECIP Waukesha 9390 GL Standard NGAS U.S. EPA AP-42 -> Profile: 0014 2000 CEL0005 PM2.5 0.0332 0.67 1.50 7

0154 RECIP Waukesha 9390 GL Standard NGAS Manufacturer 2003 CEL0006 VOC 117 0.27 0.27 1 0154 RECIP Waukesha 9390 GL Standard NGAS Manufacturer 2003 CEL0007 THC 645 0.51 0.51 1

0155 RECIP Waukesha AT25GL standard NGAS CHEMEX Labs -> Profile: 0014 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0155 RECIP Waukesha AT25GL standard NGAS Manufacturer 2003 630-08-0 CO 266 0.34 0.34 1 0155 RECIP Waukesha AT25GL standard NGAS Manufacturer 2003 74-82-8 CH4 826 0.59 0.59 1 0155 RECIP Waukesha AT25GL standard NGAS Manufacturer 2003 CEL0002 NOx 118 0.09 0.09 1

0155 RECIP Waukesha AT25GL standard NGAS U.S. EPA AP-42 -> Profile: 0014 2000 CEL0003 TPM 0.0332 0.67 1.50 7

0155 RECIP Waukesha AT25GL standard NGAS U.S. EPA AP-42 -> Profile: 0014 2000 CEL0004 PM10 0.0332 0.67 1.50 7

0155 RECIP Waukesha AT25GL standard NGAS U.S. EPA AP-42 -> Profile: 0014 2000 CEL0005 PM2.5 0.0332 0.67 1.50 7

0155 RECIP Waukesha AT25GL standard NGAS Manufacturer 2003 CEL0006 VOC 118 0.27 0.27 1 0155 RECIP Waukesha AT25GL standard NGAS Manufacturer 2003 CEL0007 THC 945 0.51 0.51 1

0156 RECIP Waukesha AT27GL Ultra Lean NGAS CHEMEX Labs -> Profile: 0014 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0156 RECIP Waukesha AT27GL Ultra Lean NGAS Manufacturer 2003 630-08-0 CO 183 0.34 0.34 1 0156 RECIP Waukesha AT27GL Ultra Lean NGAS Manufacturer 2003 74-82-8 CH4 378 0.59 0.59 1

121

Table 3.3 Compilation of combustion emission factors for estimating GHG and CAC emissions.

Fact

or

Equ

ipm

ent

Typ

e

Identifier 1 Identifier 2 Identifier 3 Fuel Type

Factor Reference Y

ear CAS

Number Compound Emission

Factor (ng/J) L

ower

U

ncer

tain

ty

Upp

er

Unc

erta

inty

U

ncer

tain

ty

Ref

eren

ce

0156 RECIP Waukesha AT27GL Ultra Lean NGAS Manufacturer 2003 CEL0002 NOx 152 0.09 0.09 1

0156 RECIP Waukesha AT27GL Ultra Lean NGAS U.S. EPA AP-42 -> Profile: 0014 2000 CEL0003 TPM 0.0332 0.67 1.50 7

0156 RECIP Waukesha AT27GL Ultra Lean NGAS U.S. EPA AP-42 -> Profile: 0014 2000 CEL0004 PM10 0.0332 0.67 1.50 7

0156 RECIP Waukesha AT27GL Ultra Lean NGAS U.S. EPA AP-42 -> Profile: 0014 2000 CEL0005 PM2.5 0.0332 0.67 1.50 7

0156 RECIP Waukesha AT27GL Ultra Lean NGAS Manufacturer 2003 CEL0006 VOC 49 0.27 0.27 1 0156 RECIP Waukesha AT27GL Ultra Lean NGAS Manufacturer 2003 CEL0007 THC 427 0.51 0.51 1

0157 RECIP Waukesha AT27GL standard NGAS CHEMEX Labs -> Profile: 0014 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0157 RECIP Waukesha AT27GL standard NGAS Manufacturer 2003 630-08-0 CO 207 0.34 0.34 1 0157 RECIP Waukesha AT27GL standard NGAS Manufacturer 2003 74-82-8 CH4 549 0.59 0.59 1 0157 RECIP Waukesha AT27GL standard NGAS Manufacturer 2003 CEL0002 NOx 183 0.09 0.09 1

0157 RECIP Waukesha AT27GL standard NGAS U.S. EPA AP-42 -> Profile: 0014 2000 CEL0003 TPM 0.0332 0.67 1.50 7

0157 RECIP Waukesha AT27GL standard NGAS U.S. EPA AP-42 -> Profile: 0014 2000 CEL0004 PM10 0.0332 0.67 1.50 7

0157 RECIP Waukesha AT27GL standard NGAS U.S. EPA AP-42 -> Profile: 0014 2000 CEL0005 PM2.5 0.0332 0.67 1.50 7

0157 RECIP Waukesha AT27GL standard NGAS Manufacturer 2003 CEL0006 VOC 61 0.27 0.27 1 0157 RECIP Waukesha AT27GL standard NGAS Manufacturer 2003 CEL0007 THC 609 0.51 0.51 1

0158 RECIP Waukesha F1197G Catalytic conv. Input (3 way) NGAS

CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0158 RECIP Waukesha F1197G Catalytic conv. Input (3 way) NGAS Manufacturer 2003 630-08-0 CO 1688 0.34 0.34 1

0158 RECIP Waukesha F1197G Catalytic conv. Input (3 way) NGAS Manufacturer 2003 74-82-8 CH4 194 0.59 0.59 1

0158 RECIP Waukesha F1197G Catalytic conv. Input (3 way) NGAS Manufacturer 2003 CEL0002 NOx 1341 0.09 0.09 1

0158 RECIP Waukesha F1197G Catalytic conv. Input (3 way) NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

0158 RECIP Waukesha F1197G Catalytic conv. Input (3 way) NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

0158 RECIP Waukesha F1197G Catalytic conv. Input (3 way) NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

122

Table 3.3 Compilation of combustion emission factors for estimating GHG and CAC emissions.

Fact

or

Equ

ipm

ent

Typ

e

Identifier 1 Identifier 2 Identifier 3 Fuel Type

Factor Reference Y

ear CAS

Number Compound Emission

Factor (ng/J) L

ower

U

ncer

tain

ty

Upp

er

Unc

erta

inty

U

ncer

tain

ty

Ref

eren

ce

0158 RECIP Waukesha F1197G Catalytic conv. Input (3 way) NGAS Manufacturer 2003 CEL0006 VOC 35 0.27 0.27 1

0158 RECIP Waukesha F1197G Catalytic conv. Input (3 way) NGAS Manufacturer 2003 CEL0007 THC 228 0.51 0.51 1

0159 RECIP Waukesha F1197G Equal NOx & CO NGAS CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0159 RECIP Waukesha F1197G Equal NOx & CO NGAS Manufacturer 2003 630-08-0 CO 1390 0.34 0.34 1 0159 RECIP Waukesha F1197G Equal NOx & CO NGAS Manufacturer 2003 74-82-8 CH4 194 0.59 0.59 1 0159 RECIP Waukesha F1197G Equal NOx & CO NGAS Manufacturer 2003 CEL0002 NOx 1390 0.09 0.09 1

0159 RECIP Waukesha F1197G Equal NOx & CO NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

0159 RECIP Waukesha F1197G Equal NOx & CO NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

0159 RECIP Waukesha F1197G Equal NOx & CO NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

0159 RECIP Waukesha F1197G Equal NOx & CO NGAS Manufacturer 2003 CEL0006 VOC 35 0.27 0.27 1 0159 RECIP Waukesha F1197G Equal NOx & CO NGAS Manufacturer 2003 CEL0007 THC 228 0.51 0.51 1

0160 RECIP Waukesha F1197G Lowest Manifold (best power) NGAS

CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0160 RECIP Waukesha F1197G Lowest Manifold (best power) NGAS Manufacturer 2003 630-08-0 CO 3873 0.34 0.34 1

0160 RECIP Waukesha F1197G Lowest Manifold (best power) NGAS Manufacturer 2003 74-82-8 CH4 248 0.59 0.59 1

0160 RECIP Waukesha F1197G Lowest Manifold (best power) NGAS Manufacturer 2003 CEL0002 NOx 993 0.09 0.09 1

0160 RECIP Waukesha F1197G Lowest Manifold (best power) NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

0160 RECIP Waukesha F1197G Lowest Manifold (best power) NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

0160 RECIP Waukesha F1197G Lowest Manifold (best power) NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

0160 RECIP Waukesha F1197G Lowest Manifold (best power) NGAS Manufacturer 2003 CEL0006 VOC 50 0.27 0.27 1

0160 RECIP Waukesha F1197G Lowest Manifold (best power) NGAS Manufacturer 2003 CEL0007 THC 298 0.51 0.51 1

0161 RECIP Waukesha F1197G Standard (best NGAS CHEMEX Labs -> 1996 10024-97-2 N2O 5.72 0.18 5.45 3

123

Table 3.3 Compilation of combustion emission factors for estimating GHG and CAC emissions.

Fact

or

Equ

ipm

ent

Typ

e

Identifier 1 Identifier 2 Identifier 3 Fuel Type

Factor Reference Y

ear CAS

Number Compound Emission

Factor (ng/J) L

ower

U

ncer

tain

ty

Upp

er

Unc

erta

inty

U

ncer

tain

ty

Ref

eren

ce

economy) Profile: 0016

0161 RECIP Waukesha F1197G Standard (best economy) NGAS Manufacturer 2003 630-08-0 CO 129 0.34 0.34 1

0161 RECIP Waukesha F1197G Standard (best economy) NGAS Manufacturer 2003 74-82-8 CH4 94 0.59 0.59 1

0161 RECIP Waukesha F1197G Standard (best economy) NGAS Manufacturer 2003 CEL0002 NOx 2185 0.09 0.09 1

0161 RECIP Waukesha F1197G Standard (best economy) NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

0161 RECIP Waukesha F1197G Standard (best economy) NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

0161 RECIP Waukesha F1197G Standard (best economy) NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

0161 RECIP Waukesha F1197G Standard (best economy) NGAS Manufacturer 2003 CEL0006 VOC 25 0.27 0.27 1

0161 RECIP Waukesha F1197G Standard (best economy) NGAS Manufacturer 2003 CEL0007 THC 119 0.51 0.51 1

0162 RECIP Waukesha F1197G - 7:1 NGAS CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0162 RECIP Waukesha F1197G - 7:1 NGAS Manufacturer 2003 630-08-0 CO 92 0.34 0.34 1

0162 RECIP Waukesha F1197G - 7:1 NGAS U.S. EPA AP-42 -> Profile: 0016 2000 74-82-8 CH4 99 0.59 0.59 1

0162 RECIP Waukesha F1197G - 7:1 NGAS Manufacturer 2003 CEL0002 NOx 1835 0.09 0.09 1

0162 RECIP Waukesha F1197G - 7:1 NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

0162 RECIP Waukesha F1197G - 7:1 NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

0162 RECIP Waukesha F1197G - 7:1 NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

0162 RECIP Waukesha F1197G - 7:1 NGAS Manufacturer 2003 CEL0006 VOC 18 0.27 0.27 1 0162 RECIP Waukesha F1197G - 7:1 NGAS CH4 + VOC 2003 CEL0007 THC 117 0.50 0.50 1

0163 RECIP Waukesha F1197G - 9:1 NGAS CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0163 RECIP Waukesha F1197G - 9:1 NGAS Manufacturer 2003 630-08-0 CO 99 0.34 0.34 1

0163 RECIP Waukesha F1197G - 9:1 NGAS U.S. EPA AP-42 -> Profile: 0016 2000 74-82-8 CH4 99 0.59 0.59 1

124

Table 3.3 Compilation of combustion emission factors for estimating GHG and CAC emissions.

Fact

or

Equ

ipm

ent

Typ

e

Identifier 1 Identifier 2 Identifier 3 Fuel Type

Factor Reference Y

ear CAS

Number Compound Emission

Factor (ng/J) L

ower

U

ncer

tain

ty

Upp

er

Unc

erta

inty

U

ncer

tain

ty

Ref

eren

ce

0163 RECIP Waukesha F1197G - 9:1 NGAS Manufacturer 2003 CEL0002 NOx 1986 0.09 0.09 1

0163 RECIP Waukesha F1197G - 9:1 NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

0163 RECIP Waukesha F1197G - 9:1 NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

0163 RECIP Waukesha F1197G - 9:1 NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

0163 RECIP Waukesha F1197G - 9:1 NGAS Manufacturer 2003 CEL0006 VOC 20 0.27 0.27 1 0163 RECIP Waukesha F1197G - 9:1 NGAS CH4 + VOC 2003 CEL0007 THC 119 0.49 0.49 1

0164 RECIP Waukesha F11G Catalytic conv. Input (3 way) NGAS

CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0164 RECIP Waukesha F11G Catalytic conv. Input (3 way) NGAS Manufacturer 2003 630-08-0 CO 1206 0.34 0.34 1

0164 RECIP Waukesha F11G Catalytic conv. Input (3 way) NGAS Manufacturer 2003 74-82-8 CH4 231 0.59 0.59 1

0164 RECIP Waukesha F11G Catalytic conv. Input (3 way) NGAS Manufacturer 2003 CEL0002 NOx 1507 0.09 0.09 1

0164 RECIP Waukesha F11G Catalytic conv. Input (3 way) NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

0164 RECIP Waukesha F11G Catalytic conv. Input (3 way) NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

0164 RECIP Waukesha F11G Catalytic conv. Input (3 way) NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

0164 RECIP Waukesha F11G Catalytic conv. Input (3 way) NGAS Manufacturer 2003 CEL0006 VOC 50 0.27 0.27 1

0164 RECIP Waukesha F11G Catalytic conv. Input (3 way) NGAS Manufacturer 2003 CEL0007 THC 281 0.51 0.51 1

0165 RECIP Waukesha F11G Equal NOx & CO NGAS CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0165 RECIP Waukesha F11G Equal NOx & CO NGAS Manufacturer 2003 630-08-0 CO 1407 0.34 0.34 1 0165 RECIP Waukesha F11G Equal NOx & CO NGAS Manufacturer 2003 74-82-8 CH4 256 0.59 0.59 1 0165 RECIP Waukesha F11G Equal NOx & CO NGAS Manufacturer 2003 CEL0002 NOx 1407 0.09 0.09 1

0165 RECIP Waukesha F11G Equal NOx & CO NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

0165 RECIP Waukesha F11G Equal NOx & CO NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

125

Table 3.3 Compilation of combustion emission factors for estimating GHG and CAC emissions.

Fact

or

Equ

ipm

ent

Typ

e

Identifier 1 Identifier 2 Identifier 3 Fuel Type

Factor Reference Y

ear CAS

Number Compound Emission

Factor (ng/J) L

ower

U

ncer

tain

ty

Upp

er

Unc

erta

inty

U

ncer

tain

ty

Ref

eren

ce

0165 RECIP Waukesha F11G Equal NOx & CO NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

0165 RECIP Waukesha F11G Equal NOx & CO NGAS Manufacturer 2003 CEL0006 VOC 45 0.27 0.27 1 0165 RECIP Waukesha F11G Equal NOx & CO NGAS Manufacturer 2003 CEL0007 THC 301 0.51 0.51 1

0166 RECIP Waukesha F11G Lowest Manifold (best power) NGAS

CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0166 RECIP Waukesha F11G Lowest Manifold (best power) NGAS Manufacturer 2003 630-08-0 CO 3819 0.34 0.34 1

0166 RECIP Waukesha F11G Lowest Manifold (best power) NGAS Manufacturer 2003 74-82-8 CH4 256 0.59 0.59 1

0166 RECIP Waukesha F11G Lowest Manifold (best power) NGAS Manufacturer 2003 CEL0002 NOx 1005 0.09 0.09 1

0166 RECIP Waukesha F11G Lowest Manifold (best power) NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

0166 RECIP Waukesha F11G Lowest Manifold (best power) NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

0166 RECIP Waukesha F11G Lowest Manifold (best power) NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

0166 RECIP Waukesha F11G Lowest Manifold (best power) NGAS Manufacturer 2003 CEL0006 VOC 45 0.27 0.27 1

0166 RECIP Waukesha F11G Lowest Manifold (best power) NGAS Manufacturer 2003 CEL0007 THC 301 0.51 0.51 1

0167 RECIP Waukesha F11G Standard (best economy) NGAS

CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0167 RECIP Waukesha F11G Standard (best economy) NGAS Manufacturer 2003 630-08-0 CO 90 0.34 0.34 1

0167 RECIP Waukesha F11G Standard (best economy) NGAS Manufacturer 2003 74-82-8 CH4 171 0.59 0.59 1

0167 RECIP Waukesha F11G Standard (best economy) NGAS Manufacturer 2003 CEL0002 NOx 2512 0.09 0.09 1

0167 RECIP Waukesha F11G Standard (best economy) NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

0167 RECIP Waukesha F11G Standard (best economy) NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

0167 RECIP Waukesha F11G Standard (best economy) NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

126

Table 3.3 Compilation of combustion emission factors for estimating GHG and CAC emissions.

Fact

or

Equ

ipm

ent

Typ

e

Identifier 1 Identifier 2 Identifier 3 Fuel Type

Factor Reference Y

ear CAS

Number Compound Emission

Factor (ng/J) L

ower

U

ncer

tain

ty

Upp

er

Unc

erta

inty

U

ncer

tain

ty

Ref

eren

ce

0167 RECIP Waukesha F11G Standard (best economy) NGAS Manufacturer 2003 CEL0006 VOC 30 0.27 0.27 1

0167 RECIP Waukesha F11G Standard (best economy) NGAS Manufacturer 2003 CEL0007 THC 201 0.51 0.51 1

0168 RECIP Waukesha F11G - 10:1 NGAS CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0168 RECIP Waukesha F11G - 10:1 NGAS Manufacturer 2003 630-08-0 CO 79 0.34 0.34 1

0168 RECIP Waukesha F11G - 10:1 NGAS U.S. EPA AP-42 -> Profile: 0016 2000 74-82-8 CH4 99 0.59 0.59 1

0168 RECIP Waukesha F11G - 10:1 NGAS Manufacturer 2003 CEL0002 NOx 2080 0.09 0.09 1

0168 RECIP Waukesha F11G - 10:1 NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

0168 RECIP Waukesha F11G - 10:1 NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

0168 RECIP Waukesha F11G - 10:1 NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

0168 RECIP Waukesha F11G - 10:1 NGAS Manufacturer 2003 CEL0006 VOC 27 0.27 0.27 1 0168 RECIP Waukesha F11G - 10:1 NGAS CH4 + VOC 2003 CEL0007 THC 126 0.46 0.46 1

0169 RECIP Waukesha F11GSI Catalytic conv. Input (3 way) NGAS

CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0169 RECIP Waukesha F11GSI Catalytic conv. Input (3 way) NGAS Manufacturer 2003 630-08-0 CO 1677 0.34 0.34 1

0169 RECIP Waukesha F11GSI Catalytic conv. Input (3 way) NGAS Manufacturer 2003 74-82-8 CH4 140 0.59 0.59 1

0169 RECIP Waukesha F11GSI Catalytic conv. Input (3 way) NGAS Manufacturer 2003 CEL0002 NOx 2013 0.09 0.09 1

0169 RECIP Waukesha F11GSI Catalytic conv. Input (3 way) NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

0169 RECIP Waukesha F11GSI Catalytic conv. Input (3 way) NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

0169 RECIP Waukesha F11GSI Catalytic conv. Input (3 way) NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

0169 RECIP Waukesha F11GSI Catalytic conv. Input (3 way) NGAS Manufacturer 2003 CEL0006 VOC 28 0.27 0.27 1

0169 RECIP Waukesha F11GSI Catalytic conv. Input (3 way) NGAS Manufacturer 2003 CEL0007 THC 168 0.51 0.51 1

127

Table 3.3 Compilation of combustion emission factors for estimating GHG and CAC emissions.

Fact

or

Equ

ipm

ent

Typ

e

Identifier 1 Identifier 2 Identifier 3 Fuel Type

Factor Reference Y

ear CAS

Number Compound Emission

Factor (ng/J) L

ower

U

ncer

tain

ty

Upp

er

Unc

erta

inty

U

ncer

tain

ty

Ref

eren

ce

0170 RECIP Waukesha F11GSI Equal NOx & CO NGAS CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0170 RECIP Waukesha F11GSI Equal NOx & CO NGAS Manufacturer 2003 630-08-0 CO 1789 0.34 0.34 1 0170 RECIP Waukesha F11GSI Equal NOx & CO NGAS Manufacturer 2003 74-82-8 CH4 151 0.59 0.59 1 0170 RECIP Waukesha F11GSI Equal NOx & CO NGAS Manufacturer 2003 CEL0002 NOx 1789 0.09 0.09 1

0170 RECIP Waukesha F11GSI Equal NOx & CO NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

0170 RECIP Waukesha F11GSI Equal NOx & CO NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

0170 RECIP Waukesha F11GSI Equal NOx & CO NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

0170 RECIP Waukesha F11GSI Equal NOx & CO NGAS Manufacturer 2003 CEL0006 VOC 28 0.27 0.27 1 0170 RECIP Waukesha F11GSI Equal NOx & CO NGAS Manufacturer 2003 CEL0007 THC 179 0.51 0.51 1

0171 RECIP Waukesha F11GSI Lowest Manifold (best power) NGAS

CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0171 RECIP Waukesha F11GSI Lowest Manifold (best power) NGAS Manufacturer 2003 630-08-0 CO 3913 0.34 0.34 1

0171 RECIP Waukesha F11GSI Lowest Manifold (best power) NGAS Manufacturer 2003 74-82-8 CH4 162 0.59 0.59 1

0171 RECIP Waukesha F11GSI Lowest Manifold (best power) NGAS Manufacturer 2003 CEL0002 NOx 1062 0.09 0.09 1

0171 RECIP Waukesha F11GSI Lowest Manifold (best power) NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

0171 RECIP Waukesha F11GSI Lowest Manifold (best power) NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

0171 RECIP Waukesha F11GSI Lowest Manifold (best power) NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

0171 RECIP Waukesha F11GSI Lowest Manifold (best power) NGAS Manufacturer 2003 CEL0006 VOC 28 0.27 0.27 1

0171 RECIP Waukesha F11GSI Lowest Manifold (best power) NGAS Manufacturer 2003 CEL0007 THC 190 0.51 0.51 1

0172 RECIP Waukesha F11GSI Standard (best economy) NGAS

CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0172 RECIP Waukesha F11GSI Standard (best economy) NGAS Manufacturer 2003 630-08-0 CO 89 0.34 0.34 1

0172 RECIP Waukesha F11GSI Standard (best NGAS Manufacturer 2003 74-82-8 CH4 106 0.59 0.59 1

128

Table 3.3 Compilation of combustion emission factors for estimating GHG and CAC emissions.

Fact

or

Equ

ipm

ent

Typ

e

Identifier 1 Identifier 2 Identifier 3 Fuel Type

Factor Reference Y

ear CAS

Number Compound Emission

Factor (ng/J) L

ower

U

ncer

tain

ty

Upp

er

Unc

erta

inty

U

ncer

tain

ty

Ref

eren

ce

economy)

0172 RECIP Waukesha F11GSI Standard (best economy) NGAS Manufacturer 2003 CEL0002 NOx 3131 0.09 0.09 1

0172 RECIP Waukesha F11GSI Standard (best economy) NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

0172 RECIP Waukesha F11GSI Standard (best economy) NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

0172 RECIP Waukesha F11GSI Standard (best economy) NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

0172 RECIP Waukesha F11GSI Standard (best economy) NGAS Manufacturer 2003 CEL0006 VOC 28 0.27 0.27 1

0172 RECIP Waukesha F11GSI Standard (best economy) NGAS Manufacturer 2003 CEL0007 THC 134 0.51 0.51 1

0173 RECIP Waukesha F11GSI - 10:1 NGAS CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0173 RECIP Waukesha F11GSI - 10:1 NGAS Manufacturer 2003 630-08-0 CO 60 0.34 0.34 1

0173 RECIP Waukesha F11GSI - 10:1 NGAS U.S. EPA AP-42 -> Profile: 0016 2000 74-82-8 CH4 99 0.59 0.59 1

0173 RECIP Waukesha F11GSI - 10:1 NGAS Manufacturer 2003 CEL0002 NOx 2589 0.09 0.09 1

0173 RECIP Waukesha F11GSI - 10:1 NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

0173 RECIP Waukesha F11GSI - 10:1 NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

0173 RECIP Waukesha F11GSI - 10:1 NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

0173 RECIP Waukesha F11GSI - 10:1 NGAS Manufacturer 2003 CEL0006 VOC 14 0.27 0.27 1 0173 RECIP Waukesha F11GSI - 10:1 NGAS CH4 + VOC 2003 CEL0007 THC 113 0.52 0.52 1

0174 RECIP Waukesha F11GSID Catalytic conv. Input (3 way) NGAS

CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0174 RECIP Waukesha F11GSID Catalytic conv. Input (3 way) NGAS Manufacturer 2003 630-08-0 CO 1677 0.34 0.34 1

0174 RECIP Waukesha F11GSID Catalytic conv. Input (3 way) NGAS Manufacturer 2003 74-82-8 CH4 140 0.59 0.59 1

0174 RECIP Waukesha F11GSID Catalytic conv. Input (3 way) NGAS Manufacturer 2003 CEL0002 NOx 2013 0.09 0.09 1

0174 RECIP Waukesha F11GSID Catalytic conv. NGAS U.S. EPA AP-42 - 2000 CEL0003 TPM 4.09 0.50 2.00 8

129

Table 3.3 Compilation of combustion emission factors for estimating GHG and CAC emissions.

Fact

or

Equ

ipm

ent

Typ

e

Identifier 1 Identifier 2 Identifier 3 Fuel Type

Factor Reference Y

ear CAS

Number Compound Emission

Factor (ng/J) L

ower

U

ncer

tain

ty

Upp

er

Unc

erta

inty

U

ncer

tain

ty

Ref

eren

ce

Input (3 way) > Profile: 0016

0174 RECIP Waukesha F11GSID Catalytic conv. Input (3 way) NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

0174 RECIP Waukesha F11GSID Catalytic conv. Input (3 way) NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

0174 RECIP Waukesha F11GSID Catalytic conv. Input (3 way) NGAS Manufacturer 2003 CEL0006 VOC 28 0.27 0.27 1

0174 RECIP Waukesha F11GSID Catalytic conv. Input (3 way) NGAS Manufacturer 2003 CEL0007 THC 168 0.51 0.51 1

0175 RECIP Waukesha F11GSID Equal NOx & CO NGAS CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0175 RECIP Waukesha F11GSID Equal NOx & CO NGAS Manufacturer 2003 630-08-0 CO 1789 0.34 0.34 1 0175 RECIP Waukesha F11GSID Equal NOx & CO NGAS Manufacturer 2003 74-82-8 CH4 151 0.59 0.59 1 0175 RECIP Waukesha F11GSID Equal NOx & CO NGAS Manufacturer 2003 CEL0002 NOx 1789 0.09 0.09 1

0175 RECIP Waukesha F11GSID Equal NOx & CO NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

0175 RECIP Waukesha F11GSID Equal NOx & CO NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

0175 RECIP Waukesha F11GSID Equal NOx & CO NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

0175 RECIP Waukesha F11GSID Equal NOx & CO NGAS Manufacturer 2003 CEL0006 VOC 28 0.27 0.27 1 0175 RECIP Waukesha F11GSID Equal NOx & CO NGAS Manufacturer 2003 CEL0007 THC 179 0.51 0.51 1

0176 RECIP Waukesha F11GSID Lowest Manifold (best power) NGAS

CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0176 RECIP Waukesha F11GSID Lowest Manifold (best power) NGAS Manufacturer 2003 630-08-0 CO 3913 0.34 0.34 1

0176 RECIP Waukesha F11GSID Lowest Manifold (best power) NGAS Manufacturer 2003 74-82-8 CH4 162 0.59 0.59 1

0176 RECIP Waukesha F11GSID Lowest Manifold (best power) NGAS Manufacturer 2003 CEL0002 NOx 1062 0.09 0.09 1

0176 RECIP Waukesha F11GSID Lowest Manifold (best power) NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

0176 RECIP Waukesha F11GSID Lowest Manifold (best power) NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

0176 RECIP Waukesha F11GSID Lowest Manifold (best power) NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

130

Table 3.3 Compilation of combustion emission factors for estimating GHG and CAC emissions.

Fact

or

Equ

ipm

ent

Typ

e

Identifier 1 Identifier 2 Identifier 3 Fuel Type

Factor Reference Y

ear CAS

Number Compound Emission

Factor (ng/J) L

ower

U

ncer

tain

ty

Upp

er

Unc

erta

inty

U

ncer

tain

ty

Ref

eren

ce

0176 RECIP Waukesha F11GSID Lowest Manifold (best power) NGAS Manufacturer 2003 CEL0006 VOC 28 0.27 0.27 1

0176 RECIP Waukesha F11GSID Lowest Manifold (best power) NGAS Manufacturer 2003 CEL0007 THC 190 0.51 0.51 1

0177 RECIP Waukesha F11GSID Standard (best economy) NGAS

CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0177 RECIP Waukesha F11GSID Standard (best economy) NGAS Manufacturer 2003 630-08-0 CO 89 0.34 0.34 1

0177 RECIP Waukesha F11GSID Standard (best economy) NGAS Manufacturer 2003 74-82-8 CH4 106 0.59 0.59 1

0177 RECIP Waukesha F11GSID Standard (best economy) NGAS Manufacturer 2003 CEL0002 NOx 3131 0.09 0.09 1

0177 RECIP Waukesha F11GSID Standard (best economy) NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

0177 RECIP Waukesha F11GSID Standard (best economy) NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

0177 RECIP Waukesha F11GSID Standard (best economy) NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

0177 RECIP Waukesha F11GSID Standard (best economy) NGAS Manufacturer 2003 CEL0006 VOC 28 0.27 0.27 1

0177 RECIP Waukesha F11GSID Standard (best economy) NGAS Manufacturer 2003 CEL0007 THC 134 0.51 0.51 1

0178 RECIP Waukesha F11GSID - 10:1 NGAS CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0178 RECIP Waukesha F11GSID - 10:1 NGAS Manufacturer 2003 630-08-0 CO 63 0.34 0.34 1

0178 RECIP Waukesha F11GSID - 10:1 NGAS U.S. EPA AP-42 -> Profile: 0016 2000 74-82-8 CH4 99 0.59 0.59 1

0178 RECIP Waukesha F11GSID - 10:1 NGAS Manufacturer 2003 CEL0002 NOx 2683 0.09 0.09 1

0178 RECIP Waukesha F11GSID - 10:1 NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

0178 RECIP Waukesha F11GSID - 10:1 NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

0178 RECIP Waukesha F11GSID - 10:1 NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

0178 RECIP Waukesha F11GSID - 10:1 NGAS Manufacturer 2003 CEL0006 VOC 15 0.27 0.27 1 0178 RECIP Waukesha F11GSID - 10:1 NGAS CH4 + VOC 2003 CEL0007 THC 114 0.51 0.51 1

131

Table 3.3 Compilation of combustion emission factors for estimating GHG and CAC emissions.

Fact

or

Equ

ipm

ent

Typ

e

Identifier 1 Identifier 2 Identifier 3 Fuel Type

Factor Reference Y

ear CAS

Number Compound Emission

Factor (ng/J) L

ower

U

ncer

tain

ty

Upp

er

Unc

erta

inty

U

ncer

tain

ty

Ref

eren

ce

0179 RECIP Waukesha F18G Catalytic conv. Input (3 way) NGAS

CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0179 RECIP Waukesha F18G Catalytic conv. Input (3 way) NGAS Manufacturer 2003 630-08-0 CO 1126 0.34 0.34 1

0179 RECIP Waukesha F18G Catalytic conv. Input (3 way) NGAS Manufacturer 2003 74-82-8 CH4 191 0.59 0.59 1

0179 RECIP Waukesha F18G Catalytic conv. Input (3 way) NGAS Manufacturer 2003 CEL0002 NOx 1801 0.09 0.09 1

0179 RECIP Waukesha F18G Catalytic conv. Input (3 way) NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

0179 RECIP Waukesha F18G Catalytic conv. Input (3 way) NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

0179 RECIP Waukesha F18G Catalytic conv. Input (3 way) NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

0179 RECIP Waukesha F18G Catalytic conv. Input (3 way) NGAS Manufacturer 2003 CEL0006 VOC 34 0.27 0.27 1

0179 RECIP Waukesha F18G Catalytic conv. Input (3 way) NGAS Manufacturer 2003 CEL0007 THC 225 0.51 0.51 1

0180 RECIP Waukesha F18G Equal NOx & CO NGAS CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0180 RECIP Waukesha F18G Equal NOx & CO NGAS Manufacturer 2003 630-08-0 CO 1688 0.34 0.34 1 0180 RECIP Waukesha F18G Equal NOx & CO NGAS Manufacturer 2003 74-82-8 CH4 191 0.59 0.59 1 0180 RECIP Waukesha F18G Equal NOx & CO NGAS Manufacturer 2003 CEL0002 NOx 1688 0.09 0.09 1

0180 RECIP Waukesha F18G Equal NOx & CO NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

0180 RECIP Waukesha F18G Equal NOx & CO NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

0180 RECIP Waukesha F18G Equal NOx & CO NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

0180 RECIP Waukesha F18G Equal NOx & CO NGAS Manufacturer 2003 CEL0006 VOC 34 0.27 0.27 1 0180 RECIP Waukesha F18G Equal NOx & CO NGAS Manufacturer 2003 CEL0007 THC 225 0.51 0.51 1

0181 RECIP Waukesha F18G Lowest Manifold (best power) NGAS

CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0181 RECIP Waukesha F18G Lowest Manifold (best power) NGAS Manufacturer 2003 630-08-0 CO 3152 0.34 0.34 1

0181 RECIP Waukesha F18G Lowest Manifold NGAS Manufacturer 2003 74-82-8 CH4 191 0.59 0.59 1

132

Table 3.3 Compilation of combustion emission factors for estimating GHG and CAC emissions.

Fact

or

Equ

ipm

ent

Typ

e

Identifier 1 Identifier 2 Identifier 3 Fuel Type

Factor Reference Y

ear CAS

Number Compound Emission

Factor (ng/J) L

ower

U

ncer

tain

ty

Upp

er

Unc

erta

inty

U

ncer

tain

ty

Ref

eren

ce

(best power)

0181 RECIP Waukesha F18G Lowest Manifold (best power) NGAS Manufacturer 2003 CEL0002 NOx 1351 0.09 0.09 1

0181 RECIP Waukesha F18G Lowest Manifold (best power) NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

0181 RECIP Waukesha F18G Lowest Manifold (best power) NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

0181 RECIP Waukesha F18G Lowest Manifold (best power) NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

0181 RECIP Waukesha F18G Lowest Manifold (best power) NGAS Manufacturer 2003 CEL0006 VOC 34 0.27 0.27 1

0181 RECIP Waukesha F18G Lowest Manifold (best power) NGAS Manufacturer 2003 CEL0007 THC 225 0.51 0.51 1

0182 RECIP Waukesha F18G Standard (best economy) NGAS

CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0182 RECIP Waukesha F18G Standard (best economy) NGAS Manufacturer 2003 630-08-0 CO 90 0.34 0.34 1

0182 RECIP Waukesha F18G Standard (best economy) NGAS Manufacturer 2003 74-82-8 CH4 118 0.59 0.59 1

0182 RECIP Waukesha F18G Standard (best economy) NGAS Manufacturer 2003 CEL0002 NOx 3152 0.09 0.09 1

0182 RECIP Waukesha F18G Standard (best economy) NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

0182 RECIP Waukesha F18G Standard (best economy) NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

0182 RECIP Waukesha F18G Standard (best economy) NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

0182 RECIP Waukesha F18G Standard (best economy) NGAS Manufacturer 2003 CEL0006 VOC 28 0.27 0.27 1

0182 RECIP Waukesha F18G Standard (best economy) NGAS Manufacturer 2003 CEL0007 THC 146 0.51 0.51 1

0183 RECIP Waukesha F18G - 11:1 NGAS CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0183 RECIP Waukesha F18G - 11:1 NGAS Manufacturer 2003 630-08-0 CO 56 0.34 0.34 1

0183 RECIP Waukesha F18G - 11:1 NGAS U.S. EPA AP-42 -> Profile: 0016 2000 74-82-8 CH4 99 0.59 0.59 1

133

Table 3.3 Compilation of combustion emission factors for estimating GHG and CAC emissions.

Fact

or

Equ

ipm

ent

Typ

e

Identifier 1 Identifier 2 Identifier 3 Fuel Type

Factor Reference Y

ear CAS

Number Compound Emission

Factor (ng/J) L

ower

U

ncer

tain

ty

Upp

er

Unc

erta

inty

U

ncer

tain

ty

Ref

eren

ce

0183 RECIP Waukesha F18G - 11:1 NGAS Manufacturer 2003 CEL0002 NOx 2814 0.09 0.09 1

0183 RECIP Waukesha F18G - 11:1 NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

0183 RECIP Waukesha F18G - 11:1 NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

0183 RECIP Waukesha F18G - 11:1 NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

0183 RECIP Waukesha F18G - 11:1 NGAS Manufacturer 2003 CEL0006 VOC 19 0.27 0.27 1 0183 RECIP Waukesha F18G - 11:1 NGAS CH4 + VOC 2003 CEL0007 THC 118 0.49 0.49 1

0184 RECIP Waukesha F18GL 8:7:1:CR Standard (HS turbo) NGAS

CHEMEX Labs -> Profile: 0014 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0184 RECIP Waukesha F18GL 8:7:1:CR Standard (HS turbo) NGAS Manufacturer 2003 630-08-0 CO 199 0.34 0.34 1

0184 RECIP Waukesha F18GL 8:7:1:CR Standard (HS turbo) NGAS Manufacturer 2003 74-82-8 CH4 299 0.59 0.59 1

0184 RECIP Waukesha F18GL 8:7:1:CR Standard (HS turbo) NGAS Manufacturer 2003 CEL0002 NOx 234 0.09 0.09 1

0184 RECIP Waukesha F18GL 8:7:1:CR Standard (HS turbo) NGAS

U.S. EPA AP-42 -> Profile: 0014 2000 CEL0003 TPM 0.0332 0.67 1.50 7

0184 RECIP Waukesha F18GL 8:7:1:CR Standard (HS turbo) NGAS

U.S. EPA AP-42 -> Profile: 0014 2000 CEL0004 PM10 0.0332 0.67 1.50 7

0184 RECIP Waukesha F18GL 8:7:1:CR Standard (HS turbo) NGAS

U.S. EPA AP-42 -> Profile: 0014 2000 CEL0005 PM2.5 0.0332 0.67 1.50 7

0184 RECIP Waukesha F18GL 8:7:1:CR Standard (HS turbo) NGAS Manufacturer 2003 CEL0006 VOC 53 0.27 0.27 1

0184 RECIP Waukesha F18GL 8:7:1:CR Standard (HS turbo) NGAS Manufacturer 2003 CEL0007 THC 352 0.51 0.51 1

0185 RECIP Waukesha F18GL/GLD - 11:1 NGAS CHEMEX Labs -> Profile: 0014 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0185 RECIP Waukesha F18GL/GLD - 11:1 NGAS Manufacturer 2003 630-08-0 CO 234 0.34 0.34 1

0185 RECIP Waukesha F18GL/GLD - 11:1 NGAS U.S. EPA AP-42 -> Profile: 0014 2000 74-82-8 CH4 538 0.59 0.59 1

0185 RECIP Waukesha F18GL/GLD - 11:1 NGAS Manufacturer 2003 CEL0002 NOx 469 0.09 0.09 1

0185 RECIP Waukesha F18GL/GLD - 11:1 NGAS U.S. EPA AP-42 -> Profile: 0014 2000 CEL0003 TPM 0.0332 0.67 1.50 7

0185 RECIP Waukesha F18GL/GLD - 11:1 NGAS U.S. EPA AP-42 - 2000 CEL0004 PM10 0.0332 0.67 1.50 7

134

Table 3.3 Compilation of combustion emission factors for estimating GHG and CAC emissions.

Fact

or

Equ

ipm

ent

Typ

e

Identifier 1 Identifier 2 Identifier 3 Fuel Type

Factor Reference Y

ear CAS

Number Compound Emission

Factor (ng/J) L

ower

U

ncer

tain

ty

Upp

er

Unc

erta

inty

U

ncer

tain

ty

Ref

eren

ce

> Profile: 0014

0185 RECIP Waukesha F18GL/GLD - 11:1 NGAS U.S. EPA AP-42 -> Profile: 0014 2000 CEL0005 PM2.5 0.0332 0.67 1.50 7

0185 RECIP Waukesha F18GL/GLD - 11:1 NGAS Manufacturer 2003 CEL0006 VOC 117 0.27 0.27 1 0185 RECIP Waukesha F18GL/GLD - 11:1 NGAS CH4 + VOC 2003 CEL0007 THC 655 0.48 0.48 1

0186 RECIP Waukesha F18GL/GLD, 11:1 CR

Standard (HS turbo) NGAS

CHEMEX Labs -> Profile: 0014 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0186 RECIP Waukesha F18GL/GLD, 11:1 CR

Standard (HS turbo) NGAS Manufacturer 2003 630-08-0 CO 205 0.34 0.34 1

0186 RECIP Waukesha F18GL/GLD, 11:1 CR

Standard (HS turbo) NGAS Manufacturer 2003 74-82-8 CH4 498 0.59 0.59 1

0186 RECIP Waukesha F18GL/GLD, 11:1 CR

Standard (HS turbo) NGAS Manufacturer 2003 CEL0002 NOx 305 0.09 0.09 1

0186 RECIP Waukesha F18GL/GLD, 11:1 CR

Standard (HS turbo) NGAS

U.S. EPA AP-42 -> Profile: 0014 2000 CEL0003 TPM 0.0332 0.67 1.50 7

0186 RECIP Waukesha F18GL/GLD, 11:1 CR

Standard (HS turbo) NGAS

U.S. EPA AP-42 -> Profile: 0014 2000 CEL0004 PM10 0.0332 0.67 1.50 7

0186 RECIP Waukesha F18GL/GLD, 11:1 CR

Standard (HS turbo) NGAS

U.S. EPA AP-42 -> Profile: 0014 2000 CEL0005 PM2.5 0.0332 0.67 1.50 7

0186 RECIP Waukesha F18GL/GLD, 11:1 CR

Standard (HS turbo) NGAS Manufacturer 2003 CEL0006 VOC 88 0.27 0.27 1

0186 RECIP Waukesha F18GL/GLD, 11:1 CR

Standard (HS turbo) NGAS Manufacturer 2003 CEL0007 THC 586 0.51 0.51 1

0187 RECIP Waukesha F18GL/GLD, 11:1 CR

T.A. Luft Emissions NGAS

CHEMEX Labs -> Profile: 0014 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0187 RECIP Waukesha F18GL/GLD, 11:1 CR

T.A. Luft Emissions NGAS Manufacturer 2003 630-08-0 CO 186 0.34 0.34 1

0187 RECIP Waukesha F18GL/GLD, 11:1 CR

T.A. Luft Emissions NGAS Manufacturer 2003 74-82-8 CH4 358 0.59 0.59 1

0187 RECIP Waukesha F18GL/GLD, 11:1 CR

T.A. Luft Emissions NGAS Manufacturer 2003 CEL0002 NOx 147 0.09 0.09 1

0187 RECIP Waukesha F18GL/GLD, 11:1 CR

T.A. Luft Emissions NGAS

U.S. EPA AP-42 -> Profile: 0014 2000 CEL0003 TPM 0.0332 0.67 1.50 7

0187 RECIP Waukesha F18GL/GLD, 11:1 CR

T.A. Luft Emissions NGAS

U.S. EPA AP-42 -> Profile: 0014 2000 CEL0004 PM10 0.0332 0.67 1.50 7

0187 RECIP Waukesha F18GL/GLD, 11:1 T.A. Luft NGAS U.S. EPA AP-42 - 2000 CEL0005 PM2.5 0.0332 0.67 1.50 7

135

Table 3.3 Compilation of combustion emission factors for estimating GHG and CAC emissions.

Fact

or

Equ

ipm

ent

Typ

e

Identifier 1 Identifier 2 Identifier 3 Fuel Type

Factor Reference Y

ear CAS

Number Compound Emission

Factor (ng/J) L

ower

U

ncer

tain

ty

Upp

er

Unc

erta

inty

U

ncer

tain

ty

Ref

eren

ce

CR Emissions > Profile: 0014

0187 RECIP Waukesha F18GL/GLD, 11:1 CR

T.A. Luft Emissions NGAS Manufacturer 2003 CEL0006 VOC 53 0.27 0.27 1

0187 RECIP Waukesha F18GL/GLD, 11:1 CR

T.A. Luft Emissions NGAS Manufacturer 2003 CEL0007 THC 410 0.51 0.51 1

0188 RECIP Waukesha F18GSID Catalytic conv. Input (3 way) NGAS

CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0188 RECIP Waukesha F18GSID Catalytic conv. Input (3 way) NGAS Manufacturer 2003 630-08-0 CO 894 0.34 0.34 1

0188 RECIP Waukesha F18GSID Catalytic conv. Input (3 way) NGAS Manufacturer 2003 74-82-8 CH4 140 0.59 0.59 1

0188 RECIP Waukesha F18GSID Catalytic conv. Input (3 way) NGAS Manufacturer 2003 CEL0002 NOx 1789 0.09 0.09 1

0188 RECIP Waukesha F18GSID Catalytic conv. Input (3 way) NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

0188 RECIP Waukesha F18GSID Catalytic conv. Input (3 way) NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

0188 RECIP Waukesha F18GSID Catalytic conv. Input (3 way) NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

0188 RECIP Waukesha F18GSID Catalytic conv. Input (3 way) NGAS Manufacturer 2003 CEL0006 VOC 28 0.27 0.27 1

0188 RECIP Waukesha F18GSID Catalytic conv. Input (3 way) NGAS Manufacturer 2003 CEL0007 THC 168 0.51 0.51 1

0189 RECIP Waukesha F2895G Catalytic conv. Input (3 way) NGAS

CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0189 RECIP Waukesha F2895G Catalytic conv. Input (3 way) NGAS Manufacturer 2003 630-08-0 CO 1000 0.34 0.34 1

0189 RECIP Waukesha F2895G Catalytic conv. Input (3 way) NGAS Manufacturer 2003 74-82-8 CH4 189 0.59 0.59 1

0189 RECIP Waukesha F2895G Catalytic conv. Input (3 way) NGAS Manufacturer 2003 CEL0002 NOx 1444 0.09 0.09 1

0189 RECIP Waukesha F2895G Catalytic conv. Input (3 way) NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

0189 RECIP Waukesha F2895G Catalytic conv. Input (3 way) NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

0189 RECIP Waukesha F2895G Catalytic conv. NGAS U.S. EPA AP-42 - 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

136

Table 3.3 Compilation of combustion emission factors for estimating GHG and CAC emissions.

Fact

or

Equ

ipm

ent

Typ

e

Identifier 1 Identifier 2 Identifier 3 Fuel Type

Factor Reference Y

ear CAS

Number Compound Emission

Factor (ng/J) L

ower

U

ncer

tain

ty

Upp

er

Unc

erta

inty

U

ncer

tain

ty

Ref

eren

ce

Input (3 way) > Profile: 0016

0189 RECIP Waukesha F2895G Catalytic conv. Input (3 way) NGAS Manufacturer 2003 CEL0006 VOC 33 0.27 0.27 1

0189 RECIP Waukesha F2895G Catalytic conv. Input (3 way) NGAS Manufacturer 2003 CEL0007 THC 222 0.51 0.51 1

0190 RECIP Waukesha F2895G Equal NOx & CO NGAS CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0190 RECIP Waukesha F2895G Equal NOx & CO NGAS Manufacturer 2003 630-08-0 CO 1333 0.34 0.34 1 0190 RECIP Waukesha F2895G Equal NOx & CO NGAS Manufacturer 2003 74-82-8 CH4 217 0.59 0.59 1 0190 RECIP Waukesha F2895G Equal NOx & CO NGAS Manufacturer 2003 CEL0002 NOx 1333 0.09 0.09 1

0190 RECIP Waukesha F2895G Equal NOx & CO NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

0190 RECIP Waukesha F2895G Equal NOx & CO NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

0190 RECIP Waukesha F2895G Equal NOx & CO NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

0190 RECIP Waukesha F2895G Equal NOx & CO NGAS Manufacturer 2003 CEL0006 VOC 39 0.27 0.27 1 0190 RECIP Waukesha F2895G Equal NOx & CO NGAS Manufacturer 2003 CEL0007 THC 255 0.51 0.51 1

0191 RECIP Waukesha F2895G Lowest Manifold (best power) NGAS

CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0191 RECIP Waukesha F2895G Lowest Manifold (best power) NGAS Manufacturer 2003 630-08-0 CO 3554 0.34 0.34 1

0191 RECIP Waukesha F2895G Lowest Manifold (best power) NGAS Manufacturer 2003 74-82-8 CH4 217 0.59 0.59 1

0191 RECIP Waukesha F2895G Lowest Manifold (best power) NGAS Manufacturer 2003 CEL0002 NOx 1222 0.09 0.09 1

0191 RECIP Waukesha F2895G Lowest Manifold (best power) NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

0191 RECIP Waukesha F2895G Lowest Manifold (best power) NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

0191 RECIP Waukesha F2895G Lowest Manifold (best power) NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

0191 RECIP Waukesha F2895G Lowest Manifold (best power) NGAS Manufacturer 2003 CEL0006 VOC 39 0.27 0.27 1

0191 RECIP Waukesha F2895G Lowest Manifold (best power) NGAS Manufacturer 2003 CEL0007 THC 255 0.51 0.51 1

137

Table 3.3 Compilation of combustion emission factors for estimating GHG and CAC emissions.

Fact

or

Equ

ipm

ent

Typ

e

Identifier 1 Identifier 2 Identifier 3 Fuel Type

Factor Reference Y

ear CAS

Number Compound Emission

Factor (ng/J) L

ower

U

ncer

tain

ty

Upp

er

Unc

erta

inty

U

ncer

tain

ty

Ref

eren

ce

0192 RECIP Waukesha F2895G Standard (best economy) NGAS

CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0192 RECIP Waukesha F2895G Standard (best economy) NGAS Manufacturer 2003 630-08-0 CO 167 0.34 0.34 1

0192 RECIP Waukesha F2895G Standard (best economy) NGAS Manufacturer 2003 74-82-8 CH4 139 0.59 0.59 1

0192 RECIP Waukesha F2895G Standard (best economy) NGAS Manufacturer 2003 CEL0002 NOx 2444 0.09 0.09 1

0192 RECIP Waukesha F2895G Standard (best economy) NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

0192 RECIP Waukesha F2895G Standard (best economy) NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

0192 RECIP Waukesha F2895G Standard (best economy) NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

0192 RECIP Waukesha F2895G Standard (best economy) NGAS Manufacturer 2003 CEL0006 VOC 28 0.27 0.27 1

0192 RECIP Waukesha F2895G Standard (best economy) NGAS Manufacturer 2003 CEL0007 THC 167 0.51 0.51 1

0193 RECIP Waukesha F2895G - 10:1 NGAS CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0193 RECIP Waukesha F2895G - 10:1 NGAS Manufacturer 2003 630-08-0 CO 111 0.34 0.34 1

0193 RECIP Waukesha F2895G - 10:1 NGAS U.S. EPA AP-42 -> Profile: 0016 2000 74-82-8 CH4 99 0.59 0.59 1

0193 RECIP Waukesha F2895G - 10:1 NGAS Manufacturer 2003 CEL0002 NOx 1999 0.09 0.09 1

0193 RECIP Waukesha F2895G - 10:1 NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

0193 RECIP Waukesha F2895G - 10:1 NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

0193 RECIP Waukesha F2895G - 10:1 NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

0193 RECIP Waukesha F2895G - 10:1 NGAS Manufacturer 2003 CEL0006 VOC 22 0.27 0.27 1 0193 RECIP Waukesha F2895G - 10:1 NGAS CH4 + VOC 2003 CEL0007 THC 121 0.48 0.48 1

0194 RECIP Waukesha F2895G - 8.2:1 NGAS CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0194 RECIP Waukesha F2895G - 8.2:1 NGAS Manufacturer 2003 630-08-0 CO 104 0.34 0.34 1 0194 RECIP Waukesha F2895G - 8.2:1 NGAS U.S. EPA AP-42 - 2000 74-82-8 CH4 99 0.59 0.59 1

138

Table 3.3 Compilation of combustion emission factors for estimating GHG and CAC emissions.

Fact

or

Equ

ipm

ent

Typ

e

Identifier 1 Identifier 2 Identifier 3 Fuel Type

Factor Reference Y

ear CAS

Number Compound Emission

Factor (ng/J) L

ower

U

ncer

tain

ty

Upp

er

Unc

erta

inty

U

ncer

tain

ty

Ref

eren

ce

> Profile: 0016 0194 RECIP Waukesha F2895G - 8.2:1 NGAS Manufacturer 2003 CEL0002 NOx 1876 0.09 0.09 1

0194 RECIP Waukesha F2895G - 8.2:1 NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

0194 RECIP Waukesha F2895G - 8.2:1 NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

0194 RECIP Waukesha F2895G - 8.2:1 NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

0194 RECIP Waukesha F2895G - 8.2:1 NGAS Manufacturer 2003 CEL0006 VOC 21 0.27 0.27 1 0194 RECIP Waukesha F2895G - 8.2:1 NGAS CH4 + VOC 2003 CEL0007 THC 120 0.49 0.49 1

0195 RECIP Waukesha F2895GL - 10:1 NGAS CHEMEX Labs -> Profile: 0014 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0195 RECIP Waukesha F2895GL - 10:1 NGAS Manufacturer 2003 630-08-0 CO 306 0.34 0.34 1 0195 RECIP Waukesha F2895GL - 10:1 NGAS Manufacturer 2003 74-82-8 CH4 520 0.59 0.59 1 0195 RECIP Waukesha F2895GL - 10:1 NGAS Manufacturer 2003 CEL0002 NOx 173 0.09 0.09 1

0195 RECIP Waukesha F2895GL - 10:1 NGAS U.S. EPA AP-42 -> Profile: 0014 2000 CEL0003 TPM 0.0332 0.67 1.50 7

0195 RECIP Waukesha F2895GL - 10:1 NGAS U.S. EPA AP-42 -> Profile: 0014 2000 CEL0004 PM10 0.0332 0.67 1.50 7

0195 RECIP Waukesha F2895GL - 10:1 NGAS U.S. EPA AP-42 -> Profile: 0014 2000 CEL0005 PM2.5 0.0332 0.67 1.50 7

0195 RECIP Waukesha F2895GL - 10:1 NGAS Manufacturer 2003 CEL0006 VOC 116 0.27 0.27 1 0195 RECIP Waukesha F2895GL - 10:1 NGAS Manufacturer 2003 CEL0007 THC 636 0.51 0.51 1

0196 RECIP Waukesha F2895GSI Catalytic conv. Input (3 way) NGAS

CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0196 RECIP Waukesha F2895GSI Catalytic conv. Input (3 way) NGAS Manufacturer 2003 630-08-0 CO 962 0.34 0.34 1

0196 RECIP Waukesha F2895GSI Catalytic conv. Input (3 way) NGAS Manufacturer 2003 74-82-8 CH4 182 0.59 0.59 1

0196 RECIP Waukesha F2895GSI Catalytic conv. Input (3 way) NGAS Manufacturer 2003 CEL0002 NOx 1389 0.09 0.09 1

0196 RECIP Waukesha F2895GSI Catalytic conv. Input (3 way) NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

0196 RECIP Waukesha F2895GSI Catalytic conv. Input (3 way) NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

0196 RECIP Waukesha F2895GSI Catalytic conv. NGAS U.S. EPA AP-42 - 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

139

Table 3.3 Compilation of combustion emission factors for estimating GHG and CAC emissions.

Fact

or

Equ

ipm

ent

Typ

e

Identifier 1 Identifier 2 Identifier 3 Fuel Type

Factor Reference Y

ear CAS

Number Compound Emission

Factor (ng/J) L

ower

U

ncer

tain

ty

Upp

er

Unc

erta

inty

U

ncer

tain

ty

Ref

eren

ce

Input (3 way) > Profile: 0016

0196 RECIP Waukesha F2895GSI Catalytic conv. Input (3 way) NGAS Manufacturer 2003 CEL0006 VOC 32 0.27 0.27 1

0196 RECIP Waukesha F2895GSI Catalytic conv. Input (3 way) NGAS Manufacturer 2003 CEL0007 THC 214 0.51 0.51 1

0197 RECIP Waukesha F2895GSI Equal NOx & CO NGAS CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0197 RECIP Waukesha F2895GSI Equal NOx & CO NGAS Manufacturer 2003 630-08-0 CO 1282 0.34 0.34 1 0197 RECIP Waukesha F2895GSI Equal NOx & CO NGAS Manufacturer 2003 74-82-8 CH4 208 0.59 0.59 1 0197 RECIP Waukesha F2895GSI Equal NOx & CO NGAS Manufacturer 2003 CEL0002 NOx 1282 0.09 0.09 1

0197 RECIP Waukesha F2895GSI Equal NOx & CO NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

0197 RECIP Waukesha F2895GSI Equal NOx & CO NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

0197 RECIP Waukesha F2895GSI Equal NOx & CO NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

0197 RECIP Waukesha F2895GSI Equal NOx & CO NGAS Manufacturer 2003 CEL0006 VOC 37 0.27 0.27 1 0197 RECIP Waukesha F2895GSI Equal NOx & CO NGAS Manufacturer 2003 CEL0007 THC 246 0.51 0.51 1

0198 RECIP Waukesha F2895GSI Lowest Manifold (best power) NGAS

CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0198 RECIP Waukesha F2895GSI Lowest Manifold (best power) NGAS Manufacturer 2003 630-08-0 CO 3419 0.34 0.34 1

0198 RECIP Waukesha F2895GSI Lowest Manifold (best power) NGAS Manufacturer 2003 74-82-8 CH4 208 0.59 0.59 1

0198 RECIP Waukesha F2895GSI Lowest Manifold (best power) NGAS Manufacturer 2003 CEL0002 NOx 1175 0.09 0.09 1

0198 RECIP Waukesha F2895GSI Lowest Manifold (best power) NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

0198 RECIP Waukesha F2895GSI Lowest Manifold (best power) NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

0198 RECIP Waukesha F2895GSI Lowest Manifold (best power) NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

0198 RECIP Waukesha F2895GSI Lowest Manifold (best power) NGAS Manufacturer 2003 CEL0006 VOC 37 0.27 0.27 1

0198 RECIP Waukesha F2895GSI Lowest Manifold (best power) NGAS Manufacturer 2003 CEL0007 THC 246 0.51 0.51 1

140

Table 3.3 Compilation of combustion emission factors for estimating GHG and CAC emissions.

Fact

or

Equ

ipm

ent

Typ

e

Identifier 1 Identifier 2 Identifier 3 Fuel Type

Factor Reference Y

ear CAS

Number Compound Emission

Factor (ng/J) L

ower

U

ncer

tain

ty

Upp

er

Unc

erta

inty

U

ncer

tain

ty

Ref

eren

ce

0199 RECIP Waukesha F2895GSI Standard (best economy) NGAS

CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0199 RECIP Waukesha F2895GSI Standard (best economy) NGAS Manufacturer 2003 630-08-0 CO 160 0.34 0.34 1

0199 RECIP Waukesha F2895GSI Standard (best economy) NGAS Manufacturer 2003 74-82-8 CH4 134 0.59 0.59 1

0199 RECIP Waukesha F2895GSI Standard (best economy) NGAS Manufacturer 2003 CEL0002 NOx 2351 0.09 0.09 1

0199 RECIP Waukesha F2895GSI Standard (best economy) NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

0199 RECIP Waukesha F2895GSI Standard (best economy) NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

0199 RECIP Waukesha F2895GSI Standard (best economy) NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

0199 RECIP Waukesha F2895GSI Standard (best economy) NGAS Manufacturer 2003 CEL0006 VOC 27 0.27 0.27 1

0199 RECIP Waukesha F2895GSI Standard (best economy) NGAS Manufacturer 2003 CEL0007 THC 160 0.51 0.51 1

0200 RECIP Waukesha F2895GSI - 8.2:1 NGAS CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0200 RECIP Waukesha F2895GSI - 8.2:1 NGAS Manufacturer 2003 630-08-0 CO 107 0.34 0.34 1

0200 RECIP Waukesha F2895GSI - 8.2:1 NGAS U.S. EPA AP-42 -> Profile: 0016 2000 74-82-8 CH4 99 0.59 0.59 1

0200 RECIP Waukesha F2895GSI - 8.2:1 NGAS Manufacturer 2003 CEL0002 NOx 1923 0.09 0.09 1

0200 RECIP Waukesha F2895GSI - 8.2:1 NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

0200 RECIP Waukesha F2895GSI - 8.2:1 NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

0200 RECIP Waukesha F2895GSI - 8.2:1 NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

0200 RECIP Waukesha F2895GSI - 8.2:1 NGAS Manufacturer 2003 CEL0006 VOC 21 0.27 0.27 1 0200 RECIP Waukesha F2895GSI - 8.2:1 NGAS CH4 + VOC 2003 CEL0007 THC 120 0.49 0.49 1

0201 RECIP Waukesha F3521G Catalytic conv. Input (3 way) NGAS

CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0201 RECIP Waukesha F3521G Catalytic conv. Input (3 way) NGAS Manufacturer 2003 630-08-0 CO 974 0.34 0.34 1

141

Table 3.3 Compilation of combustion emission factors for estimating GHG and CAC emissions.

Fact

or

Equ

ipm

ent

Typ

e

Identifier 1 Identifier 2 Identifier 3 Fuel Type

Factor Reference Y

ear CAS

Number Compound Emission

Factor (ng/J) L

ower

U

ncer

tain

ty

Upp

er

Unc

erta

inty

U

ncer

tain

ty

Ref

eren

ce

0201 RECIP Waukesha F3521G Catalytic conv. Input (3 way) NGAS Manufacturer 2003 74-82-8 CH4 184 0.59 0.59 1

0201 RECIP Waukesha F3521G Catalytic conv. Input (3 way) NGAS Manufacturer 2003 CEL0002 NOx 1407 0.09 0.09 1

0201 RECIP Waukesha F3521G Catalytic conv. Input (3 way) NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

0201 RECIP Waukesha F3521G Catalytic conv. Input (3 way) NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

0201 RECIP Waukesha F3521G Catalytic conv. Input (3 way) NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

0201 RECIP Waukesha F3521G Catalytic conv. Input (3 way) NGAS Manufacturer 2003 CEL0006 VOC 32 0.27 0.27 1

0201 RECIP Waukesha F3521G Catalytic conv. Input (3 way) NGAS Manufacturer 2003 CEL0007 THC 216 0.51 0.51 1

0202 RECIP Waukesha F3521G Equal NOx & CO NGAS CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0202 RECIP Waukesha F3521G Equal NOx & CO NGAS Manufacturer 2003 630-08-0 CO 1299 0.34 0.34 1 0202 RECIP Waukesha F3521G Equal NOx & CO NGAS Manufacturer 2003 74-82-8 CH4 211 0.59 0.59 1 0202 RECIP Waukesha F3521G Equal NOx & CO NGAS Manufacturer 2003 CEL0002 NOx 1299 0.09 0.09 1

0202 RECIP Waukesha F3521G Equal NOx & CO NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

0202 RECIP Waukesha F3521G Equal NOx & CO NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

0202 RECIP Waukesha F3521G Equal NOx & CO NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

0202 RECIP Waukesha F3521G Equal NOx & CO NGAS Manufacturer 2003 CEL0006 VOC 38 0.27 0.27 1 0202 RECIP Waukesha F3521G Equal NOx & CO NGAS Manufacturer 2003 CEL0007 THC 249 0.51 0.51 1

0203 RECIP Waukesha F3521G Lowest Manifold (best power) NGAS

CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0203 RECIP Waukesha F3521G Lowest Manifold (best power) NGAS Manufacturer 2003 630-08-0 CO 3463 0.34 0.34 1

0203 RECIP Waukesha F3521G Lowest Manifold (best power) NGAS Manufacturer 2003 74-82-8 CH4 211 0.59 0.59 1

0203 RECIP Waukesha F3521G Lowest Manifold (best power) NGAS Manufacturer 2003 CEL0002 NOx 1190 0.09 0.09 1

0203 RECIP Waukesha F3521G Lowest Manifold NGAS U.S. EPA AP-42 - 2000 CEL0003 TPM 4.09 0.50 2.00 8

142

Table 3.3 Compilation of combustion emission factors for estimating GHG and CAC emissions.

Fact

or

Equ

ipm

ent

Typ

e

Identifier 1 Identifier 2 Identifier 3 Fuel Type

Factor Reference Y

ear CAS

Number Compound Emission

Factor (ng/J) L

ower

U

ncer

tain

ty

Upp

er

Unc

erta

inty

U

ncer

tain

ty

Ref

eren

ce

(best power) > Profile: 0016

0203 RECIP Waukesha F3521G Lowest Manifold (best power) NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

0203 RECIP Waukesha F3521G Lowest Manifold (best power) NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

0203 RECIP Waukesha F3521G Lowest Manifold (best power) NGAS Manufacturer 2003 CEL0006 VOC 38 0.27 0.27 1

0203 RECIP Waukesha F3521G Lowest Manifold (best power) NGAS Manufacturer 2003 CEL0007 THC 249 0.51 0.51 1

0204 RECIP Waukesha F3521G Standard (best economy) NGAS

CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0204 RECIP Waukesha F3521G Standard (best economy) NGAS Manufacturer 2003 630-08-0 CO 162 0.34 0.34 1

0204 RECIP Waukesha F3521G Standard (best economy) NGAS Manufacturer 2003 74-82-8 CH4 135 0.59 0.59 1

0204 RECIP Waukesha F3521G Standard (best economy) NGAS Manufacturer 2003 CEL0002 NOx 2381 0.09 0.09 1

0204 RECIP Waukesha F3521G Standard (best economy) NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

0204 RECIP Waukesha F3521G Standard (best economy) NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

0204 RECIP Waukesha F3521G Standard (best economy) NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

0204 RECIP Waukesha F3521G Standard (best economy) NGAS Manufacturer 2003 CEL0006 VOC 27 0.27 0.27 1

0204 RECIP Waukesha F3521G Standard (best economy) NGAS Manufacturer 2003 CEL0007 THC 162 0.51 0.51 1

0205 RECIP Waukesha F3521G - 10:1 NGAS CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0205 RECIP Waukesha F3521G - 10:1 NGAS Manufacturer 2003 630-08-0 CO 108 0.34 0.34 1

0205 RECIP Waukesha F3521G - 10:1 NGAS U.S. EPA AP-42 -> Profile: 0016 2000 74-82-8 CH4 99 0.59 0.59 1

0205 RECIP Waukesha F3521G - 10:1 NGAS Manufacturer 2003 CEL0002 NOx 1948 0.09 0.09 1

0205 RECIP Waukesha F3521G - 10:1 NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

0205 RECIP Waukesha F3521G - 10:1 NGAS U.S. EPA AP-42 - 2000 CEL0004 PM10 4.09 0.50 2.00 8

143

Table 3.3 Compilation of combustion emission factors for estimating GHG and CAC emissions.

Fact

or

Equ

ipm

ent

Typ

e

Identifier 1 Identifier 2 Identifier 3 Fuel Type

Factor Reference Y

ear CAS

Number Compound Emission

Factor (ng/J) L

ower

U

ncer

tain

ty

Upp

er

Unc

erta

inty

U

ncer

tain

ty

Ref

eren

ce

> Profile: 0016

0205 RECIP Waukesha F3521G - 10:1 NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

0205 RECIP Waukesha F3521G - 10:1 NGAS Manufacturer 2003 CEL0006 VOC 22 0.27 0.27 1 0205 RECIP Waukesha F3521G - 10:1 NGAS CH4 + VOC 2003 CEL0007 THC 121 0.48 0.48 1

0206 RECIP Waukesha F3521G - 8:1 NGAS CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0206 RECIP Waukesha F3521G - 8:1 NGAS Manufacturer 2003 630-08-0 CO 104 0.34 0.34 1

0206 RECIP Waukesha F3521G - 8:1 NGAS U.S. EPA AP-42 -> Profile: 0016 2000 74-82-8 CH4 99 0.59 0.59 1

0206 RECIP Waukesha F3521G - 8:1 NGAS Manufacturer 2003 CEL0002 NOx 1876 0.09 0.09 1

0206 RECIP Waukesha F3521G - 8:1 NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

0206 RECIP Waukesha F3521G - 8:1 NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

0206 RECIP Waukesha F3521G - 8:1 NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

0206 RECIP Waukesha F3521G - 8:1 NGAS Manufacturer 2003 CEL0006 VOC 21 0.27 0.27 1 0206 RECIP Waukesha F3521G - 8:1 NGAS CH4 + VOC 2003 CEL0007 THC 120 0.49 0.49 1

0207 RECIP Waukesha F3521GL - 10.5:1 NGAS CHEMEX Labs -> Profile: 0014 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0207 RECIP Waukesha F3521GL - 10.5:1 NGAS Manufacturer 2003 630-08-0 CO 306 0.34 0.34 1 0207 RECIP Waukesha F3521GL - 10.5:1 NGAS Manufacturer 2003 74-82-8 CH4 520 0.59 0.59 1 0207 RECIP Waukesha F3521GL - 10.5:1 NGAS Manufacturer 2003 CEL0002 NOx 173 0.09 0.09 1

0207 RECIP Waukesha F3521GL - 10.5:1 NGAS U.S. EPA AP-42 -> Profile: 0014 2000 CEL0003 TPM 0.0332 0.67 1.50 7

0207 RECIP Waukesha F3521GL - 10.5:1 NGAS U.S. EPA AP-42 -> Profile: 0014 2000 CEL0004 PM10 0.0332 0.67 1.50 7

0207 RECIP Waukesha F3521GL - 10.5:1 NGAS U.S. EPA AP-42 -> Profile: 0014 2000 CEL0005 PM2.5 0.0332 0.67 1.50 7

0207 RECIP Waukesha F3521GL - 10.5:1 NGAS Manufacturer 2003 CEL0006 VOC 116 0.27 0.27 1 0207 RECIP Waukesha F3521GL - 10.5:1 NGAS Manufacturer 2003 CEL0007 THC 636 0.51 0.51 1

0208 RECIP Waukesha F3521GSI Catalytic conv. Input (3 way) NGAS

CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0208 RECIP Waukesha F3521GSI Catalytic conv. Input (3 way) NGAS Manufacturer 2003 630-08-0 CO 965 0.34 0.34 1

144

Table 3.3 Compilation of combustion emission factors for estimating GHG and CAC emissions.

Fact

or

Equ

ipm

ent

Typ

e

Identifier 1 Identifier 2 Identifier 3 Fuel Type

Factor Reference Y

ear CAS

Number Compound Emission

Factor (ng/J) L

ower

U

ncer

tain

ty

Upp

er

Unc

erta

inty

U

ncer

tain

ty

Ref

eren

ce

0208 RECIP Waukesha F3521GSI Catalytic conv. Input (3 way) NGAS Manufacturer 2003 74-82-8 CH4 182 0.59 0.59 1

0208 RECIP Waukesha F3521GSI Catalytic conv. Input (3 way) NGAS Manufacturer 2003 CEL0002 NOx 1394 0.09 0.09 1

0208 RECIP Waukesha F3521GSI Catalytic conv. Input (3 way) NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

0208 RECIP Waukesha F3521GSI Catalytic conv. Input (3 way) NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

0208 RECIP Waukesha F3521GSI Catalytic conv. Input (3 way) NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

0208 RECIP Waukesha F3521GSI Catalytic conv. Input (3 way) NGAS Manufacturer 2003 CEL0006 VOC 32 0.27 0.27 1

0208 RECIP Waukesha F3521GSI Catalytic conv. Input (3 way) NGAS Manufacturer 2003 CEL0007 THC 214 0.51 0.51 1

0209 RECIP Waukesha F3521GSI Equal NOx & CO NGAS CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0209 RECIP Waukesha F3521GSI Equal NOx & CO NGAS Manufacturer 2003 630-08-0 CO 1286 0.34 0.34 1 0209 RECIP Waukesha F3521GSI Equal NOx & CO NGAS Manufacturer 2003 74-82-8 CH4 209 0.59 0.59 1 0209 RECIP Waukesha F3521GSI Equal NOx & CO NGAS Manufacturer 2003 CEL0002 NOx 1286 0.09 0.09 1

0209 RECIP Waukesha F3521GSI Equal NOx & CO NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

0209 RECIP Waukesha F3521GSI Equal NOx & CO NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

0209 RECIP Waukesha F3521GSI Equal NOx & CO NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

0209 RECIP Waukesha F3521GSI Equal NOx & CO NGAS Manufacturer 2003 CEL0006 VOC 38 0.27 0.27 1 0209 RECIP Waukesha F3521GSI Equal NOx & CO NGAS Manufacturer 2003 CEL0007 THC 247 0.51 0.51 1

0210 RECIP Waukesha F3521GSI Lowest Manifold (best power) NGAS

CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0210 RECIP Waukesha F3521GSI Lowest Manifold (best power) NGAS Manufacturer 2003 630-08-0 CO 3430 0.34 0.34 1

0210 RECIP Waukesha F3521GSI Lowest Manifold (best power) NGAS Manufacturer 2003 74-82-8 CH4 209 0.59 0.59 1

0210 RECIP Waukesha F3521GSI Lowest Manifold (best power) NGAS Manufacturer 2003 CEL0002 NOx 1179 0.09 0.09 1

0210 RECIP Waukesha F3521GSI Lowest Manifold NGAS U.S. EPA AP-42 - 2000 CEL0003 TPM 4.09 0.50 2.00 8

145

Table 3.3 Compilation of combustion emission factors for estimating GHG and CAC emissions.

Fact

or

Equ

ipm

ent

Typ

e

Identifier 1 Identifier 2 Identifier 3 Fuel Type

Factor Reference Y

ear CAS

Number Compound Emission

Factor (ng/J) L

ower

U

ncer

tain

ty

Upp

er

Unc

erta

inty

U

ncer

tain

ty

Ref

eren

ce

(best power) > Profile: 0016

0210 RECIP Waukesha F3521GSI Lowest Manifold (best power) NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

0210 RECIP Waukesha F3521GSI Lowest Manifold (best power) NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

0210 RECIP Waukesha F3521GSI Lowest Manifold (best power) NGAS Manufacturer 2003 CEL0006 VOC 38 0.27 0.27 1

0210 RECIP Waukesha F3521GSI Lowest Manifold (best power) NGAS Manufacturer 2003 CEL0007 THC 247 0.51 0.51 1

0211 RECIP Waukesha F3521GSI Standard (best economy) NGAS

CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0211 RECIP Waukesha F3521GSI Standard (best economy) NGAS Manufacturer 2003 630-08-0 CO 161 0.34 0.34 1

0211 RECIP Waukesha F3521GSI Standard (best economy) NGAS Manufacturer 2003 74-82-8 CH4 134 0.59 0.59 1

0211 RECIP Waukesha F3521GSI Standard (best economy) NGAS Manufacturer 2003 CEL0002 NOx 2358 0.09 0.09 1

0211 RECIP Waukesha F3521GSI Standard (best economy) NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

0211 RECIP Waukesha F3521GSI Standard (best economy) NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

0211 RECIP Waukesha F3521GSI Standard (best economy) NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

0211 RECIP Waukesha F3521GSI Standard (best economy) NGAS Manufacturer 2003 CEL0006 VOC 27 0.27 0.27 1

0211 RECIP Waukesha F3521GSI Standard (best economy) NGAS Manufacturer 2003 CEL0007 THC 161 0.51 0.51 1

0212 RECIP Waukesha F3521GSI - 8:1 NGAS CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0212 RECIP Waukesha F3521GSI - 8:1 NGAS Manufacturer 2003 630-08-0 CO 107 0.34 0.34 1

0212 RECIP Waukesha F3521GSI - 8:1 NGAS U.S. EPA AP-42 -> Profile: 0016 2000 74-82-8 CH4 99 0.59 0.59 1

0212 RECIP Waukesha F3521GSI - 8:1 NGAS Manufacturer 2003 CEL0002 NOx 1929 0.09 0.09 1

0212 RECIP Waukesha F3521GSI - 8:1 NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

0212 RECIP Waukesha F3521GSI - 8:1 NGAS U.S. EPA AP-42 - 2000 CEL0004 PM10 4.09 0.50 2.00 8

146

Table 3.3 Compilation of combustion emission factors for estimating GHG and CAC emissions.

Fact

or

Equ

ipm

ent

Typ

e

Identifier 1 Identifier 2 Identifier 3 Fuel Type

Factor Reference Y

ear CAS

Number Compound Emission

Factor (ng/J) L

ower

U

ncer

tain

ty

Upp

er

Unc

erta

inty

U

ncer

tain

ty

Ref

eren

ce

> Profile: 0016

0212 RECIP Waukesha F3521GSI - 8:1 NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

0212 RECIP Waukesha F3521GSI - 8:1 NGAS Manufacturer 2003 CEL0006 VOC 21 0.27 0.27 1 0212 RECIP Waukesha F3521GSI - 8:1 NGAS CH4 + VOC 2003 CEL0007 THC 120 0.49 0.49 1

0213 RECIP Waukesha F3524GSI Catalytic conv. Input (3 way) NGAS

CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0213 RECIP Waukesha F3524GSI Catalytic conv. Input (3 way) NGAS Manufacturer 2003 630-08-0 CO 1453 0.34 0.34 1

0213 RECIP Waukesha F3524GSI Catalytic conv. Input (3 way) NGAS Manufacturer 2003 74-82-8 CH4 89 0.59 0.59 1

0213 RECIP Waukesha F3524GSI Catalytic conv. Input (3 way) NGAS Manufacturer 2003 CEL0002 NOx 1676 0.09 0.09 1

0213 RECIP Waukesha F3524GSI Catalytic conv. Input (3 way) NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

0213 RECIP Waukesha F3524GSI Catalytic conv. Input (3 way) NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

0213 RECIP Waukesha F3524GSI Catalytic conv. Input (3 way) NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

0213 RECIP Waukesha F3524GSI Catalytic conv. Input (3 way) NGAS Manufacturer 2003 CEL0006 VOC 22 0.27 0.27 1

0213 RECIP Waukesha F3524GSI Catalytic conv. Input (3 way) NGAS Manufacturer 2003 CEL0007 THC 112 0.51 0.51 1

0214 RECIP Waukesha F3524GSI Equal NOx & CO NGAS CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0214 RECIP Waukesha F3524GSI Equal NOx & CO NGAS Manufacturer 2003 630-08-0 CO 1564 0.34 0.34 1 0214 RECIP Waukesha F3524GSI Equal NOx & CO NGAS Manufacturer 2003 74-82-8 CH4 95 0.59 0.59 1 0214 RECIP Waukesha F3524GSI Equal NOx & CO NGAS Manufacturer 2003 CEL0002 NOx 1564 0.09 0.09 1

0214 RECIP Waukesha F3524GSI Equal NOx & CO NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

0214 RECIP Waukesha F3524GSI Equal NOx & CO NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

0214 RECIP Waukesha F3524GSI Equal NOx & CO NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

0214 RECIP Waukesha F3524GSI Equal NOx & CO NGAS Manufacturer 2003 CEL0006 VOC 28 0.27 0.27 1 0214 RECIP Waukesha F3524GSI Equal NOx & CO NGAS Manufacturer 2003 CEL0007 THC 123 0.51 0.51 1

147

Table 3.3 Compilation of combustion emission factors for estimating GHG and CAC emissions.

Fact

or

Equ

ipm

ent

Typ

e

Identifier 1 Identifier 2 Identifier 3 Fuel Type

Factor Reference Y

ear CAS

Number Compound Emission

Factor (ng/J) L

ower

U

ncer

tain

ty

Upp

er

Unc

erta

inty

U

ncer

tain

ty

Ref

eren

ce

0215 RECIP Waukesha F3524GSI Standard (best economy) NGAS

CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0215 RECIP Waukesha F3524GSI Standard (best economy) NGAS Manufacturer 2003 630-08-0 CO 223 0.34 0.34 1

0215 RECIP Waukesha F3524GSI Standard (best economy) NGAS Manufacturer 2003 74-82-8 CH4 67 0.59 0.59 1

0215 RECIP Waukesha F3524GSI Standard (best economy) NGAS Manufacturer 2003 CEL0002 NOx 2570 0.09 0.09 1

0215 RECIP Waukesha F3524GSI Standard (best economy) NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

0215 RECIP Waukesha F3524GSI Standard (best economy) NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

0215 RECIP Waukesha F3524GSI Standard (best economy) NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

0215 RECIP Waukesha F3524GSI Standard (best economy) NGAS Manufacturer 2003 CEL0006 VOC 22 0.27 0.27 1

0215 RECIP Waukesha F3524GSI Standard (best economy) NGAS Manufacturer 2003 CEL0007 THC 89 0.51 0.51 1

0216 RECIP Waukesha F817G Catalytic conv. Input (3 way) NGAS

CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0216 RECIP Waukesha F817G Catalytic conv. Input (3 way) NGAS Manufacturer 2003 630-08-0 CO 1455 0.34 0.34 1

0216 RECIP Waukesha F817G Catalytic conv. Input (3 way) NGAS Manufacturer 2003 74-82-8 CH4 165 0.59 0.59 1

0216 RECIP Waukesha F817G Catalytic conv. Input (3 way) NGAS Manufacturer 2003 CEL0002 NOx 1164 0.09 0.09 1

0216 RECIP Waukesha F817G Catalytic conv. Input (3 way) NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

0216 RECIP Waukesha F817G Catalytic conv. Input (3 way) NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

0216 RECIP Waukesha F817G Catalytic conv. Input (3 way) NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

0216 RECIP Waukesha F817G Catalytic conv. Input (3 way) NGAS Manufacturer 2003 CEL0006 VOC 29 0.27 0.27 1

0216 RECIP Waukesha F817G Catalytic conv. Input (3 way) NGAS Manufacturer 2003 CEL0007 THC 194 0.51 0.51 1

148

Table 3.3 Compilation of combustion emission factors for estimating GHG and CAC emissions.

Fact

or

Equ

ipm

ent

Typ

e

Identifier 1 Identifier 2 Identifier 3 Fuel Type

Factor Reference Y

ear CAS

Number Compound Emission

Factor (ng/J) L

ower

U

ncer

tain

ty

Upp

er

Unc

erta

inty

U

ncer

tain

ty

Ref

eren

ce

0217 RECIP Waukesha F817G Equal NOx & CO NGAS CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0217 RECIP Waukesha F817G Equal NOx & CO NGAS Manufacturer 2003 630-08-0 CO 1261 0.34 0.34 1 0217 RECIP Waukesha F817G Equal NOx & CO NGAS Manufacturer 2003 74-82-8 CH4 165 0.59 0.59 1 0217 RECIP Waukesha F817G Equal NOx & CO NGAS Manufacturer 2003 CEL0002 NOx 1261 0.09 0.09 1

0217 RECIP Waukesha F817G Equal NOx & CO NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

0217 RECIP Waukesha F817G Equal NOx & CO NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

0217 RECIP Waukesha F817G Equal NOx & CO NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

0217 RECIP Waukesha F817G Equal NOx & CO NGAS Manufacturer 2003 CEL0006 VOC 29 0.27 0.27 1 0217 RECIP Waukesha F817G Equal NOx & CO NGAS Manufacturer 2003 CEL0007 THC 194 0.51 0.51 1

0218 RECIP Waukesha F817G Lowest Manifold (best power) NGAS

CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0218 RECIP Waukesha F817G Lowest Manifold (best power) NGAS Manufacturer 2003 630-08-0 CO 3687 0.34 0.34 1

0218 RECIP Waukesha F817G Lowest Manifold (best power) NGAS Manufacturer 2003 74-82-8 CH4 189 0.59 0.59 1

0218 RECIP Waukesha F817G Lowest Manifold (best power) NGAS Manufacturer 2003 CEL0002 NOx 825 0.09 0.09 1

0218 RECIP Waukesha F817G Lowest Manifold (best power) NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

0218 RECIP Waukesha F817G Lowest Manifold (best power) NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

0218 RECIP Waukesha F817G Lowest Manifold (best power) NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

0218 RECIP Waukesha F817G Lowest Manifold (best power) NGAS Manufacturer 2003 CEL0006 VOC 34 0.27 0.27 1

0218 RECIP Waukesha F817G Lowest Manifold (best power) NGAS Manufacturer 2003 CEL0007 THC 223 0.51 0.51 1

0219 RECIP Waukesha F817G Standard (best economy) NGAS

CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0219 RECIP Waukesha F817G Standard (best economy) NGAS Manufacturer 2003 630-08-0 CO 126 0.34 0.34 1

0219 RECIP Waukesha F817G Standard (best NGAS Manufacturer 2003 74-82-8 CH4 165 0.59 0.59 1

149

Table 3.3 Compilation of combustion emission factors for estimating GHG and CAC emissions.

Fact

or

Equ

ipm

ent

Typ

e

Identifier 1 Identifier 2 Identifier 3 Fuel Type

Factor Reference Y

ear CAS

Number Compound Emission

Factor (ng/J) L

ower

U

ncer

tain

ty

Upp

er

Unc

erta

inty

U

ncer

tain

ty

Ref

eren

ce

economy)

0219 RECIP Waukesha F817G Standard (best economy) NGAS Manufacturer 2003 CEL0002 NOx 1747 0.09 0.09 1

0219 RECIP Waukesha F817G Standard (best economy) NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

0219 RECIP Waukesha F817G Standard (best economy) NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

0219 RECIP Waukesha F817G Standard (best economy) NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

0219 RECIP Waukesha F817G Standard (best economy) NGAS Manufacturer 2003 CEL0006 VOC 29 0.27 0.27 1

0219 RECIP Waukesha F817G Standard (best economy) NGAS Manufacturer 2003 CEL0007 THC 194 0.51 0.51 1

0220 RECIP Waukesha F817G - 7.2:1 NGAS CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0220 RECIP Waukesha F817G - 7.2:1 NGAS Manufacturer 2003 630-08-0 CO 93 0.34 0.34 1

0220 RECIP Waukesha F817G - 7.2:1 NGAS U.S. EPA AP-42 -> Profile: 0016 2000 74-82-8 CH4 99 0.59 0.59 1

0220 RECIP Waukesha F817G - 7.2:1 NGAS Manufacturer 2003 CEL0002 NOx 1484 0.09 0.09 1

0220 RECIP Waukesha F817G - 7.2:1 NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

0220 RECIP Waukesha F817G - 7.2:1 NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

0220 RECIP Waukesha F817G - 7.2:1 NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

0220 RECIP Waukesha F817G - 7.2:1 NGAS Manufacturer 2003 CEL0006 VOC 23 0.27 0.27 1 0220 RECIP Waukesha F817G - 7.2:1 NGAS CH4 + VOC 2003 CEL0007 THC 122 0.48 0.48 1

0221 RECIP Waukesha F817G - 9:1 NGAS CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0221 RECIP Waukesha F817G - 9:1 NGAS Manufacturer 2003 630-08-0 CO 97 0.34 0.34 1

0221 RECIP Waukesha F817G - 9:1 NGAS U.S. EPA AP-42 -> Profile: 0016 2000 74-82-8 CH4 99 0.59 0.59 1

0221 RECIP Waukesha F817G - 9:1 NGAS Manufacturer 2003 CEL0002 NOx 1552 0.09 0.09 1

0221 RECIP Waukesha F817G - 9:1 NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

0221 RECIP Waukesha F817G - 9:1 NGAS U.S. EPA AP-42 - 2000 CEL0004 PM10 4.09 0.50 2.00 8

150

Table 3.3 Compilation of combustion emission factors for estimating GHG and CAC emissions.

Fact

or

Equ

ipm

ent

Typ

e

Identifier 1 Identifier 2 Identifier 3 Fuel Type

Factor Reference Y

ear CAS

Number Compound Emission

Factor (ng/J) L

ower

U

ncer

tain

ty

Upp

er

Unc

erta

inty

U

ncer

tain

ty

Ref

eren

ce

> Profile: 0016

0221 RECIP Waukesha F817G - 9:1 NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

0221 RECIP Waukesha F817G - 9:1 NGAS Manufacturer 2003 CEL0006 VOC 24 0.27 0.27 1 0221 RECIP Waukesha F817G - 9:1 NGAS CH4 + VOC 2003 CEL0007 THC 123 0.48 0.48 1

0222 RECIP Waukesha H24G Catalytic conv. Input (3 way) NGAS

CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0222 RECIP Waukesha H24G Catalytic conv. Input (3 way) NGAS Manufacturer 2003 630-08-0 CO 1126 0.34 0.34 1

0222 RECIP Waukesha H24G Catalytic conv. Input (3 way) NGAS Manufacturer 2003 74-82-8 CH4 191 0.59 0.59 1

0222 RECIP Waukesha H24G Catalytic conv. Input (3 way) NGAS Manufacturer 2003 CEL0002 NOx 1801 0.09 0.09 1

0222 RECIP Waukesha H24G Catalytic conv. Input (3 way) NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

0222 RECIP Waukesha H24G Catalytic conv. Input (3 way) NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

0222 RECIP Waukesha H24G Catalytic conv. Input (3 way) NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

0222 RECIP Waukesha H24G Catalytic conv. Input (3 way) NGAS Manufacturer 2003 CEL0006 VOC 34 0.27 0.27 1

0222 RECIP Waukesha H24G Catalytic conv. Input (3 way) NGAS Manufacturer 2003 CEL0007 THC 225 0.51 0.51 1

0223 RECIP Waukesha H24G Equal NOx & CO NGAS CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0223 RECIP Waukesha H24G Equal NOx & CO NGAS Manufacturer 2003 630-08-0 CO 1688 0.34 0.34 1 0223 RECIP Waukesha H24G Equal NOx & CO NGAS Manufacturer 2003 74-82-8 CH4 191 0.59 0.59 1 0223 RECIP Waukesha H24G Equal NOx & CO NGAS Manufacturer 2003 CEL0002 NOx 1688 0.09 0.09 1

0223 RECIP Waukesha H24G Equal NOx & CO NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

0223 RECIP Waukesha H24G Equal NOx & CO NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

0223 RECIP Waukesha H24G Equal NOx & CO NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

0223 RECIP Waukesha H24G Equal NOx & CO NGAS Manufacturer 2003 CEL0006 VOC 34 0.27 0.27 1 0223 RECIP Waukesha H24G Equal NOx & CO NGAS Manufacturer 2003 CEL0007 THC 225 0.51 0.51 1

151

Table 3.3 Compilation of combustion emission factors for estimating GHG and CAC emissions.

Fact

or

Equ

ipm

ent

Typ

e

Identifier 1 Identifier 2 Identifier 3 Fuel Type

Factor Reference Y

ear CAS

Number Compound Emission

Factor (ng/J) L

ower

U

ncer

tain

ty

Upp

er

Unc

erta

inty

U

ncer

tain

ty

Ref

eren

ce

0224 RECIP Waukesha H24G Lowest Manifold (best power) NGAS

CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0224 RECIP Waukesha H24G Lowest Manifold (best power) NGAS Manufacturer 2003 630-08-0 CO 3152 0.34 0.34 1

0224 RECIP Waukesha H24G Lowest Manifold (best power) NGAS Manufacturer 2003 74-82-8 CH4 191 0.59 0.59 1

0224 RECIP Waukesha H24G Lowest Manifold (best power) NGAS Manufacturer 2003 CEL0002 NOx 1351 0.09 0.09 1

0224 RECIP Waukesha H24G Lowest Manifold (best power) NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

0224 RECIP Waukesha H24G Lowest Manifold (best power) NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

0224 RECIP Waukesha H24G Lowest Manifold (best power) NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

0224 RECIP Waukesha H24G Lowest Manifold (best power) NGAS Manufacturer 2003 CEL0006 VOC 34 0.27 0.27 1

0224 RECIP Waukesha H24G Lowest Manifold (best power) NGAS Manufacturer 2003 CEL0007 THC 225 0.51 0.51 1

0225 RECIP Waukesha H24G Standard (best economy) NGAS

CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0225 RECIP Waukesha H24G Standard (best economy) NGAS Manufacturer 2003 630-08-0 CO 90 0.34 0.34 1

0225 RECIP Waukesha H24G Standard (best economy) NGAS Manufacturer 2003 74-82-8 CH4 118 0.59 0.59 1

0225 RECIP Waukesha H24G Standard (best economy) NGAS Manufacturer 2003 CEL0002 NOx 3152 0.09 0.09 1

0225 RECIP Waukesha H24G Standard (best economy) NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

0225 RECIP Waukesha H24G Standard (best economy) NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

0225 RECIP Waukesha H24G Standard (best economy) NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

0225 RECIP Waukesha H24G Standard (best economy) NGAS Manufacturer 2003 CEL0006 VOC 28 0.27 0.27 1

0225 RECIP Waukesha H24G Standard (best economy) NGAS Manufacturer 2003 CEL0007 THC 146 0.51 0.51 1

152

Table 3.3 Compilation of combustion emission factors for estimating GHG and CAC emissions.

Fact

or

Equ

ipm

ent

Typ

e

Identifier 1 Identifier 2 Identifier 3 Fuel Type

Factor Reference Y

ear CAS

Number Compound Emission

Factor (ng/J) L

ower

U

ncer

tain

ty

Upp

er

Unc

erta

inty

U

ncer

tain

ty

Ref

eren

ce

0226 RECIP Waukesha H24G - 11:1 NGAS CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0226 RECIP Waukesha H24G - 11:1 NGAS Manufacturer 2003 630-08-0 CO 56 0.34 0.34 1

0226 RECIP Waukesha H24G - 11:1 NGAS U.S. EPA AP-42 -> Profile: 0016 2000 74-82-8 CH4 99 0.59 0.59 1

0226 RECIP Waukesha H24G - 11:1 NGAS Manufacturer 2003 CEL0002 NOx 2814 0.09 0.09 1

0226 RECIP Waukesha H24G - 11:1 NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

0226 RECIP Waukesha H24G - 11:1 NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

0226 RECIP Waukesha H24G - 11:1 NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

0226 RECIP Waukesha H24G - 11:1 NGAS Manufacturer 2003 CEL0006 VOC 19 0.27 0.27 1 0226 RECIP Waukesha H24G - 11:1 NGAS CH4 + VOC 2003 CEL0007 THC 118 0.49 0.49 1

0227 RECIP Waukesha H24GL 8:7:1:CR Standard (HS turbo) NGAS

CHEMEX Labs -> Profile: 0014 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0227 RECIP Waukesha H24GL 8:7:1:CR Standard (HS turbo) NGAS Manufacturer 2003 630-08-0 CO 202 0.34 0.34 1

0227 RECIP Waukesha H24GL 8:7:1:CR Standard (HS turbo) NGAS Manufacturer 2003 74-82-8 CH4 303 0.59 0.59 1

0227 RECIP Waukesha H24GL 8:7:1:CR Standard (HS turbo) NGAS Manufacturer 2003 CEL0002 NOx 238 0.09 0.09 1

0227 RECIP Waukesha H24GL 8:7:1:CR Standard (HS turbo) NGAS

U.S. EPA AP-42 -> Profile: 0014 2000 CEL0003 TPM 0.0332 0.67 1.50 7

0227 RECIP Waukesha H24GL 8:7:1:CR Standard (HS turbo) NGAS

U.S. EPA AP-42 -> Profile: 0014 2000 CEL0004 PM10 0.0332 0.67 1.50 7

0227 RECIP Waukesha H24GL 8:7:1:CR Standard (HS turbo) NGAS

U.S. EPA AP-42 -> Profile: 0014 2000 CEL0005 PM2.5 0.0332 0.67 1.50 7

0227 RECIP Waukesha H24GL 8:7:1:CR Standard (HS turbo) NGAS Manufacturer 2003 CEL0006 VOC 54 0.27 0.27 1

0227 RECIP Waukesha H24GL 8:7:1:CR Standard (HS turbo) NGAS Manufacturer 2003 CEL0007 THC 357 0.51 0.51 1

0228 RECIP Waukesha H24GL/GLD - 11:1 NGAS

CHEMEX Labs -> Profile: 0014 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0228 RECIP Waukesha H24GL/GLD - 11:1 NGAS Manufacturer 2003 630-08-0 CO 238 0.34 0.34 1

153

Table 3.3 Compilation of combustion emission factors for estimating GHG and CAC emissions.

Fact

or

Equ

ipm

ent

Typ

e

Identifier 1 Identifier 2 Identifier 3 Fuel Type

Factor Reference Y

ear CAS

Number Compound Emission

Factor (ng/J) L

ower

U

ncer

tain

ty

Upp

er

Unc

erta

inty

U

ncer

tain

ty

Ref

eren

ce

0228 RECIP Waukesha H24GL/GLD - 11:1 NGAS

U.S. EPA AP-42 -> Profile: 0014 2000 74-82-8 CH4 538 0.59 0.59 1

0228 RECIP Waukesha H24GL/GLD - 11:1 NGAS Manufacturer 2003 CEL0002 NOx 476 0.09 0.09 1

0228 RECIP Waukesha H24GL/GLD - 11:1 NGAS

U.S. EPA AP-42 -> Profile: 0014 2000 CEL0003 TPM 0.0332 0.67 1.50 7

0228 RECIP Waukesha H24GL/GLD - 11:1 NGAS

U.S. EPA AP-42 -> Profile: 0014 2000 CEL0004 PM10 0.0332 0.67 1.50 7

0228 RECIP Waukesha H24GL/GLD - 11:1 NGAS

U.S. EPA AP-42 -> Profile: 0014 2000 CEL0005 PM2.5 0.0332 0.67 1.50 7

0228 RECIP Waukesha H24GL/GLD - 11:1 NGAS Manufacturer 2003 CEL0006 VOC 119 0.27 0.27 1

0228 RECIP Waukesha H24GL/GLD - 11:1 NGAS CH4 + VOC 2003 CEL0007 THC 657 0.48 0.48 1

0229 RECIP Waukesha H24GL/GLD, 11:1 CR

Standard (HS turbo) NGAS

CHEMEX Labs -> Profile: 0014 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0229 RECIP Waukesha H24GL/GLD, 11:1 CR

Standard (HS turbo) NGAS Manufacturer 2003 630-08-0 CO 208 0.34 0.34 1

0229 RECIP Waukesha H24GL/GLD, 11:1 CR

Standard (HS turbo) NGAS Manufacturer 2003 74-82-8 CH4 505 0.59 0.59 1

0229 RECIP Waukesha H24GL/GLD, 11:1 CR

Standard (HS turbo) NGAS Manufacturer 2003 CEL0002 NOx 309 0.09 0.09 1

0229 RECIP Waukesha H24GL/GLD, 11:1 CR

Standard (HS turbo) NGAS

U.S. EPA AP-42 -> Profile: 0014 2000 CEL0003 TPM 0.0332 0.67 1.50 7

0229 RECIP Waukesha H24GL/GLD, 11:1 CR

Standard (HS turbo) NGAS

U.S. EPA AP-42 -> Profile: 0014 2000 CEL0004 PM10 0.0332 0.67 1.50 7

0229 RECIP Waukesha H24GL/GLD, 11:1 CR

Standard (HS turbo) NGAS

U.S. EPA AP-42 -> Profile: 0014 2000 CEL0005 PM2.5 0.0332 0.67 1.50 7

0229 RECIP Waukesha H24GL/GLD, 11:1 CR

Standard (HS turbo) NGAS Manufacturer 2003 CEL0006 VOC 89 0.27 0.27 1

0229 RECIP Waukesha H24GL/GLD, 11:1 CR

Standard (HS turbo) NGAS Manufacturer 2003 CEL0007 THC 594 0.51 0.51 1

0230 RECIP Waukesha H24GL/GLD, 11:1 CR

T.A. Luft Emissions NGAS

CHEMEX Labs -> Profile: 0014 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0230 RECIP Waukesha H24GL/GLD, 11:1 CR

T.A. Luft Emissions NGAS Manufacturer 2003 630-08-0 CO 189 0.34 0.34 1

154

Table 3.3 Compilation of combustion emission factors for estimating GHG and CAC emissions.

Fact

or

Equ

ipm

ent

Typ

e

Identifier 1 Identifier 2 Identifier 3 Fuel Type

Factor Reference Y

ear CAS

Number Compound Emission

Factor (ng/J) L

ower

U

ncer

tain

ty

Upp

er

Unc

erta

inty

U

ncer

tain

ty

Ref

eren

ce

0230 RECIP Waukesha H24GL/GLD, 11:1 CR

T.A. Luft Emissions NGAS Manufacturer 2003 74-82-8 CH4 363 0.59 0.59 1

0230 RECIP Waukesha H24GL/GLD, 11:1 CR

T.A. Luft Emissions NGAS Manufacturer 2003 CEL0002 NOx 149 0.09 0.09 1

0230 RECIP Waukesha H24GL/GLD, 11:1 CR

T.A. Luft Emissions NGAS

U.S. EPA AP-42 -> Profile: 0014 2000 CEL0003 TPM 0.0332 0.67 1.50 7

0230 RECIP Waukesha H24GL/GLD, 11:1 CR

T.A. Luft Emissions NGAS

U.S. EPA AP-42 -> Profile: 0014 2000 CEL0004 PM10 0.0332 0.67 1.50 7

0230 RECIP Waukesha H24GL/GLD, 11:1 CR

T.A. Luft Emissions NGAS

U.S. EPA AP-42 -> Profile: 0014 2000 CEL0005 PM2.5 0.0332 0.67 1.50 7

0230 RECIP Waukesha H24GL/GLD, 11:1 CR

T.A. Luft Emissions NGAS Manufacturer 2003 CEL0006 VOC 54 0.27 0.27 1

0230 RECIP Waukesha H24GL/GLD, 11:1 CR

T.A. Luft Emissions NGAS Manufacturer 2003 CEL0007 THC 416 0.51 0.51 1

0231 RECIP Waukesha H24GSID Catalytic conv. Input (3 way) NGAS

CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0231 RECIP Waukesha H24GSID Catalytic conv. Input (3 way) NGAS Manufacturer 2003 630-08-0 CO 866 0.34 0.34 1

0231 RECIP Waukesha H24GSID Catalytic conv. Input (3 way) NGAS Manufacturer 2003 74-82-8 CH4 135 0.59 0.59 1

0231 RECIP Waukesha H24GSID Catalytic conv. Input (3 way) NGAS Manufacturer 2003 CEL0002 NOx 1732 0.09 0.09 1

0231 RECIP Waukesha H24GSID Catalytic conv. Input (3 way) NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

0231 RECIP Waukesha H24GSID Catalytic conv. Input (3 way) NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

0231 RECIP Waukesha H24GSID Catalytic conv. Input (3 way) NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

0231 RECIP Waukesha H24GSID Catalytic conv. Input (3 way) NGAS Manufacturer 2003 CEL0006 VOC 27 0.27 0.27 1

0231 RECIP Waukesha H24GSID Catalytic conv. Input (3 way) NGAS Manufacturer 2003 CEL0007 THC 162 0.51 0.51 1

0232 RECIP Waukesha L36GL 8:7:1:CR Standard (HS turbo) NGAS

CHEMEX Labs -> Profile: 0014 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0232 RECIP Waukesha L36GL 8:7:1:CR Standard (HS turbo) NGAS Manufacturer 2003 630-08-0 CO 211 0.34 0.34 1

155

Table 3.3 Compilation of combustion emission factors for estimating GHG and CAC emissions.

Fact

or

Equ

ipm

ent

Typ

e

Identifier 1 Identifier 2 Identifier 3 Fuel Type

Factor Reference Y

ear CAS

Number Compound Emission

Factor (ng/J) L

ower

U

ncer

tain

ty

Upp

er

Unc

erta

inty

U

ncer

tain

ty

Ref

eren

ce

0232 RECIP Waukesha L36GL 8:7:1:CR Standard (HS turbo) NGAS Manufacturer 2003 74-82-8 CH4 317 0.59 0.59 1

0232 RECIP Waukesha L36GL 8:7:1:CR Standard (HS turbo) NGAS Manufacturer 2003 CEL0002 NOx 248 0.09 0.09 1

0232 RECIP Waukesha L36GL 8:7:1:CR Standard (HS turbo) NGAS

U.S. EPA AP-42 -> Profile: 0014 2000 CEL0003 TPM 0.0332 0.67 1.50 7

0232 RECIP Waukesha L36GL 8:7:1:CR Standard (HS turbo) NGAS

U.S. EPA AP-42 -> Profile: 0014 2000 CEL0004 PM10 0.0332 0.67 1.50 7

0232 RECIP Waukesha L36GL 8:7:1:CR Standard (HS turbo) NGAS

U.S. EPA AP-42 -> Profile: 0014 2000 CEL0005 PM2.5 0.0332 0.67 1.50 7

0232 RECIP Waukesha L36GL 8:7:1:CR Standard (HS turbo) NGAS Manufacturer 2003 CEL0006 VOC 56 0.27 0.27 1

0232 RECIP Waukesha L36GL 8:7:1:CR Standard (HS turbo) NGAS Manufacturer 2003 CEL0007 THC 372 0.51 0.51 1

0233 RECIP Waukesha L36GL/GLD - 11:1 NGAS CHEMEX Labs -> Profile: 0014 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0233 RECIP Waukesha L36GL/GLD - 11:1 NGAS Manufacturer 2003 630-08-0 CO 248 0.34 0.34 1

0233 RECIP Waukesha L36GL/GLD - 11:1 NGAS U.S. EPA AP-42 -> Profile: 0014 2000 74-82-8 CH4 538 0.59 0.59 1

0233 RECIP Waukesha L36GL/GLD - 11:1 NGAS Manufacturer 2003 CEL0002 NOx 497 0.09 0.09 1

0233 RECIP Waukesha L36GL/GLD - 11:1 NGAS U.S. EPA AP-42 -> Profile: 0014 2000 CEL0003 TPM 0.0332 0.67 1.50 7

0233 RECIP Waukesha L36GL/GLD - 11:1 NGAS U.S. EPA AP-42 -> Profile: 0014 2000 CEL0004 PM10 0.0332 0.67 1.50 7

0233 RECIP Waukesha L36GL/GLD - 11:1 NGAS U.S. EPA AP-42 -> Profile: 0014 2000 CEL0005 PM2.5 0.0332 0.67 1.50 7

0233 RECIP Waukesha L36GL/GLD - 11:1 NGAS Manufacturer 2003 CEL0006 VOC 124 0.27 0.27 1 0233 RECIP Waukesha L36GL/GLD - 11:1 NGAS CH4 + VOC 2003 CEL0007 THC 662 0.48 0.48 1

0234 RECIP Waukesha L36GL/GLD, 11:1 CR

Standard (HS turbo) NGAS

CHEMEX Labs -> Profile: 0014 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0234 RECIP Waukesha L36GL/GLD, 11:1 CR

Standard (HS turbo) NGAS Manufacturer 2003 630-08-0 CO 217 0.34 0.34 1

0234 RECIP Waukesha L36GL/GLD, 11:1 CR

Standard (HS turbo) NGAS Manufacturer 2003 74-82-8 CH4 528 0.59 0.59 1

0234 RECIP Waukesha L36GL/GLD, 11:1 CR

Standard (HS turbo) NGAS Manufacturer 2003 CEL0002 NOx 323 0.09 0.09 1

156

Table 3.3 Compilation of combustion emission factors for estimating GHG and CAC emissions.

Fact

or

Equ

ipm

ent

Typ

e

Identifier 1 Identifier 2 Identifier 3 Fuel Type

Factor Reference Y

ear CAS

Number Compound Emission

Factor (ng/J) L

ower

U

ncer

tain

ty

Upp

er

Unc

erta

inty

U

ncer

tain

ty

Ref

eren

ce

0234 RECIP Waukesha L36GL/GLD, 11:1 CR

Standard (HS turbo) NGAS

U.S. EPA AP-42 -> Profile: 0014 2000 CEL0003 TPM 0.0332 0.67 1.50 7

0234 RECIP Waukesha L36GL/GLD, 11:1 CR

Standard (HS turbo) NGAS

U.S. EPA AP-42 -> Profile: 0014 2000 CEL0004 PM10 0.0332 0.67 1.50 7

0234 RECIP Waukesha L36GL/GLD, 11:1 CR

Standard (HS turbo) NGAS

U.S. EPA AP-42 -> Profile: 0014 2000 CEL0005 PM2.5 0.0332 0.67 1.50 7

0234 RECIP Waukesha L36GL/GLD, 11:1 CR

Standard (HS turbo) NGAS Manufacturer 2003 CEL0006 VOC 93 0.27 0.27 1

0234 RECIP Waukesha L36GL/GLD, 11:1 CR

Standard (HS turbo) NGAS Manufacturer 2003 CEL0007 THC 621 0.51 0.51 1

0235 RECIP Waukesha L36GL/GLD, 11:1 CR

T.A. Luft Emissions NGAS

CHEMEX Labs -> Profile: 0014 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0235 RECIP Waukesha L36GL/GLD, 11:1 CR

T.A. Luft Emissions NGAS Manufacturer 2003 630-08-0 CO 197 0.34 0.34 1

0235 RECIP Waukesha L36GL/GLD, 11:1 CR

T.A. Luft Emissions NGAS Manufacturer 2003 74-82-8 CH4 379 0.59 0.59 1

0235 RECIP Waukesha L36GL/GLD, 11:1 CR

T.A. Luft Emissions NGAS Manufacturer 2003 CEL0002 NOx 155 0.09 0.09 1

0235 RECIP Waukesha L36GL/GLD, 11:1 CR

T.A. Luft Emissions NGAS

U.S. EPA AP-42 -> Profile: 0014 2000 CEL0003 TPM 0.0332 0.67 1.50 7

0235 RECIP Waukesha L36GL/GLD, 11:1 CR

T.A. Luft Emissions NGAS

U.S. EPA AP-42 -> Profile: 0014 2000 CEL0004 PM10 0.0332 0.67 1.50 7

0235 RECIP Waukesha L36GL/GLD, 11:1 CR

T.A. Luft Emissions NGAS

U.S. EPA AP-42 -> Profile: 0014 2000 CEL0005 PM2.5 0.0332 0.67 1.50 7

0235 RECIP Waukesha L36GL/GLD, 11:1 CR

T.A. Luft Emissions NGAS Manufacturer 2003 CEL0006 VOC 56 0.27 0.27 1

0235 RECIP Waukesha L36GL/GLD, 11:1 CR

T.A. Luft Emissions NGAS Manufacturer 2003 CEL0007 THC 434 0.51 0.51 1

0236 RECIP Waukesha L36GLD - 11:1 NGAS CHEMEX Labs -> Profile: 0014 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0236 RECIP Waukesha L36GLD - 11:1 NGAS Manufacturer 2003 630-08-0 CO 233 0.34 0.34 1

0236 RECIP Waukesha L36GLD - 11:1 NGAS U.S. EPA AP-42 -> Profile: 0014 2000 74-82-8 CH4 538 0.59 0.59 1

0236 RECIP Waukesha L36GLD - 11:1 NGAS Manufacturer 2003 CEL0002 NOx 466 0.09 0.09 1

0236 RECIP Waukesha L36GLD - 11:1 NGAS U.S. EPA AP-42 -> Profile: 0014 2000 CEL0003 TPM 0.0332 0.67 1.50 7

157

Table 3.3 Compilation of combustion emission factors for estimating GHG and CAC emissions.

Fact

or

Equ

ipm

ent

Typ

e

Identifier 1 Identifier 2 Identifier 3 Fuel Type

Factor Reference Y

ear CAS

Number Compound Emission

Factor (ng/J) L

ower

U

ncer

tain

ty

Upp

er

Unc

erta

inty

U

ncer

tain

ty

Ref

eren

ce

0236 RECIP Waukesha L36GLD - 11:1 NGAS U.S. EPA AP-42 -> Profile: 0014 2000 CEL0004 PM10 0.0332 0.67 1.50 7

0236 RECIP Waukesha L36GLD - 11:1 NGAS U.S. EPA AP-42 -> Profile: 0014 2000 CEL0005 PM2.5 0.0332 0.67 1.50 7

0236 RECIP Waukesha L36GLD - 11:1 NGAS Manufacturer 2003 CEL0006 VOC 116 0.27 0.27 1 0236 RECIP Waukesha L36GLD - 11:1 NGAS CH4 + VOC 2003 CEL0007 THC 654 0.49 0.49 1

0237 RECIP Waukesha L5108G Catalytic conv. Input (3 way) NGAS

CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0237 RECIP Waukesha L5108G Catalytic conv. Input (3 way) NGAS Manufacturer 2003 630-08-0 CO 1000 0.34 0.34 1

0237 RECIP Waukesha L5108G Catalytic conv. Input (3 way) NGAS Manufacturer 2003 74-82-8 CH4 189 0.59 0.59 1

0237 RECIP Waukesha L5108G Catalytic conv. Input (3 way) NGAS Manufacturer 2003 CEL0002 NOx 1444 0.09 0.09 1

0237 RECIP Waukesha L5108G Catalytic conv. Input (3 way) NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

0237 RECIP Waukesha L5108G Catalytic conv. Input (3 way) NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

0237 RECIP Waukesha L5108G Catalytic conv. Input (3 way) NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

0237 RECIP Waukesha L5108G Catalytic conv. Input (3 way) NGAS Manufacturer 2003 CEL0006 VOC 33 0.27 0.27 1

0237 RECIP Waukesha L5108G Catalytic conv. Input (3 way) NGAS Manufacturer 2003 CEL0007 THC 222 0.51 0.51 1

0238 RECIP Waukesha L5108G Equal NOx & CO NGAS CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0238 RECIP Waukesha L5108G Equal NOx & CO NGAS Manufacturer 2003 630-08-0 CO 1333 0.34 0.34 1 0238 RECIP Waukesha L5108G Equal NOx & CO NGAS Manufacturer 2003 74-82-8 CH4 217 0.59 0.59 1 0238 RECIP Waukesha L5108G Equal NOx & CO NGAS Manufacturer 2003 CEL0002 NOx 1333 0.09 0.09 1

0238 RECIP Waukesha L5108G Equal NOx & CO NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

0238 RECIP Waukesha L5108G Equal NOx & CO NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

0238 RECIP Waukesha L5108G Equal NOx & CO NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

0238 RECIP Waukesha L5108G Equal NOx & CO NGAS Manufacturer 2003 CEL0006 VOC 39 0.27 0.27 1

158

Table 3.3 Compilation of combustion emission factors for estimating GHG and CAC emissions.

Fact

or

Equ

ipm

ent

Typ

e

Identifier 1 Identifier 2 Identifier 3 Fuel Type

Factor Reference Y

ear CAS

Number Compound Emission

Factor (ng/J) L

ower

U

ncer

tain

ty

Upp

er

Unc

erta

inty

U

ncer

tain

ty

Ref

eren

ce

0238 RECIP Waukesha L5108G Equal NOx & CO NGAS Manufacturer 2003 CEL0007 THC 255 0.51 0.51 1

0239 RECIP Waukesha L5108G Lowest Manifold (best power) NGAS

CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0239 RECIP Waukesha L5108G Lowest Manifold (best power) NGAS Manufacturer 2003 630-08-0 CO 3554 0.34 0.34 1

0239 RECIP Waukesha L5108G Lowest Manifold (best power) NGAS Manufacturer 2003 74-82-8 CH4 217 0.59 0.59 1

0239 RECIP Waukesha L5108G Lowest Manifold (best power) NGAS Manufacturer 2003 CEL0002 NOx 1222 0.09 0.09 1

0239 RECIP Waukesha L5108G Lowest Manifold (best power) NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

0239 RECIP Waukesha L5108G Lowest Manifold (best power) NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

0239 RECIP Waukesha L5108G Lowest Manifold (best power) NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

0239 RECIP Waukesha L5108G Lowest Manifold (best power) NGAS Manufacturer 2003 CEL0006 VOC 39 0.27 0.27 1

0239 RECIP Waukesha L5108G Lowest Manifold (best power) NGAS Manufacturer 2003 CEL0007 THC 255 0.51 0.51 1

0240 RECIP Waukesha L5108G Standard (best economy) NGAS

CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0240 RECIP Waukesha L5108G Standard (best economy) NGAS Manufacturer 2003 630-08-0 CO 167 0.34 0.34 1

0240 RECIP Waukesha L5108G Standard (best economy) NGAS Manufacturer 2003 74-82-8 CH4 139 0.59 0.59 1

0240 RECIP Waukesha L5108G Standard (best economy) NGAS Manufacturer 2003 CEL0002 NOx 2444 0.09 0.09 1

0240 RECIP Waukesha L5108G Standard (best economy) NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

0240 RECIP Waukesha L5108G Standard (best economy) NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

0240 RECIP Waukesha L5108G Standard (best economy) NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

0240 RECIP Waukesha L5108G Standard (best economy) NGAS Manufacturer 2003 CEL0006 VOC 28 0.27 0.27 1

0240 RECIP Waukesha L5108G Standard (best NGAS Manufacturer 2003 CEL0007 THC 167 0.51 0.51 1

159

Table 3.3 Compilation of combustion emission factors for estimating GHG and CAC emissions.

Fact

or

Equ

ipm

ent

Typ

e

Identifier 1 Identifier 2 Identifier 3 Fuel Type

Factor Reference Y

ear CAS

Number Compound Emission

Factor (ng/J) L

ower

U

ncer

tain

ty

Upp

er

Unc

erta

inty

U

ncer

tain

ty

Ref

eren

ce

economy)

0241 RECIP Waukesha L5108G - 10:1 NGAS CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0241 RECIP Waukesha L5108G - 10:1 NGAS Manufacturer 2003 630-08-0 CO 111 0.34 0.34 1

0241 RECIP Waukesha L5108G - 10:1 NGAS U.S. EPA AP-42 -> Profile: 0016 2000 74-82-8 CH4 99 0.59 0.59 1

0241 RECIP Waukesha L5108G - 10:1 NGAS Manufacturer 2003 CEL0002 NOx 1999 0.09 0.09 1

0241 RECIP Waukesha L5108G - 10:1 NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

0241 RECIP Waukesha L5108G - 10:1 NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

0241 RECIP Waukesha L5108G - 10:1 NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

0241 RECIP Waukesha L5108G - 10:1 NGAS Manufacturer 2003 CEL0006 VOC 22 0.27 0.27 1 0241 RECIP Waukesha L5108G - 10:1 NGAS CH4 + VOC 2003 CEL0007 THC 121 0.48 0.48 1

0242 RECIP Waukesha L5108G - 8.2:1 NGAS CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0242 RECIP Waukesha L5108G - 8.2:1 NGAS Manufacturer 2003 630-08-0 CO 106 0.34 0.34 1

0242 RECIP Waukesha L5108G - 8.2:1 NGAS U.S. EPA AP-42 -> Profile: 0016 2000 74-82-8 CH4 99 0.59 0.59 1

0242 RECIP Waukesha L5108G - 8.2:1 NGAS Manufacturer 2003 CEL0002 NOx 1899 0.09 0.09 1

0242 RECIP Waukesha L5108G - 8.2:1 NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

0242 RECIP Waukesha L5108G - 8.2:1 NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

0242 RECIP Waukesha L5108G - 8.2:1 NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

0242 RECIP Waukesha L5108G - 8.2:1 NGAS Manufacturer 2003 CEL0006 VOC 21 0.27 0.27 1 0242 RECIP Waukesha L5108G - 8.2:1 NGAS CH4 + VOC 2003 CEL0007 THC 120 0.49 0.49 1

0243 RECIP Waukesha L5108GL - 10.5:1 NGAS CHEMEX Labs -> Profile: 0014 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0243 RECIP Waukesha L5108GL - 10.5:1 NGAS Manufacturer 2003 630-08-0 CO 306 0.34 0.34 1 0243 RECIP Waukesha L5108GL - 10.5:1 NGAS Manufacturer 2003 74-82-8 CH4 520 0.59 0.59 1 0243 RECIP Waukesha L5108GL - 10.5:1 NGAS Manufacturer 2003 CEL0002 NOx 173 0.09 0.09 1

0243 RECIP Waukesha L5108GL - 10.5:1 NGAS U.S. EPA AP-42 -> Profile: 0014 2000 CEL0003 TPM 0.0332 0.67 1.50 7

160

Table 3.3 Compilation of combustion emission factors for estimating GHG and CAC emissions.

Fact

or

Equ

ipm

ent

Typ

e

Identifier 1 Identifier 2 Identifier 3 Fuel Type

Factor Reference Y

ear CAS

Number Compound Emission

Factor (ng/J) L

ower

U

ncer

tain

ty

Upp

er

Unc

erta

inty

U

ncer

tain

ty

Ref

eren

ce

0243 RECIP Waukesha L5108GL - 10.5:1 NGAS U.S. EPA AP-42 -> Profile: 0014 2000 CEL0004 PM10 0.0332 0.67 1.50 7

0243 RECIP Waukesha L5108GL - 10.5:1 NGAS U.S. EPA AP-42 -> Profile: 0014 2000 CEL0005 PM2.5 0.0332 0.67 1.50 7

0243 RECIP Waukesha L5108GL - 10.5:1 NGAS Manufacturer 2003 CEL0006 VOC 116 0.27 0.27 1 0243 RECIP Waukesha L5108GL - 10.5:1 NGAS Manufacturer 2003 CEL0007 THC 636 0.51 0.51 1

0244 RECIP Waukesha L5108GSI Catalytic conv. Input (3 way) NGAS

CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0244 RECIP Waukesha L5108GSI Catalytic conv. Input (3 way) NGAS Manufacturer 2003 630-08-0 CO 1000 0.34 0.34 1

0244 RECIP Waukesha L5108GSI Catalytic conv. Input (3 way) NGAS Manufacturer 2003 74-82-8 CH4 189 0.59 0.59 1

0244 RECIP Waukesha L5108GSI Catalytic conv. Input (3 way) NGAS Manufacturer 2003 CEL0002 NOx 1444 0.09 0.09 1

0244 RECIP Waukesha L5108GSI Catalytic conv. Input (3 way) NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

0244 RECIP Waukesha L5108GSI Catalytic conv. Input (3 way) NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

0244 RECIP Waukesha L5108GSI Catalytic conv. Input (3 way) NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

0244 RECIP Waukesha L5108GSI Catalytic conv. Input (3 way) NGAS Manufacturer 2003 CEL0006 VOC 33 0.27 0.27 1

0244 RECIP Waukesha L5108GSI Catalytic conv. Input (3 way) NGAS Manufacturer 2003 CEL0007 THC 222 0.51 0.51 1

0245 RECIP Waukesha L5108GSI Equal NOx & CO NGAS CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0245 RECIP Waukesha L5108GSI Equal NOx & CO NGAS Manufacturer 2003 630-08-0 CO 1333 0.34 0.34 1 0245 RECIP Waukesha L5108GSI Equal NOx & CO NGAS Manufacturer 2003 74-82-8 CH4 217 0.59 0.59 1 0245 RECIP Waukesha L5108GSI Equal NOx & CO NGAS Manufacturer 2003 CEL0002 NOx 1333 0.09 0.09 1

0245 RECIP Waukesha L5108GSI Equal NOx & CO NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

0245 RECIP Waukesha L5108GSI Equal NOx & CO NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

0245 RECIP Waukesha L5108GSI Equal NOx & CO NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

0245 RECIP Waukesha L5108GSI Equal NOx & CO NGAS Manufacturer 2003 CEL0006 VOC 39 0.27 0.27 1

161

Table 3.3 Compilation of combustion emission factors for estimating GHG and CAC emissions.

Fact

or

Equ

ipm

ent

Typ

e

Identifier 1 Identifier 2 Identifier 3 Fuel Type

Factor Reference Y

ear CAS

Number Compound Emission

Factor (ng/J) L

ower

U

ncer

tain

ty

Upp

er

Unc

erta

inty

U

ncer

tain

ty

Ref

eren

ce

0245 RECIP Waukesha L5108GSI Equal NOx & CO NGAS Manufacturer 2003 CEL0007 THC 255 0.51 0.51 1

0246 RECIP Waukesha L5108GSI Lowest Manifold (best power) NGAS

CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0246 RECIP Waukesha L5108GSI Lowest Manifold (best power) NGAS Manufacturer 2003 630-08-0 CO 3554 0.34 0.34 1

0246 RECIP Waukesha L5108GSI Lowest Manifold (best power) NGAS Manufacturer 2003 74-82-8 CH4 217 0.59 0.59 1

0246 RECIP Waukesha L5108GSI Lowest Manifold (best power) NGAS Manufacturer 2003 CEL0002 NOx 1222 0.09 0.09 1

0246 RECIP Waukesha L5108GSI Lowest Manifold (best power) NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

0246 RECIP Waukesha L5108GSI Lowest Manifold (best power) NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

0246 RECIP Waukesha L5108GSI Lowest Manifold (best power) NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

0246 RECIP Waukesha L5108GSI Lowest Manifold (best power) NGAS Manufacturer 2003 CEL0006 VOC 39 0.27 0.27 1

0246 RECIP Waukesha L5108GSI Lowest Manifold (best power) NGAS Manufacturer 2003 CEL0007 THC 255 0.51 0.51 1

0247 RECIP Waukesha L5108GSI Standard (best economy) NGAS

CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0247 RECIP Waukesha L5108GSI Standard (best economy) NGAS Manufacturer 2003 630-08-0 CO 167 0.34 0.34 1

0247 RECIP Waukesha L5108GSI Standard (best economy) NGAS Manufacturer 2003 74-82-8 CH4 139 0.59 0.59 1

0247 RECIP Waukesha L5108GSI Standard (best economy) NGAS Manufacturer 2003 CEL0002 NOx 2444 0.09 0.09 1

0247 RECIP Waukesha L5108GSI Standard (best economy) NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

0247 RECIP Waukesha L5108GSI Standard (best economy) NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

0247 RECIP Waukesha L5108GSI Standard (best economy) NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

0247 RECIP Waukesha L5108GSI Standard (best economy) NGAS Manufacturer 2003 CEL0006 VOC 28 0.27 0.27 1

0247 RECIP Waukesha L5108GSI Standard (best NGAS Manufacturer 2003 CEL0007 THC 167 0.51 0.51 1

162

Table 3.3 Compilation of combustion emission factors for estimating GHG and CAC emissions.

Fact

or

Equ

ipm

ent

Typ

e

Identifier 1 Identifier 2 Identifier 3 Fuel Type

Factor Reference Y

ear CAS

Number Compound Emission

Factor (ng/J) L

ower

U

ncer

tain

ty

Upp

er

Unc

erta

inty

U

ncer

tain

ty

Ref

eren

ce

economy)

0248 RECIP Waukesha L5108GSI - 8.2:1 NGAS CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0248 RECIP Waukesha L5108GSI - 8.2:1 NGAS Manufacturer 2003 630-08-0 CO 111 0.34 0.34 1

0248 RECIP Waukesha L5108GSI - 8.2:1 NGAS U.S. EPA AP-42 -> Profile: 0016 2000 74-82-8 CH4 99 0.59 0.59 1

0248 RECIP Waukesha L5108GSI - 8.2:1 NGAS Manufacturer 2003 CEL0002 NOx 1999 0.09 0.09 1

0248 RECIP Waukesha L5108GSI - 8.2:1 NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

0248 RECIP Waukesha L5108GSI - 8.2:1 NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

0248 RECIP Waukesha L5108GSI - 8.2:1 NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

0248 RECIP Waukesha L5108GSI - 8.2:1 NGAS Manufacturer 2003 CEL0006 VOC 22 0.27 0.27 1 0248 RECIP Waukesha L5108GSI - 8.2:1 NGAS CH4 + VOC 2003 CEL0007 THC 121 0.48 0.48 1

0249 RECIP Waukesha L5774LT Standard NGAS CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0249 RECIP Waukesha L5774LT Standard NGAS Manufacturer 2003 630-08-0 CO 232 0.34 0.34 1 0249 RECIP Waukesha L5774LT Standard NGAS Manufacturer 2003 74-82-8 CH4 395 0.59 0.59 1 0249 RECIP Waukesha L5774LT Standard NGAS Manufacturer 2003 CEL0002 NOx 302 0.09 0.09 1

0249 RECIP Waukesha L5774LT Standard NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

0249 RECIP Waukesha L5774LT Standard NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

0249 RECIP Waukesha L5774LT Standard NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

0249 RECIP Waukesha L5774LT Standard NGAS Manufacturer 2003 CEL0006 VOC 70 0.27 0.27 1 0249 RECIP Waukesha L5774LT Standard NGAS Manufacturer 2003 CEL0007 THC 464 0.51 0.51 1

0250 RECIP Waukesha L5790G Catalytic conv. Input (3 way) NGAS

CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0250 RECIP Waukesha L5790G Catalytic conv. Input (3 way) NGAS Manufacturer 2003 630-08-0 CO 1000 0.34 0.34 1

0250 RECIP Waukesha L5790G Catalytic conv. Input (3 way) NGAS Manufacturer 2003 74-82-8 CH4 189 0.59 0.59 1

0250 RECIP Waukesha L5790G Catalytic conv. Input (3 way) NGAS Manufacturer 2003 CEL0002 NOx 1444 0.09 0.09 1

163

Table 3.3 Compilation of combustion emission factors for estimating GHG and CAC emissions.

Fact

or

Equ

ipm

ent

Typ

e

Identifier 1 Identifier 2 Identifier 3 Fuel Type

Factor Reference Y

ear CAS

Number Compound Emission

Factor (ng/J) L

ower

U

ncer

tain

ty

Upp

er

Unc

erta

inty

U

ncer

tain

ty

Ref

eren

ce

0250 RECIP Waukesha L5790G Catalytic conv. Input (3 way) NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

0250 RECIP Waukesha L5790G Catalytic conv. Input (3 way) NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

0250 RECIP Waukesha L5790G Catalytic conv. Input (3 way) NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

0250 RECIP Waukesha L5790G Catalytic conv. Input (3 way) NGAS Manufacturer 2003 CEL0006 VOC 33 0.27 0.27 1

0250 RECIP Waukesha L5790G Catalytic conv. Input (3 way) NGAS Manufacturer 2003 CEL0007 THC 222 0.51 0.51 1

0251 RECIP Waukesha L5790G Equal NOx & CO NGAS CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0251 RECIP Waukesha L5790G Equal NOx & CO NGAS Manufacturer 2003 630-08-0 CO 1333 0.34 0.34 1 0251 RECIP Waukesha L5790G Equal NOx & CO NGAS Manufacturer 2003 74-82-8 CH4 217 0.59 0.59 1 0251 RECIP Waukesha L5790G Equal NOx & CO NGAS Manufacturer 2003 CEL0002 NOx 1333 0.09 0.09 1

0251 RECIP Waukesha L5790G Equal NOx & CO NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

0251 RECIP Waukesha L5790G Equal NOx & CO NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

0251 RECIP Waukesha L5790G Equal NOx & CO NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

0251 RECIP Waukesha L5790G Equal NOx & CO NGAS Manufacturer 2003 CEL0006 VOC 39 0.27 0.27 1 0251 RECIP Waukesha L5790G Equal NOx & CO NGAS Manufacturer 2003 CEL0007 THC 255 0.51 0.51 1

0252 RECIP Waukesha L5790G Lowest Manifold (best power) NGAS

CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0252 RECIP Waukesha L5790G Lowest Manifold (best power) NGAS Manufacturer 2003 630-08-0 CO 3554 0.34 0.34 1

0252 RECIP Waukesha L5790G Lowest Manifold (best power) NGAS Manufacturer 2003 74-82-8 CH4 217 0.59 0.59 1

0252 RECIP Waukesha L5790G Lowest Manifold (best power) NGAS Manufacturer 2003 CEL0002 NOx 1222 0.09 0.09 1

0252 RECIP Waukesha L5790G Lowest Manifold (best power) NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

0252 RECIP Waukesha L5790G Lowest Manifold (best power) NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

0252 RECIP Waukesha L5790G Lowest Manifold NGAS U.S. EPA AP-42 - 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

164

Table 3.3 Compilation of combustion emission factors for estimating GHG and CAC emissions.

Fact

or

Equ

ipm

ent

Typ

e

Identifier 1 Identifier 2 Identifier 3 Fuel Type

Factor Reference Y

ear CAS

Number Compound Emission

Factor (ng/J) L

ower

U

ncer

tain

ty

Upp

er

Unc

erta

inty

U

ncer

tain

ty

Ref

eren

ce

(best power) > Profile: 0016

0252 RECIP Waukesha L5790G Lowest Manifold (best power) NGAS Manufacturer 2003 CEL0006 VOC 39 0.27 0.27 1

0252 RECIP Waukesha L5790G Lowest Manifold (best power) NGAS Manufacturer 2003 CEL0007 THC 255 0.51 0.51 1

0253 RECIP Waukesha L5790G Standard (best economy) NGAS

CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0253 RECIP Waukesha L5790G Standard (best economy) NGAS Manufacturer 2003 630-08-0 CO 167 0.34 0.34 1

0253 RECIP Waukesha L5790G Standard (best economy) NGAS Manufacturer 2003 74-82-8 CH4 139 0.59 0.59 1

0253 RECIP Waukesha L5790G Standard (best economy) NGAS Manufacturer 2003 CEL0002 NOx 2444 0.09 0.09 1

0253 RECIP Waukesha L5790G Standard (best economy) NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

0253 RECIP Waukesha L5790G Standard (best economy) NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

0253 RECIP Waukesha L5790G Standard (best economy) NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

0253 RECIP Waukesha L5790G Standard (best economy) NGAS Manufacturer 2003 CEL0006 VOC 28 0.27 0.27 1

0253 RECIP Waukesha L5790G Standard (best economy) NGAS Manufacturer 2003 CEL0007 THC 167 0.51 0.51 1

0254 RECIP Waukesha L5790G - 10:1 NGAS CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0254 RECIP Waukesha L5790G - 10:1 NGAS Manufacturer 2003 630-08-0 CO 111 0.34 0.34 1

0254 RECIP Waukesha L5790G - 10:1 NGAS U.S. EPA AP-42 -> Profile: 0016 2000 74-82-8 CH4 99 0.59 0.59 1

0254 RECIP Waukesha L5790G - 10:1 NGAS Manufacturer 2003 CEL0002 NOx 1999 0.09 0.09 1

0254 RECIP Waukesha L5790G - 10:1 NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

0254 RECIP Waukesha L5790G - 10:1 NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

0254 RECIP Waukesha L5790G - 10:1 NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

0254 RECIP Waukesha L5790G - 10:1 NGAS Manufacturer 2003 CEL0006 VOC 22 0.27 0.27 1

165

Table 3.3 Compilation of combustion emission factors for estimating GHG and CAC emissions.

Fact

or

Equ

ipm

ent

Typ

e

Identifier 1 Identifier 2 Identifier 3 Fuel Type

Factor Reference Y

ear CAS

Number Compound Emission

Factor (ng/J) L

ower

U

ncer

tain

ty

Upp

er

Unc

erta

inty

U

ncer

tain

ty

Ref

eren

ce

0254 RECIP Waukesha L5790G - 10:1 NGAS CH4 + VOC 2003 CEL0007 THC 121 0.48 0.48 1

0255 RECIP Waukesha L5790GL - 10.5:1 NGAS CHEMEX Labs -> Profile: 0014 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0255 RECIP Waukesha L5790GL - 10.5:1 NGAS Manufacturer 2003 630-08-0 CO 306 0.34 0.34 1 0255 RECIP Waukesha L5790GL - 10.5:1 NGAS Manufacturer 2003 74-82-8 CH4 520 0.59 0.59 1 0255 RECIP Waukesha L5790GL - 10.5:1 NGAS Manufacturer 2003 CEL0002 NOx 173 0.09 0.09 1

0255 RECIP Waukesha L5790GL - 10.5:1 NGAS U.S. EPA AP-42 -> Profile: 0014 2000 CEL0003 TPM 0.0332 0.67 1.50 7

0255 RECIP Waukesha L5790GL - 10.5:1 NGAS U.S. EPA AP-42 -> Profile: 0014 2000 CEL0004 PM10 0.0332 0.67 1.50 7

0255 RECIP Waukesha L5790GL - 10.5:1 NGAS U.S. EPA AP-42 -> Profile: 0014 2000 CEL0005 PM2.5 0.0332 0.67 1.50 7

0255 RECIP Waukesha L5790GL - 10.5:1 NGAS Manufacturer 2003 CEL0006 VOC 116 0.27 0.27 1 0255 RECIP Waukesha L5790GL - 10.5:1 NGAS Manufacturer 2003 CEL0007 THC 636 0.51 0.51 1

0256 RECIP Waukesha L5790GSI Catalytic conv. Input (3 way) NGAS

CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0256 RECIP Waukesha L5790GSI Catalytic conv. Input (3 way) NGAS Manufacturer 2003 630-08-0 CO 974 0.34 0.34 1

0256 RECIP Waukesha L5790GSI Catalytic conv. Input (3 way) NGAS Manufacturer 2003 74-82-8 CH4 184 0.59 0.59 1

0256 RECIP Waukesha L5790GSI Catalytic conv. Input (3 way) NGAS Manufacturer 2003 CEL0002 NOx 1407 0.09 0.09 1

0256 RECIP Waukesha L5790GSI Catalytic conv. Input (3 way) NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

0256 RECIP Waukesha L5790GSI Catalytic conv. Input (3 way) NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

0256 RECIP Waukesha L5790GSI Catalytic conv. Input (3 way) NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

0256 RECIP Waukesha L5790GSI Catalytic conv. Input (3 way) NGAS Manufacturer 2003 CEL0006 VOC 32 0.27 0.27 1

0256 RECIP Waukesha L5790GSI Catalytic conv. Input (3 way) NGAS Manufacturer 2003 CEL0007 THC 216 0.51 0.51 1

0257 RECIP Waukesha L5790GSI Equal NOx & CO NGAS CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0257 RECIP Waukesha L5790GSI Equal NOx & CO NGAS Manufacturer 2003 630-08-0 CO 1299 0.34 0.34 1 0257 RECIP Waukesha L5790GSI Equal NOx & CO NGAS Manufacturer 2003 74-82-8 CH4 211 0.59 0.59 1

166

Table 3.3 Compilation of combustion emission factors for estimating GHG and CAC emissions.

Fact

or

Equ

ipm

ent

Typ

e

Identifier 1 Identifier 2 Identifier 3 Fuel Type

Factor Reference Y

ear CAS

Number Compound Emission

Factor (ng/J) L

ower

U

ncer

tain

ty

Upp

er

Unc

erta

inty

U

ncer

tain

ty

Ref

eren

ce

0257 RECIP Waukesha L5790GSI Equal NOx & CO NGAS Manufacturer 2003 CEL0002 NOx 1299 0.09 0.09 1

0257 RECIP Waukesha L5790GSI Equal NOx & CO NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

0257 RECIP Waukesha L5790GSI Equal NOx & CO NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

0257 RECIP Waukesha L5790GSI Equal NOx & CO NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

0257 RECIP Waukesha L5790GSI Equal NOx & CO NGAS Manufacturer 2003 CEL0006 VOC 38 0.27 0.27 1 0257 RECIP Waukesha L5790GSI Equal NOx & CO NGAS Manufacturer 2003 CEL0007 THC 249 0.51 0.51 1

0258 RECIP Waukesha L5790GSI Lowest Manifold (best power) NGAS

CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0258 RECIP Waukesha L5790GSI Lowest Manifold (best power) NGAS Manufacturer 2003 630-08-0 CO 3463 0.34 0.34 1

0258 RECIP Waukesha L5790GSI Lowest Manifold (best power) NGAS Manufacturer 2003 74-82-8 CH4 211 0.59 0.59 1

0258 RECIP Waukesha L5790GSI Lowest Manifold (best power) NGAS Manufacturer 2003 CEL0002 NOx 1190 0.09 0.09 1

0258 RECIP Waukesha L5790GSI Lowest Manifold (best power) NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

0258 RECIP Waukesha L5790GSI Lowest Manifold (best power) NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

0258 RECIP Waukesha L5790GSI Lowest Manifold (best power) NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

0258 RECIP Waukesha L5790GSI Lowest Manifold (best power) NGAS Manufacturer 2003 CEL0006 VOC 38 0.27 0.27 1

0258 RECIP Waukesha L5790GSI Lowest Manifold (best power) NGAS Manufacturer 2003 CEL0007 THC 249 0.51 0.51 1

0259 RECIP Waukesha L5790GSI Standard (best economy) NGAS

CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0259 RECIP Waukesha L5790GSI Standard (best economy) NGAS Manufacturer 2003 630-08-0 CO 162 0.34 0.34 1

0259 RECIP Waukesha L5790GSI Standard (best economy) NGAS Manufacturer 2003 74-82-8 CH4 135 0.59 0.59 1

0259 RECIP Waukesha L5790GSI Standard (best economy) NGAS Manufacturer 2003 CEL0002 NOx 2381 0.09 0.09 1

0259 RECIP Waukesha L5790GSI Standard (best NGAS U.S. EPA AP-42 - 2000 CEL0003 TPM 4.09 0.50 2.00 8

167

Table 3.3 Compilation of combustion emission factors for estimating GHG and CAC emissions.

Fact

or

Equ

ipm

ent

Typ

e

Identifier 1 Identifier 2 Identifier 3 Fuel Type

Factor Reference Y

ear CAS

Number Compound Emission

Factor (ng/J) L

ower

U

ncer

tain

ty

Upp

er

Unc

erta

inty

U

ncer

tain

ty

Ref

eren

ce

economy) > Profile: 0016

0259 RECIP Waukesha L5790GSI Standard (best economy) NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

0259 RECIP Waukesha L5790GSI Standard (best economy) NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

0259 RECIP Waukesha L5790GSI Standard (best economy) NGAS Manufacturer 2003 CEL0006 VOC 27 0.27 0.27 1

0259 RECIP Waukesha L5790GSI Standard (best economy) NGAS Manufacturer 2003 CEL0007 THC 162 0.51 0.51 1

0260 RECIP Waukesha L5790GSI - 10:1 NGAS CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0260 RECIP Waukesha L5790GSI - 10:1 NGAS Manufacturer 2003 630-08-0 CO 108 0.34 0.34 1

0260 RECIP Waukesha L5790GSI - 10:1 NGAS U.S. EPA AP-42 -> Profile: 0016 2000 74-82-8 CH4 99 0.59 0.59 1

0260 RECIP Waukesha L5790GSI - 10:1 NGAS Manufacturer 2003 CEL0002 NOx 1948 0.09 0.09 1

0260 RECIP Waukesha L5790GSI - 10:1 NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

0260 RECIP Waukesha L5790GSI - 10:1 NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

0260 RECIP Waukesha L5790GSI - 10:1 NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

0260 RECIP Waukesha L5790GSI - 10:1 NGAS Manufacturer 2003 CEL0006 VOC 22 0.27 0.27 1 0260 RECIP Waukesha L5790GSI - 10:1 NGAS CH4 + VOC 2003 CEL0007 THC 121 0.48 0.48 1

0261 RECIP Waukesha L5790GSI - 8.2:1 NGAS CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0261 RECIP Waukesha L5790GSI - 8.2:1 NGAS Manufacturer 2003 630-08-0 CO 108 0.34 0.34 1

0261 RECIP Waukesha L5790GSI - 8.2:1 NGAS U.S. EPA AP-42 -> Profile: 0016 2000 74-82-8 CH4 99 0.59 0.59 1

0261 RECIP Waukesha L5790GSI - 8.2:1 NGAS Manufacturer 2003 CEL0002 NOx 1948 0.09 0.09 1

0261 RECIP Waukesha L5790GSI - 8.2:1 NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

0261 RECIP Waukesha L5790GSI - 8.2:1 NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

0261 RECIP Waukesha L5790GSI - 8.2:1 NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

0261 RECIP Waukesha L5790GSI - 8.2:1 NGAS Manufacturer 2003 CEL0006 VOC 22 0.27 0.27 1

168

Table 3.3 Compilation of combustion emission factors for estimating GHG and CAC emissions.

Fact

or

Equ

ipm

ent

Typ

e

Identifier 1 Identifier 2 Identifier 3 Fuel Type

Factor Reference Y

ear CAS

Number Compound Emission

Factor (ng/J) L

ower

U

ncer

tain

ty

Upp

er

Unc

erta

inty

U

ncer

tain

ty

Ref

eren

ce

0261 RECIP Waukesha L5790GSI - 8.2:1 NGAS CH4 + VOC 2003 CEL0007 THC 121 0.48 0.48 1

0262 RECIP Waukesha L5794GSI Catalytic conv. Input (3 way) NGAS

CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0262 RECIP Waukesha L5794GSI Catalytic conv. Input (3 way) NGAS Manufacturer 2003 630-08-0 CO 1262 0.34 0.34 1

0262 RECIP Waukesha L5794GSI Catalytic conv. Input (3 way) NGAS Manufacturer 2003 74-82-8 CH4 281 0.59 0.59 1

0262 RECIP Waukesha L5794GSI Catalytic conv. Input (3 way) NGAS Manufacturer 2003 CEL0002 NOx 1663 0.09 0.09 1

0262 RECIP Waukesha L5794GSI Catalytic conv. Input (3 way) NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

0262 RECIP Waukesha L5794GSI Catalytic conv. Input (3 way) NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

0262 RECIP Waukesha L5794GSI Catalytic conv. Input (3 way) NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

0262 RECIP Waukesha L5794GSI Catalytic conv. Input (3 way) NGAS Manufacturer 2003 CEL0006 VOC 52 0.27 0.27 1

0262 RECIP Waukesha L5794GSI Catalytic conv. Input (3 way) NGAS Manufacturer 2003 CEL0007 THC 333 0.51 0.51 1

0263 RECIP Waukesha L5794GSI Equal NOx & CO NGAS CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0263 RECIP Waukesha L5794GSI Equal NOx & CO NGAS Manufacturer 2003 630-08-0 CO 1548 0.34 0.34 1 0263 RECIP Waukesha L5794GSI Equal NOx & CO NGAS Manufacturer 2003 74-82-8 CH4 292 0.59 0.59 1 0263 RECIP Waukesha L5794GSI Equal NOx & CO NGAS Manufacturer 2003 CEL0002 NOx 1548 0.09 0.09 1

0263 RECIP Waukesha L5794GSI Equal NOx & CO NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

0263 RECIP Waukesha L5794GSI Equal NOx & CO NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

0263 RECIP Waukesha L5794GSI Equal NOx & CO NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

0263 RECIP Waukesha L5794GSI Equal NOx & CO NGAS Manufacturer 2003 CEL0006 VOC 52 0.27 0.27 1 0263 RECIP Waukesha L5794GSI Equal NOx & CO NGAS Manufacturer 2003 CEL0007 THC 344 0.51 0.51 1

0264 RECIP Waukesha L5794GSI Standard (best economy) NGAS

CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0264 RECIP Waukesha L5794GSI Standard (best economy) NGAS Manufacturer 2003 630-08-0 CO 344 0.34 0.34 1

169

Table 3.3 Compilation of combustion emission factors for estimating GHG and CAC emissions.

Fact

or

Equ

ipm

ent

Typ

e

Identifier 1 Identifier 2 Identifier 3 Fuel Type

Factor Reference Y

ear CAS

Number Compound Emission

Factor (ng/J) L

ower

U

ncer

tain

ty

Upp

er

Unc

erta

inty

U

ncer

tain

ty

Ref

eren

ce

0264 RECIP Waukesha L5794GSI Standard (best economy) NGAS Manufacturer 2003 74-82-8 CH4 235 0.59 0.59 1

0264 RECIP Waukesha L5794GSI Standard (best economy) NGAS Manufacturer 2003 CEL0002 NOx 2523 0.09 0.09 1

0264 RECIP Waukesha L5794GSI Standard (best economy) NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

0264 RECIP Waukesha L5794GSI Standard (best economy) NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

0264 RECIP Waukesha L5794GSI Standard (best economy) NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

0264 RECIP Waukesha L5794GSI Standard (best economy) NGAS Manufacturer 2003 CEL0006 VOC 40 0.27 0.27 1

0264 RECIP Waukesha L5794GSI Standard (best economy) NGAS Manufacturer 2003 CEL0007 THC 275 0.51 0.51 1

0265 RECIP Waukesha L5794LT Standard NGAS CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0265 RECIP Waukesha L5794LT Standard NGAS Manufacturer 2003 630-08-0 CO 238 0.34 0.34 1 0265 RECIP Waukesha L5794LT Standard NGAS Manufacturer 2003 74-82-8 CH4 405 0.59 0.59 1 0265 RECIP Waukesha L5794LT Standard NGAS Manufacturer 2003 CEL0002 NOx 310 0.09 0.09 1

0265 RECIP Waukesha L5794LT Standard NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

0265 RECIP Waukesha L5794LT Standard NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

0265 RECIP Waukesha L5794LT Standard NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

0265 RECIP Waukesha L5794LT Standard NGAS Manufacturer 2003 CEL0006 VOC 72 0.27 0.27 1 0265 RECIP Waukesha L5794LT Standard NGAS Manufacturer 2003 CEL0007 THC 477 0.51 0.51 1

0266 RECIP Waukesha L7042G Catalytic conv. Input (3 way) NGAS

CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0266 RECIP Waukesha L7042G Catalytic conv. Input (3 way) NGAS Manufacturer 2003 630-08-0 CO 1013 0.34 0.34 1

0266 RECIP Waukesha L7042G Catalytic conv. Input (3 way) NGAS Manufacturer 2003 74-82-8 CH4 191 0.59 0.59 1

0266 RECIP Waukesha L7042G Catalytic conv. Input (3 way) NGAS Manufacturer 2003 CEL0002 NOx 1463 0.09 0.09 1

0266 RECIP Waukesha L7042G Catalytic conv. NGAS U.S. EPA AP-42 - 2000 CEL0003 TPM 4.09 0.50 2.00 8

170

Table 3.3 Compilation of combustion emission factors for estimating GHG and CAC emissions.

Fact

or

Equ

ipm

ent

Typ

e

Identifier 1 Identifier 2 Identifier 3 Fuel Type

Factor Reference Y

ear CAS

Number Compound Emission

Factor (ng/J) L

ower

U

ncer

tain

ty

Upp

er

Unc

erta

inty

U

ncer

tain

ty

Ref

eren

ce

Input (3 way) > Profile: 0016

0266 RECIP Waukesha L7042G Catalytic conv. Input (3 way) NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

0266 RECIP Waukesha L7042G Catalytic conv. Input (3 way) NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

0266 RECIP Waukesha L7042G Catalytic conv. Input (3 way) NGAS Manufacturer 2003 CEL0006 VOC 34 0.27 0.27 1

0266 RECIP Waukesha L7042G Catalytic conv. Input (3 way) NGAS Manufacturer 2003 CEL0007 THC 225 0.51 0.51 1

0267 RECIP Waukesha L7042G Equal NOx & CO NGAS CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0267 RECIP Waukesha L7042G Equal NOx & CO NGAS Manufacturer 2003 630-08-0 CO 1351 0.34 0.34 1 0267 RECIP Waukesha L7042G Equal NOx & CO NGAS Manufacturer 2003 74-82-8 CH4 219 0.59 0.59 1 0267 RECIP Waukesha L7042G Equal NOx & CO NGAS Manufacturer 2003 CEL0002 NOx 1351 0.09 0.09 1

0267 RECIP Waukesha L7042G Equal NOx & CO NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

0267 RECIP Waukesha L7042G Equal NOx & CO NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

0267 RECIP Waukesha L7042G Equal NOx & CO NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

0267 RECIP Waukesha L7042G Equal NOx & CO NGAS Manufacturer 2003 CEL0006 VOC 39 0.27 0.27 1 0267 RECIP Waukesha L7042G Equal NOx & CO NGAS Manufacturer 2003 CEL0007 THC 259 0.51 0.51 1

0268 RECIP Waukesha L7042G Lowest Manifold (best power) NGAS

CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0268 RECIP Waukesha L7042G Lowest Manifold (best power) NGAS Manufacturer 2003 630-08-0 CO 3602 0.34 0.34 1

0268 RECIP Waukesha L7042G Lowest Manifold (best power) NGAS Manufacturer 2003 74-82-8 CH4 219 0.59 0.59 1

0268 RECIP Waukesha L7042G Lowest Manifold (best power) NGAS Manufacturer 2003 CEL0002 NOx 1238 0.09 0.09 1

0268 RECIP Waukesha L7042G Lowest Manifold (best power) NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

0268 RECIP Waukesha L7042G Lowest Manifold (best power) NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

0268 RECIP Waukesha L7042G Lowest Manifold (best power) NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

171

Table 3.3 Compilation of combustion emission factors for estimating GHG and CAC emissions.

Fact

or

Equ

ipm

ent

Typ

e

Identifier 1 Identifier 2 Identifier 3 Fuel Type

Factor Reference Y

ear CAS

Number Compound Emission

Factor (ng/J) L

ower

U

ncer

tain

ty

Upp

er

Unc

erta

inty

U

ncer

tain

ty

Ref

eren

ce

0268 RECIP Waukesha L7042G Lowest Manifold (best power) NGAS Manufacturer 2003 CEL0006 VOC 39 0.27 0.27 1

0268 RECIP Waukesha L7042G Lowest Manifold (best power) NGAS Manufacturer 2003 CEL0007 THC 259 0.51 0.51 1

0269 RECIP Waukesha L7042G Standard (best economy) NGAS

CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0269 RECIP Waukesha L7042G Standard (best economy) NGAS Manufacturer 2003 630-08-0 CO 169 0.34 0.34 1

0269 RECIP Waukesha L7042G Standard (best economy) NGAS Manufacturer 2003 74-82-8 CH4 141 0.59 0.59 1

0269 RECIP Waukesha L7042G Standard (best economy) NGAS Manufacturer 2003 CEL0002 NOx 2476 0.09 0.09 1

0269 RECIP Waukesha L7042G Standard (best economy) NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

0269 RECIP Waukesha L7042G Standard (best economy) NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

0269 RECIP Waukesha L7042G Standard (best economy) NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

0269 RECIP Waukesha L7042G Standard (best economy) NGAS Manufacturer 2003 CEL0006 VOC 28 0.27 0.27 1

0269 RECIP Waukesha L7042G Standard (best economy) NGAS Manufacturer 2003 CEL0007 THC 169 0.51 0.51 1

0270 RECIP Waukesha L7042G - 10:1 NGAS CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0270 RECIP Waukesha L7042G - 10:1 NGAS Manufacturer 2003 630-08-0 CO 113 0.34 0.34 1

0270 RECIP Waukesha L7042G - 10:1 NGAS U.S. EPA AP-42 -> Profile: 0016 2000 74-82-8 CH4 99 0.59 0.59 1

0270 RECIP Waukesha L7042G - 10:1 NGAS Manufacturer 2003 CEL0002 NOx 2026 0.09 0.09 1

0270 RECIP Waukesha L7042G - 10:1 NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

0270 RECIP Waukesha L7042G - 10:1 NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

0270 RECIP Waukesha L7042G - 10:1 NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

0270 RECIP Waukesha L7042G - 10:1 NGAS Manufacturer 2003 CEL0006 VOC 23 0.27 0.27 1 0270 RECIP Waukesha L7042G - 10:1 NGAS CH4 + VOC 2003 CEL0007 THC 122 0.48 0.48 1

172

Table 3.3 Compilation of combustion emission factors for estimating GHG and CAC emissions.

Fact

or

Equ

ipm

ent

Typ

e

Identifier 1 Identifier 2 Identifier 3 Fuel Type

Factor Reference Y

ear CAS

Number Compound Emission

Factor (ng/J) L

ower

U

ncer

tain

ty

Upp

er

Unc

erta

inty

U

ncer

tain

ty

Ref

eren

ce

0271 RECIP Waukesha L7042G - 8:1 NGAS CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0271 RECIP Waukesha L7042G - 8:1 NGAS Manufacturer 2003 630-08-0 CO 106 0.34 0.34 1

0271 RECIP Waukesha L7042G - 8:1 NGAS U.S. EPA AP-42 -> Profile: 0016 2000 74-82-8 CH4 99 0.59 0.59 1

0271 RECIP Waukesha L7042G - 8:1 NGAS Manufacturer 2003 CEL0002 NOx 1899 0.09 0.09 1

0271 RECIP Waukesha L7042G - 8:1 NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

0271 RECIP Waukesha L7042G - 8:1 NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

0271 RECIP Waukesha L7042G - 8:1 NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

0271 RECIP Waukesha L7042G - 8:1 NGAS Manufacturer 2003 CEL0006 VOC 21 0.27 0.27 1 0271 RECIP Waukesha L7042G - 8:1 NGAS CH4 + VOC 2003 CEL0007 THC 120 0.49 0.49 1

0272 RECIP Waukesha L7042GL - 10.5:1 NGAS CHEMEX Labs -> Profile: 0014 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0272 RECIP Waukesha L7042GL - 10.5:1 NGAS Manufacturer 2003 630-08-0 CO 306 0.34 0.34 1 0272 RECIP Waukesha L7042GL - 10.5:1 NGAS Manufacturer 2003 74-82-8 CH4 520 0.59 0.59 1 0272 RECIP Waukesha L7042GL - 10.5:1 NGAS Manufacturer 2003 CEL0002 NOx 173 0.09 0.09 1

0272 RECIP Waukesha L7042GL - 10.5:1 NGAS U.S. EPA AP-42 -> Profile: 0014 2000 CEL0003 TPM 0.0332 0.67 1.50 7

0272 RECIP Waukesha L7042GL - 10.5:1 NGAS U.S. EPA AP-42 -> Profile: 0014 2000 CEL0004 PM10 0.0332 0.67 1.50 7

0272 RECIP Waukesha L7042GL - 10.5:1 NGAS U.S. EPA AP-42 -> Profile: 0014 2000 CEL0005 PM2.5 0.0332 0.67 1.50 7

0272 RECIP Waukesha L7042GL - 10.5:1 NGAS Manufacturer 2003 CEL0006 VOC 116 0.27 0.27 1 0272 RECIP Waukesha L7042GL - 10.5:1 NGAS Manufacturer 2003 CEL0007 THC 636 0.51 0.51 1

0273 RECIP Waukesha L7042GSI Catalytic conv. Input (3 way) NGAS

CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0273 RECIP Waukesha L7042GSI Catalytic conv. Input (3 way) NGAS Manufacturer 2003 630-08-0 CO 971 0.34 0.34 1

0273 RECIP Waukesha L7042GSI Catalytic conv. Input (3 way) NGAS Manufacturer 2003 74-82-8 CH4 183 0.59 0.59 1

0273 RECIP Waukesha L7042GSI Catalytic conv. Input (3 way) NGAS Manufacturer 2003 CEL0002 NOx 1402 0.09 0.09 1

0273 RECIP Waukesha L7042GSI Catalytic conv. NGAS U.S. EPA AP-42 - 2000 CEL0003 TPM 4.09 0.50 2.00 8

173

Table 3.3 Compilation of combustion emission factors for estimating GHG and CAC emissions.

Fact

or

Equ

ipm

ent

Typ

e

Identifier 1 Identifier 2 Identifier 3 Fuel Type

Factor Reference Y

ear CAS

Number Compound Emission

Factor (ng/J) L

ower

U

ncer

tain

ty

Upp

er

Unc

erta

inty

U

ncer

tain

ty

Ref

eren

ce

Input (3 way) > Profile: 0016

0273 RECIP Waukesha L7042GSI Catalytic conv. Input (3 way) NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

0273 RECIP Waukesha L7042GSI Catalytic conv. Input (3 way) NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

0273 RECIP Waukesha L7042GSI Catalytic conv. Input (3 way) NGAS Manufacturer 2003 CEL0006 VOC 32 0.27 0.27 1

0273 RECIP Waukesha L7042GSI Catalytic conv. Input (3 way) NGAS Manufacturer 2003 CEL0007 THC 216 0.51 0.51 1

0274 RECIP Waukesha L7042GSI Equal NOx & CO NGAS CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0274 RECIP Waukesha L7042GSI Equal NOx & CO NGAS Manufacturer 2003 630-08-0 CO 1295 0.34 0.34 1 0274 RECIP Waukesha L7042GSI Equal NOx & CO NGAS Manufacturer 2003 74-82-8 CH4 210 0.59 0.59 1 0274 RECIP Waukesha L7042GSI Equal NOx & CO NGAS Manufacturer 2003 CEL0002 NOx 1295 0.09 0.09 1

0274 RECIP Waukesha L7042GSI Equal NOx & CO NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

0274 RECIP Waukesha L7042GSI Equal NOx & CO NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

0274 RECIP Waukesha L7042GSI Equal NOx & CO NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

0274 RECIP Waukesha L7042GSI Equal NOx & CO NGAS Manufacturer 2003 CEL0006 VOC 38 0.27 0.27 1 0274 RECIP Waukesha L7042GSI Equal NOx & CO NGAS Manufacturer 2003 CEL0007 THC 248 0.51 0.51 1

0275 RECIP Waukesha L7042GSI Lowest Manifold (best power) NGAS

CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0275 RECIP Waukesha L7042GSI Lowest Manifold (best power) NGAS Manufacturer 2003 630-08-0 CO 3452 0.34 0.34 1

0275 RECIP Waukesha L7042GSI Lowest Manifold (best power) NGAS Manufacturer 2003 74-82-8 CH4 210 0.59 0.59 1

0275 RECIP Waukesha L7042GSI Lowest Manifold (best power) NGAS Manufacturer 2003 CEL0002 NOx 1187 0.09 0.09 1

0275 RECIP Waukesha L7042GSI Lowest Manifold (best power) NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

0275 RECIP Waukesha L7042GSI Lowest Manifold (best power) NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

0275 RECIP Waukesha L7042GSI Lowest Manifold (best power) NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

174

Table 3.3 Compilation of combustion emission factors for estimating GHG and CAC emissions.

Fact

or

Equ

ipm

ent

Typ

e

Identifier 1 Identifier 2 Identifier 3 Fuel Type

Factor Reference Y

ear CAS

Number Compound Emission

Factor (ng/J) L

ower

U

ncer

tain

ty

Upp

er

Unc

erta

inty

U

ncer

tain

ty

Ref

eren

ce

0275 RECIP Waukesha L7042GSI Lowest Manifold (best power) NGAS Manufacturer 2003 CEL0006 VOC 38 0.27 0.27 1

0275 RECIP Waukesha L7042GSI Lowest Manifold (best power) NGAS Manufacturer 2003 CEL0007 THC 248 0.51 0.51 1

0276 RECIP Waukesha L7042GSI Standard (best economy) NGAS

CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0276 RECIP Waukesha L7042GSI Standard (best economy) NGAS Manufacturer 2003 630-08-0 CO 162 0.34 0.34 1

0276 RECIP Waukesha L7042GSI Standard (best economy) NGAS Manufacturer 2003 74-82-8 CH4 135 0.59 0.59 1

0276 RECIP Waukesha L7042GSI Standard (best economy) NGAS Manufacturer 2003 CEL0002 NOx 2373 0.09 0.09 1

0276 RECIP Waukesha L7042GSI Standard (best economy) NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

0276 RECIP Waukesha L7042GSI Standard (best economy) NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

0276 RECIP Waukesha L7042GSI Standard (best economy) NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

0276 RECIP Waukesha L7042GSI Standard (best economy) NGAS Manufacturer 2003 CEL0006 VOC 27 0.27 0.27 1

0276 RECIP Waukesha L7042GSI Standard (best economy) NGAS Manufacturer 2003 CEL0007 THC 162 0.51 0.51 1

0277 RECIP Waukesha L7042GSI - 8:1 NGAS CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0277 RECIP Waukesha L7042GSI - 8:1 NGAS Manufacturer 2003 630-08-0 CO 108 0.34 0.34 1

0277 RECIP Waukesha L7042GSI - 8:1 NGAS U.S. EPA AP-42 -> Profile: 0016 2000 74-82-8 CH4 99 0.59 0.59 1

0277 RECIP Waukesha L7042GSI - 8:1 NGAS Manufacturer 2003 CEL0002 NOx 1942 0.09 0.09 1

0277 RECIP Waukesha L7042GSI - 8:1 NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

0277 RECIP Waukesha L7042GSI - 8:1 NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

0277 RECIP Waukesha L7042GSI - 8:1 NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

0277 RECIP Waukesha L7042GSI - 8:1 NGAS Manufacturer 2003 CEL0006 VOC 22 0.27 0.27 1 0277 RECIP Waukesha L7042GSI - 8:1 NGAS CH4 + VOC 2003 CEL0007 THC 121 0.48 0.48 1

175

Table 3.3 Compilation of combustion emission factors for estimating GHG and CAC emissions.

Fact

or

Equ

ipm

ent

Typ

e

Identifier 1 Identifier 2 Identifier 3 Fuel Type

Factor Reference Y

ear CAS

Number Compound Emission

Factor (ng/J) L

ower

U

ncer

tain

ty

Upp

er

Unc

erta

inty

U

ncer

tain

ty

Ref

eren

ce

0278 RECIP Waukesha L7044GSI Catalytic conv. Input (3 way) NGAS

CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0278 RECIP Waukesha L7044GSI Catalytic conv. Input (3 way) NGAS Manufacturer 2003 630-08-0 CO 1445 0.34 0.34 1

0278 RECIP Waukesha L7044GSI Catalytic conv. Input (3 way) NGAS Manufacturer 2003 74-82-8 CH4 89 0.59 0.59 1

0278 RECIP Waukesha L7044GSI Catalytic conv. Input (3 way) NGAS Manufacturer 2003 CEL0002 NOx 1667 0.09 0.09 1

0278 RECIP Waukesha L7044GSI Catalytic conv. Input (3 way) NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

0278 RECIP Waukesha L7044GSI Catalytic conv. Input (3 way) NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

0278 RECIP Waukesha L7044GSI Catalytic conv. Input (3 way) NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

0278 RECIP Waukesha L7044GSI Catalytic conv. Input (3 way) NGAS Manufacturer 2003 CEL0006 VOC 22 0.27 0.27 1

0278 RECIP Waukesha L7044GSI Catalytic conv. Input (3 way) NGAS Manufacturer 2003 CEL0007 THC 111 0.51 0.51 1

0279 RECIP Waukesha L7044GSI Equal NOx & CO NGAS CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0279 RECIP Waukesha L7044GSI Equal NOx & CO NGAS Manufacturer 2003 630-08-0 CO 1556 0.34 0.34 1 0279 RECIP Waukesha L7044GSI Equal NOx & CO NGAS Manufacturer 2003 74-82-8 CH4 94 0.59 0.59 1 0279 RECIP Waukesha L7044GSI Equal NOx & CO NGAS Manufacturer 2003 CEL0002 NOx 1556 0.09 0.09 1

0279 RECIP Waukesha L7044GSI Equal NOx & CO NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

0279 RECIP Waukesha L7044GSI Equal NOx & CO NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

0279 RECIP Waukesha L7044GSI Equal NOx & CO NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

0279 RECIP Waukesha L7044GSI Equal NOx & CO NGAS Manufacturer 2003 CEL0006 VOC 28 0.27 0.27 1 0279 RECIP Waukesha L7044GSI Equal NOx & CO NGAS Manufacturer 2003 CEL0007 THC 122 0.51 0.51 1

0280 RECIP Waukesha L7044GSI Standard (best economy) NGAS

CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0280 RECIP Waukesha L7044GSI Standard (best economy) NGAS Manufacturer 2003 630-08-0 CO 222 0.34 0.34 1

0280 RECIP Waukesha L7044GSI Standard (best NGAS Manufacturer 2003 74-82-8 CH4 67 0.59 0.59 1

176

Table 3.3 Compilation of combustion emission factors for estimating GHG and CAC emissions.

Fact

or

Equ

ipm

ent

Typ

e

Identifier 1 Identifier 2 Identifier 3 Fuel Type

Factor Reference Y

ear CAS

Number Compound Emission

Factor (ng/J) L

ower

U

ncer

tain

ty

Upp

er

Unc

erta

inty

U

ncer

tain

ty

Ref

eren

ce

economy)

0280 RECIP Waukesha L7044GSI Standard (best economy) NGAS Manufacturer 2003 CEL0002 NOx 2556 0.09 0.09 1

0280 RECIP Waukesha L7044GSI Standard (best economy) NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

0280 RECIP Waukesha L7044GSI Standard (best economy) NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

0280 RECIP Waukesha L7044GSI Standard (best economy) NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

0280 RECIP Waukesha L7044GSI Standard (best economy) NGAS Manufacturer 2003 CEL0006 VOC 22 0.27 0.27 1

0280 RECIP Waukesha L7044GSI Standard (best economy) NGAS Manufacturer 2003 CEL0007 THC 89 0.51 0.51 1

0281 RECIP Waukesha P48GL 8:7:1:CR Standard (HS turbo) NGAS

CHEMEX Labs -> Profile: 0014 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0281 RECIP Waukesha P48GL 8:7:1:CR Standard (HS turbo) NGAS Manufacturer 2003 630-08-0 CO 202 0.34 0.34 1

0281 RECIP Waukesha P48GL 8:7:1:CR Standard (HS turbo) NGAS Manufacturer 2003 74-82-8 CH4 303 0.59 0.59 1

0281 RECIP Waukesha P48GL 8:7:1:CR Standard (HS turbo) NGAS Manufacturer 2003 CEL0002 NOx 238 0.09 0.09 1

0281 RECIP Waukesha P48GL 8:7:1:CR Standard (HS turbo) NGAS

U.S. EPA AP-42 -> Profile: 0014 2000 CEL0003 TPM 0.0332 0.67 1.50 7

0281 RECIP Waukesha P48GL 8:7:1:CR Standard (HS turbo) NGAS

U.S. EPA AP-42 -> Profile: 0014 2000 CEL0004 PM10 0.0332 0.67 1.50 7

0281 RECIP Waukesha P48GL 8:7:1:CR Standard (HS turbo) NGAS

U.S. EPA AP-42 -> Profile: 0014 2000 CEL0005 PM2.5 0.0332 0.67 1.50 7

0281 RECIP Waukesha P48GL 8:7:1:CR Standard (HS turbo) NGAS Manufacturer 2003 CEL0006 VOC 54 0.27 0.27 1

0281 RECIP Waukesha P48GL 8:7:1:CR Standard (HS turbo) NGAS Manufacturer 2003 CEL0007 THC 357 0.51 0.51 1

0282 RECIP Waukesha P48GL/GLD - 11:1 NGAS CHEMEX Labs -> Profile: 0014 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0282 RECIP Waukesha P48GL/GLD - 11:1 NGAS Manufacturer 2003 630-08-0 CO 238 0.34 0.34 1

0282 RECIP Waukesha P48GL/GLD - 11:1 NGAS U.S. EPA AP-42 -> Profile: 0014 2000 74-82-8 CH4 538 0.59 0.59 1

177

Table 3.3 Compilation of combustion emission factors for estimating GHG and CAC emissions.

Fact

or

Equ

ipm

ent

Typ

e

Identifier 1 Identifier 2 Identifier 3 Fuel Type

Factor Reference Y

ear CAS

Number Compound Emission

Factor (ng/J) L

ower

U

ncer

tain

ty

Upp

er

Unc

erta

inty

U

ncer

tain

ty

Ref

eren

ce

0282 RECIP Waukesha P48GL/GLD - 11:1 NGAS Manufacturer 2003 CEL0002 NOx 476 0.09 0.09 1

0282 RECIP Waukesha P48GL/GLD - 11:1 NGAS U.S. EPA AP-42 -> Profile: 0014 2000 CEL0003 TPM 0.0332 0.67 1.50 7

0282 RECIP Waukesha P48GL/GLD - 11:1 NGAS U.S. EPA AP-42 -> Profile: 0014 2000 CEL0004 PM10 0.0332 0.67 1.50 7

0282 RECIP Waukesha P48GL/GLD - 11:1 NGAS U.S. EPA AP-42 -> Profile: 0014 2000 CEL0005 PM2.5 0.0332 0.67 1.50 7

0282 RECIP Waukesha P48GL/GLD - 11:1 NGAS Manufacturer 2003 CEL0006 VOC 119 0.27 0.27 1 0282 RECIP Waukesha P48GL/GLD - 11:1 NGAS CH4 + VOC 2003 CEL0007 THC 657 0.48 0.48 1

0283 RECIP Waukesha P48GL/GLD, 11:1 CR

Standard (HS turbo) NGAS

CHEMEX Labs -> Profile: 0014 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0283 RECIP Waukesha P48GL/GLD, 11:1 CR

Standard (HS turbo) NGAS Manufacturer 2003 630-08-0 CO 208 0.34 0.34 1

0283 RECIP Waukesha P48GL/GLD, 11:1 CR

Standard (HS turbo) NGAS Manufacturer 2003 74-82-8 CH4 505 0.59 0.59 1

0283 RECIP Waukesha P48GL/GLD, 11:1 CR

Standard (HS turbo) NGAS Manufacturer 2003 CEL0002 NOx 309 0.09 0.09 1

0283 RECIP Waukesha P48GL/GLD, 11:1 CR

Standard (HS turbo) NGAS

U.S. EPA AP-42 -> Profile: 0014 2000 CEL0003 TPM 0.0332 0.67 1.50 7

0283 RECIP Waukesha P48GL/GLD, 11:1 CR

Standard (HS turbo) NGAS

U.S. EPA AP-42 -> Profile: 0014 2000 CEL0004 PM10 0.0332 0.67 1.50 7

0283 RECIP Waukesha P48GL/GLD, 11:1 CR

Standard (HS turbo) NGAS

U.S. EPA AP-42 -> Profile: 0014 2000 CEL0005 PM2.5 0.0332 0.67 1.50 7

0283 RECIP Waukesha P48GL/GLD, 11:1 CR

Standard (HS turbo) NGAS Manufacturer 2003 CEL0006 VOC 89 0.27 0.27 1

0283 RECIP Waukesha P48GL/GLD, 11:1 CR

Standard (HS turbo) NGAS Manufacturer 2003 CEL0007 THC 594 0.51 0.51 1

0284 RECIP Waukesha P48GL/GLD, 11:1 CR

T.A. Luft Emissions NGAS

CHEMEX Labs -> Profile: 0014 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0284 RECIP Waukesha P48GL/GLD, 11:1 CR

T.A. Luft Emissions NGAS Manufacturer 2003 630-08-0 CO 189 0.34 0.34 1

0284 RECIP Waukesha P48GL/GLD, 11:1 CR

T.A. Luft Emissions NGAS Manufacturer 2003 74-82-8 CH4 363 0.59 0.59 1

0284 RECIP Waukesha P48GL/GLD, 11:1 CR

T.A. Luft Emissions NGAS Manufacturer 2003 CEL0002 NOx 149 0.09 0.09 1

0284 RECIP Waukesha P48GL/GLD, 11:1 T.A. Luft NGAS U.S. EPA AP-42 - 2000 CEL0003 TPM 0.0332 0.67 1.50 7

178

Table 3.3 Compilation of combustion emission factors for estimating GHG and CAC emissions.

Fact

or

Equ

ipm

ent

Typ

e

Identifier 1 Identifier 2 Identifier 3 Fuel Type

Factor Reference Y

ear CAS

Number Compound Emission

Factor (ng/J) L

ower

U

ncer

tain

ty

Upp

er

Unc

erta

inty

U

ncer

tain

ty

Ref

eren

ce

CR Emissions > Profile: 0014

0284 RECIP Waukesha P48GL/GLD, 11:1 CR

T.A. Luft Emissions NGAS

U.S. EPA AP-42 -> Profile: 0014 2000 CEL0004 PM10 0.0332 0.67 1.50 7

0284 RECIP Waukesha P48GL/GLD, 11:1 CR

T.A. Luft Emissions NGAS

U.S. EPA AP-42 -> Profile: 0014 2000 CEL0005 PM2.5 0.0332 0.67 1.50 7

0284 RECIP Waukesha P48GL/GLD, 11:1 CR

T.A. Luft Emissions NGAS Manufacturer 2003 CEL0006 VOC 54 0.27 0.27 1

0284 RECIP Waukesha P48GL/GLD, 11:1 CR

T.A. Luft Emissions NGAS Manufacturer 2003 CEL0007 THC 416 0.51 0.51 1

0285 RECIP Waukesha P9390G Catalytic conv. Input (3 way) NGAS

CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0285 RECIP Waukesha P9390G Catalytic conv. Input (3 way) NGAS Manufacturer 2003 630-08-0 CO 1000 0.34 0.34 1

0285 RECIP Waukesha P9390G Catalytic conv. Input (3 way) NGAS Manufacturer 2003 74-82-8 CH4 189 0.59 0.59 1

0285 RECIP Waukesha P9390G Catalytic conv. Input (3 way) NGAS Manufacturer 2003 CEL0002 NOx 1444 0.09 0.09 1

0285 RECIP Waukesha P9390G Catalytic conv. Input (3 way) NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

0285 RECIP Waukesha P9390G Catalytic conv. Input (3 way) NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

0285 RECIP Waukesha P9390G Catalytic conv. Input (3 way) NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

0285 RECIP Waukesha P9390G Catalytic conv. Input (3 way) NGAS Manufacturer 2003 CEL0006 VOC 33 0.27 0.27 1

0285 RECIP Waukesha P9390G Catalytic conv. Input (3 way) NGAS Manufacturer 2003 CEL0007 THC 222 0.51 0.51 1

0286 RECIP Waukesha P9390G Equal NOx & CO NGAS CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0286 RECIP Waukesha P9390G Equal NOx & CO NGAS Manufacturer 2003 630-08-0 CO 1333 0.34 0.34 1 0286 RECIP Waukesha P9390G Equal NOx & CO NGAS Manufacturer 2003 74-82-8 CH4 217 0.59 0.59 1 0286 RECIP Waukesha P9390G Equal NOx & CO NGAS Manufacturer 2003 CEL0002 NOx 1333 0.09 0.09 1

0286 RECIP Waukesha P9390G Equal NOx & CO NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

0286 RECIP Waukesha P9390G Equal NOx & CO NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

179

Table 3.3 Compilation of combustion emission factors for estimating GHG and CAC emissions.

Fact

or

Equ

ipm

ent

Typ

e

Identifier 1 Identifier 2 Identifier 3 Fuel Type

Factor Reference Y

ear CAS

Number Compound Emission

Factor (ng/J) L

ower

U

ncer

tain

ty

Upp

er

Unc

erta

inty

U

ncer

tain

ty

Ref

eren

ce

0286 RECIP Waukesha P9390G Equal NOx & CO NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

0286 RECIP Waukesha P9390G Equal NOx & CO NGAS Manufacturer 2003 CEL0006 VOC 39 0.27 0.27 1 0286 RECIP Waukesha P9390G Equal NOx & CO NGAS Manufacturer 2003 CEL0007 THC 255 0.51 0.51 1

0287 RECIP Waukesha P9390G Lowest Manifold (best power) NGAS

CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0287 RECIP Waukesha P9390G Lowest Manifold (best power) NGAS Manufacturer 2003 630-08-0 CO 3554 0.34 0.34 1

0287 RECIP Waukesha P9390G Lowest Manifold (best power) NGAS Manufacturer 2003 74-82-8 CH4 217 0.59 0.59 1

0287 RECIP Waukesha P9390G Lowest Manifold (best power) NGAS Manufacturer 2003 CEL0002 NOx 1222 0.09 0.09 1

0287 RECIP Waukesha P9390G Lowest Manifold (best power) NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

0287 RECIP Waukesha P9390G Lowest Manifold (best power) NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

0287 RECIP Waukesha P9390G Lowest Manifold (best power) NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

0287 RECIP Waukesha P9390G Lowest Manifold (best power) NGAS Manufacturer 2003 CEL0006 VOC 39 0.27 0.27 1

0287 RECIP Waukesha P9390G Lowest Manifold (best power) NGAS Manufacturer 2003 CEL0007 THC 255 0.51 0.51 1

0288 RECIP Waukesha P9390G Standard (best economy) NGAS

CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0288 RECIP Waukesha P9390G Standard (best economy) NGAS Manufacturer 2003 630-08-0 CO 167 0.34 0.34 1

0288 RECIP Waukesha P9390G Standard (best economy) NGAS Manufacturer 2003 74-82-8 CH4 139 0.59 0.59 1

0288 RECIP Waukesha P9390G Standard (best economy) NGAS Manufacturer 2003 CEL0002 NOx 2444 0.09 0.09 1

0288 RECIP Waukesha P9390G Standard (best economy) NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

0288 RECIP Waukesha P9390G Standard (best economy) NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

0288 RECIP Waukesha P9390G Standard (best economy) NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

180

Table 3.3 Compilation of combustion emission factors for estimating GHG and CAC emissions.

Fact

or

Equ

ipm

ent

Typ

e

Identifier 1 Identifier 2 Identifier 3 Fuel Type

Factor Reference Y

ear CAS

Number Compound Emission

Factor (ng/J) L

ower

U

ncer

tain

ty

Upp

er

Unc

erta

inty

U

ncer

tain

ty

Ref

eren

ce

0288 RECIP Waukesha P9390G Standard (best economy) NGAS Manufacturer 2003 CEL0006 VOC 28 0.27 0.27 1

0288 RECIP Waukesha P9390G Standard (best economy) NGAS Manufacturer 2003 CEL0007 THC 167 0.51 0.51 1

0289 RECIP Waukesha P9390G - 10:1 NGAS CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0289 RECIP Waukesha P9390G - 10:1 NGAS Manufacturer 2003 630-08-0 CO 111 0.34 0.34 1

0289 RECIP Waukesha P9390G - 10:1 NGAS U.S. EPA AP-42 -> Profile: 0016 2000 74-82-8 CH4 99 0.59 0.59 1

0289 RECIP Waukesha P9390G - 10:1 NGAS Manufacturer 2003 CEL0002 NOx 1999 0.09 0.09 1

0289 RECIP Waukesha P9390G - 10:1 NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

0289 RECIP Waukesha P9390G - 10:1 NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

0289 RECIP Waukesha P9390G - 10:1 NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

0289 RECIP Waukesha P9390G - 10:1 NGAS Manufacturer 2003 CEL0006 VOC 22 0.27 0.27 1 0289 RECIP Waukesha P9390G - 10:1 NGAS CH4 + VOC 2003 CEL0007 THC 121 0.48 0.48 1

0290 RECIP Waukesha P9390G - 8:1 NGAS CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0290 RECIP Waukesha P9390G - 8:1 NGAS Manufacturer 2003 630-08-0 CO 104 0.34 0.34 1

0290 RECIP Waukesha P9390G - 8:1 NGAS U.S. EPA AP-42 -> Profile: 0016 2000 74-82-8 CH4 99 0.59 0.59 1

0290 RECIP Waukesha P9390G - 8:1 NGAS Manufacturer 2003 CEL0002 NOx 1876 0.09 0.09 1

0290 RECIP Waukesha P9390G - 8:1 NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

0290 RECIP Waukesha P9390G - 8:1 NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

0290 RECIP Waukesha P9390G - 8:1 NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

0290 RECIP Waukesha P9390G - 8:1 NGAS Manufacturer 2003 CEL0006 VOC 21 0.27 0.27 1 0290 RECIP Waukesha P9390G - 8:1 NGAS CH4 + VOC 2003 CEL0007 THC 120 0.49 0.49 1

0291 RECIP Waukesha P9390GL - 10.5:1 NGAS CHEMEX Labs -> Profile: 0014 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0291 RECIP Waukesha P9390GL - 10.5:1 NGAS Manufacturer 2003 630-08-0 CO 311 0.34 0.34 1 0291 RECIP Waukesha P9390GL - 10.5:1 NGAS Manufacturer 2003 74-82-8 CH4 528 0.59 0.59 1

181

Table 3.3 Compilation of combustion emission factors for estimating GHG and CAC emissions.

Fact

or

Equ

ipm

ent

Typ

e

Identifier 1 Identifier 2 Identifier 3 Fuel Type

Factor Reference Y

ear CAS

Number Compound Emission

Factor (ng/J) L

ower

U

ncer

tain

ty

Upp

er

Unc

erta

inty

U

ncer

tain

ty

Ref

eren

ce

0291 RECIP Waukesha P9390GL - 10.5:1 NGAS Manufacturer 2003 CEL0002 NOx 176 0.09 0.09 1

0291 RECIP Waukesha P9390GL - 10.5:1 NGAS U.S. EPA AP-42 -> Profile: 0014 2000 CEL0003 TPM 0.0332 0.67 1.50 7

0291 RECIP Waukesha P9390GL - 10.5:1 NGAS U.S. EPA AP-42 -> Profile: 0014 2000 CEL0004 PM10 0.0332 0.67 1.50 7

0291 RECIP Waukesha P9390GL - 10.5:1 NGAS U.S. EPA AP-42 -> Profile: 0014 2000 CEL0005 PM2.5 0.0332 0.67 1.50 7

0291 RECIP Waukesha P9390GL - 10.5:1 NGAS Manufacturer 2003 CEL0006 VOC 117 0.27 0.27 1 0291 RECIP Waukesha P9390GL - 10.5:1 NGAS Manufacturer 2003 CEL0007 THC 645 0.51 0.51 1

0292 RECIP Waukesha P9390GSI Catalytic conv. Input (3 way) NGAS

CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0292 RECIP Waukesha P9390GSI Catalytic conv. Input (3 way) NGAS Manufacturer 2003 630-08-0 CO 1000 0.34 0.34 1

0292 RECIP Waukesha P9390GSI Catalytic conv. Input (3 way) NGAS Manufacturer 2003 74-82-8 CH4 189 0.59 0.59 1

0292 RECIP Waukesha P9390GSI Catalytic conv. Input (3 way) NGAS Manufacturer 2003 CEL0002 NOx 1444 0.09 0.09 1

0292 RECIP Waukesha P9390GSI Catalytic conv. Input (3 way) NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

0292 RECIP Waukesha P9390GSI Catalytic conv. Input (3 way) NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

0292 RECIP Waukesha P9390GSI Catalytic conv. Input (3 way) NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

0292 RECIP Waukesha P9390GSI Catalytic conv. Input (3 way) NGAS Manufacturer 2003 CEL0006 VOC 33 0.27 0.27 1

0292 RECIP Waukesha P9390GSI Catalytic conv. Input (3 way) NGAS Manufacturer 2003 CEL0007 THC 222 0.51 0.51 1

0293 RECIP Waukesha P9390GSI Equal NOx & CO NGAS CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0293 RECIP Waukesha P9390GSI Equal NOx & CO NGAS Manufacturer 2003 630-08-0 CO 1333 0.34 0.34 1 0293 RECIP Waukesha P9390GSI Equal NOx & CO NGAS Manufacturer 2003 74-82-8 CH4 217 0.59 0.59 1 0293 RECIP Waukesha P9390GSI Equal NOx & CO NGAS Manufacturer 2003 CEL0002 NOx 1333 0.09 0.09 1

0293 RECIP Waukesha P9390GSI Equal NOx & CO NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

0293 RECIP Waukesha P9390GSI Equal NOx & CO NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

182

Table 3.3 Compilation of combustion emission factors for estimating GHG and CAC emissions.

Fact

or

Equ

ipm

ent

Typ

e

Identifier 1 Identifier 2 Identifier 3 Fuel Type

Factor Reference Y

ear CAS

Number Compound Emission

Factor (ng/J) L

ower

U

ncer

tain

ty

Upp

er

Unc

erta

inty

U

ncer

tain

ty

Ref

eren

ce

0293 RECIP Waukesha P9390GSI Equal NOx & CO NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

0293 RECIP Waukesha P9390GSI Equal NOx & CO NGAS Manufacturer 2003 CEL0006 VOC 39 0.27 0.27 1 0293 RECIP Waukesha P9390GSI Equal NOx & CO NGAS Manufacturer 2003 CEL0007 THC 255 0.51 0.51 1

0294 RECIP Waukesha P9390GSI Lowest Manifold (best power) NGAS

CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0294 RECIP Waukesha P9390GSI Lowest Manifold (best power) NGAS Manufacturer 2003 630-08-0 CO 3554 0.34 0.34 1

0294 RECIP Waukesha P9390GSI Lowest Manifold (best power) NGAS Manufacturer 2003 74-82-8 CH4 217 0.59 0.59 1

0294 RECIP Waukesha P9390GSI Lowest Manifold (best power) NGAS Manufacturer 2003 CEL0002 NOx 1222 0.09 0.09 1

0294 RECIP Waukesha P9390GSI Lowest Manifold (best power) NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

0294 RECIP Waukesha P9390GSI Lowest Manifold (best power) NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

0294 RECIP Waukesha P9390GSI Lowest Manifold (best power) NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

0294 RECIP Waukesha P9390GSI Lowest Manifold (best power) NGAS Manufacturer 2003 CEL0006 VOC 39 0.27 0.27 1

0294 RECIP Waukesha P9390GSI Lowest Manifold (best power) NGAS Manufacturer 2003 CEL0007 THC 255 0.51 0.51 1

0295 RECIP Waukesha P9390GSI Standard (best economy) NGAS

CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0295 RECIP Waukesha P9390GSI Standard (best economy) NGAS Manufacturer 2003 630-08-0 CO 167 0.34 0.34 1

0295 RECIP Waukesha P9390GSI Standard (best economy) NGAS Manufacturer 2003 74-82-8 CH4 139 0.59 0.59 1

0295 RECIP Waukesha P9390GSI Standard (best economy) NGAS Manufacturer 2003 CEL0002 NOx 2444 0.09 0.09 1

0295 RECIP Waukesha P9390GSI Standard (best economy) NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

0295 RECIP Waukesha P9390GSI Standard (best economy) NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

0295 RECIP Waukesha P9390GSI Standard (best economy) NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

183

Table 3.3 Compilation of combustion emission factors for estimating GHG and CAC emissions.

Fact

or

Equ

ipm

ent

Typ

e

Identifier 1 Identifier 2 Identifier 3 Fuel Type

Factor Reference Y

ear CAS

Number Compound Emission

Factor (ng/J) L

ower

U

ncer

tain

ty

Upp

er

Unc

erta

inty

U

ncer

tain

ty

Ref

eren

ce

0295 RECIP Waukesha P9390GSI Standard (best economy) NGAS Manufacturer 2003 CEL0006 VOC 28 0.27 0.27 1

0295 RECIP Waukesha P9390GSI Standard (best economy) NGAS Manufacturer 2003 CEL0007 THC 167 0.51 0.51 1

0296 RECIP Waukesha VR220 Catalytic conv. Input (3 way) NGAS

CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0296 RECIP Waukesha VR220 Catalytic conv. Input (3 way) NGAS Manufacturer 2003 630-08-0 CO 1688 0.34 0.34 1

0296 RECIP Waukesha VR220 Catalytic conv. Input (3 way) NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 74-82-8 CH4 99 0.59 0.59 1

0296 RECIP Waukesha VR220 Catalytic conv. Input (3 way) NGAS Manufacturer 2003 CEL0002 NOx 950 0.09 0.09 1

0296 RECIP Waukesha VR220 Catalytic conv. Input (3 way) NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

0296 RECIP Waukesha VR220 Catalytic conv. Input (3 way) NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

0296 RECIP Waukesha VR220 Catalytic conv. Input (3 way) NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

0296 RECIP Waukesha VR220 Catalytic conv. Input (3 way) NGAS Manufacturer 2003 CEL0006 VOC 37 0.27 0.27 1

0296 RECIP Waukesha VR220 Catalytic conv. Input (3 way) NGAS CH4 + VOC 2003 CEL0007 THC 136 0.43 0.43 1

0297 RECIP Waukesha VR220 Equal NOx & CO NGAS CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0297 RECIP Waukesha VR220 Equal NOx & CO NGAS Manufacturer 2003 630-08-0 CO 950 0.34 0.34 1

0297 RECIP Waukesha VR220 Equal NOx & CO NGAS U.S. EPA AP-42 -> Profile: 0016 2000 74-82-8 CH4 99 0.59 0.59 1

0297 RECIP Waukesha VR220 Equal NOx & CO NGAS Manufacturer 2003 CEL0002 NOx 791 0.09 0.09 1

0297 RECIP Waukesha VR220 Equal NOx & CO NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

0297 RECIP Waukesha VR220 Equal NOx & CO NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

0297 RECIP Waukesha VR220 Equal NOx & CO NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

0297 RECIP Waukesha VR220 Equal NOx & CO NGAS Manufacturer 2003 CEL0006 VOC 37 0.27 0.27 1 0297 RECIP Waukesha VR220 Equal NOx & CO NGAS CH4 + VOC 2003 CEL0007 THC 136 0.43 0.43 1

184

Table 3.3 Compilation of combustion emission factors for estimating GHG and CAC emissions.

Fact

or

Equ

ipm

ent

Typ

e

Identifier 1 Identifier 2 Identifier 3 Fuel Type

Factor Reference Y

ear CAS

Number Compound Emission

Factor (ng/J) L

ower

U

ncer

tain

ty

Upp

er

Unc

erta

inty

U

ncer

tain

ty

Ref

eren

ce

0298 RECIP Waukesha VR220 Lowest Manifold (best power) NGAS

CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0298 RECIP Waukesha VR220 Lowest Manifold (best power) NGAS Manufacturer 2003 630-08-0 CO 4748 0.34 0.34 1

0298 RECIP Waukesha VR220 Lowest Manifold (best power) NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 74-82-8 CH4 99 0.59 0.59 1

0298 RECIP Waukesha VR220 Lowest Manifold (best power) NGAS Manufacturer 2003 CEL0002 NOx 1161 0.09 0.09 1

0298 RECIP Waukesha VR220 Lowest Manifold (best power) NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

0298 RECIP Waukesha VR220 Lowest Manifold (best power) NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

0298 RECIP Waukesha VR220 Lowest Manifold (best power) NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

0298 RECIP Waukesha VR220 Lowest Manifold (best power) NGAS Manufacturer 2003 CEL0006 VOC 42 0.27 0.27 1

0298 RECIP Waukesha VR220 Lowest Manifold (best power) NGAS CH4 + VOC 2003 CEL0007 THC 141 0.42 0.42 1

0299 RECIP Waukesha VR220 Standard (best economy) NGAS

CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0299 RECIP Waukesha VR220 Standard (best economy) NGAS Manufacturer 2003 630-08-0 CO 211 0.34 0.34 1

0299 RECIP Waukesha VR220 Standard (best economy) NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 74-82-8 CH4 99 0.59 0.59 1

0299 RECIP Waukesha VR220 Standard (best economy) NGAS Manufacturer 2003 CEL0002 NOx 897 0.09 0.09 1

0299 RECIP Waukesha VR220 Standard (best economy) NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

0299 RECIP Waukesha VR220 Standard (best economy) NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

0299 RECIP Waukesha VR220 Standard (best economy) NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

0299 RECIP Waukesha VR220 Standard (best economy) NGAS Manufacturer 2003 CEL0006 VOC 32 0.27 0.27 1

0299 RECIP Waukesha VR220 Standard (best economy) NGAS CH4 + VOC 2003 CEL0007 THC 131 0.45 0.45 1

185

Table 3.3 Compilation of combustion emission factors for estimating GHG and CAC emissions.

Fact

or

Equ

ipm

ent

Typ

e

Identifier 1 Identifier 2 Identifier 3 Fuel Type

Factor Reference Y

ear CAS

Number Compound Emission

Factor (ng/J) L

ower

U

ncer

tain

ty

Upp

er

Unc

erta

inty

U

ncer

tain

ty

Ref

eren

ce

0300 RECIP Waukesha VR330 Catalytic conv. Input (3 way) NGAS

CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0300 RECIP Waukesha VR330 Catalytic conv. Input (3 way) NGAS Manufacturer 2003 630-08-0 CO 1688 0.34 0.34 1

0300 RECIP Waukesha VR330 Catalytic conv. Input (3 way) NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 74-82-8 CH4 99 0.59 0.59 1

0300 RECIP Waukesha VR330 Catalytic conv. Input (3 way) NGAS Manufacturer 2003 CEL0002 NOx 950 0.09 0.09 1

0300 RECIP Waukesha VR330 Catalytic conv. Input (3 way) NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

0300 RECIP Waukesha VR330 Catalytic conv. Input (3 way) NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

0300 RECIP Waukesha VR330 Catalytic conv. Input (3 way) NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

0300 RECIP Waukesha VR330 Catalytic conv. Input (3 way) NGAS Manufacturer 2003 CEL0006 VOC 37 0.27 0.27 1

0300 RECIP Waukesha VR330 Catalytic conv. Input (3 way) NGAS CH4 + VOC 2003 CEL0007 THC 136 0.43 0.43 1

0301 RECIP Waukesha VR330 Equal NOx & CO NGAS CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0301 RECIP Waukesha VR330 Equal NOx & CO NGAS Manufacturer 2003 630-08-0 CO 950 0.34 0.34 1

0301 RECIP Waukesha VR330 Equal NOx & CO NGAS U.S. EPA AP-42 -> Profile: 0016 2000 74-82-8 CH4 99 0.59 0.59 1

0301 RECIP Waukesha VR330 Equal NOx & CO NGAS Manufacturer 2003 CEL0002 NOx 791 0.09 0.09 1

0301 RECIP Waukesha VR330 Equal NOx & CO NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

0301 RECIP Waukesha VR330 Equal NOx & CO NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

0301 RECIP Waukesha VR330 Equal NOx & CO NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

0301 RECIP Waukesha VR330 Equal NOx & CO NGAS Manufacturer 2003 CEL0006 VOC 37 0.27 0.27 1 0301 RECIP Waukesha VR330 Equal NOx & CO NGAS CH4 + VOC 2003 CEL0007 THC 136 0.43 0.43 1

0302 RECIP Waukesha VR330 Lowest Manifold (best power) NGAS

CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0302 RECIP Waukesha VR330 Lowest Manifold (best power) NGAS Manufacturer 2003 630-08-0 CO 4748 0.34 0.34 1

186

Table 3.3 Compilation of combustion emission factors for estimating GHG and CAC emissions.

Fact

or

Equ

ipm

ent

Typ

e

Identifier 1 Identifier 2 Identifier 3 Fuel Type

Factor Reference Y

ear CAS

Number Compound Emission

Factor (ng/J) L

ower

U

ncer

tain

ty

Upp

er

Unc

erta

inty

U

ncer

tain

ty

Ref

eren

ce

0302 RECIP Waukesha VR330 Lowest Manifold (best power) NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 74-82-8 CH4 99 0.59 0.59 1

0302 RECIP Waukesha VR330 Lowest Manifold (best power) NGAS Manufacturer 2003 CEL0002 NOx 1161 0.09 0.09 1

0302 RECIP Waukesha VR330 Lowest Manifold (best power) NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

0302 RECIP Waukesha VR330 Lowest Manifold (best power) NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

0302 RECIP Waukesha VR330 Lowest Manifold (best power) NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

0302 RECIP Waukesha VR330 Lowest Manifold (best power) NGAS Manufacturer 2003 CEL0006 VOC 42 0.27 0.27 1

0302 RECIP Waukesha VR330 Lowest Manifold (best power) NGAS CH4 + VOC 2003 CEL0007 THC 141 0.42 0.42 1

0303 RECIP Waukesha VR330 Standard (best economy) NGAS

CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0303 RECIP Waukesha VR330 Standard (best economy) NGAS Manufacturer 2003 630-08-0 CO 211 0.34 0.34 1

0303 RECIP Waukesha VR330 Standard (best economy) NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 74-82-8 CH4 99 0.59 0.59 1

0303 RECIP Waukesha VR330 Standard (best economy) NGAS Manufacturer 2003 CEL0002 NOx 897 0.09 0.09 1

0303 RECIP Waukesha VR330 Standard (best economy) NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

0303 RECIP Waukesha VR330 Standard (best economy) NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

0303 RECIP Waukesha VR330 Standard (best economy) NGAS

U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

0303 RECIP Waukesha VR330 Standard (best economy) NGAS Manufacturer 2003 CEL0006 VOC 32 0.27 0.27 1

0303 RECIP Waukesha VR330 Standard (best economy) NGAS CH4 + VOC 2003 CEL0007 THC 131 0.45 0.45 1

0304 RECIP White Superior 12G825 NGAS CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0304 RECIP White Superior 12G825 NGAS Manufacturer 2003 630-08-0 CO 211 0.34 0.34 1 0304 RECIP White Superior 12G825 NGAS U.S. EPA AP-42 - 2000 74-82-8 CH4 99 0.59 0.59 1

187

Table 3.3 Compilation of combustion emission factors for estimating GHG and CAC emissions.

Fact

or

Equ

ipm

ent

Typ

e

Identifier 1 Identifier 2 Identifier 3 Fuel Type

Factor Reference Y

ear CAS

Number Compound Emission

Factor (ng/J) L

ower

U

ncer

tain

ty

Upp

er

Unc

erta

inty

U

ncer

tain

ty

Ref

eren

ce

> Profile: 0016 0304 RECIP White Superior 12G825 NGAS Manufacturer 2003 CEL0002 NOx 1759 0.09 0.09 1

0304 RECIP White Superior 12G825 NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

0304 RECIP White Superior 12G825 NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

0304 RECIP White Superior 12G825 NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

0304 RECIP White Superior 12G825 NGAS Manufacturer 2003 CEL0006 VOC 23 0.27 0.27 1 0304 RECIP White Superior 12G825 NGAS CH4 + VOC 2003 CEL0007 THC 122 0.48 0.48 1

0305 RECIP White Superior 12GTL NGAS CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0305 RECIP White Superior 12GTL NGAS Manufacturer 2003 630-08-0 CO 106 0.34 0.34 1

0305 RECIP White Superior 12GTL NGAS U.S. EPA AP-42 -> Profile: 0016 2000 74-82-8 CH4 99 0.59 0.59 1

0305 RECIP White Superior 12GTL NGAS Manufacturer 2003 CEL0002 NOx 1759 0.09 0.09 1

0305 RECIP White Superior 12GTL NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

0305 RECIP White Superior 12GTL NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

0305 RECIP White Superior 12GTL NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

0305 RECIP White Superior 12GTL NGAS Manufacturer 2003 CEL0006 VOC 59 0.27 0.27 1 0305 RECIP White Superior 12GTL NGAS CH4 + VOC 2003 CEL0007 THC 158 0.38 0.38 1

0306 RECIP White Superior 12GTLB NGAS CHEMEX Labs -> Profile: 0014 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0306 RECIP White Superior 12GTLB NGAS Manufacturer 2003 630-08-0 CO 151 0.34 0.34 1

0306 RECIP White Superior 12GTLB NGAS U.S. EPA AP-42 -> Profile: 0014 2000 74-82-8 CH4 538 0.59 0.59 1

0306 RECIP White Superior 12GTLB NGAS Manufacturer 2003 CEL0002 NOx 172 0.09 0.09 1

0306 RECIP White Superior 12GTLB NGAS U.S. EPA AP-42 -> Profile: 0014 2000 CEL0003 TPM 0.0332 0.67 1.50 7

0306 RECIP White Superior 12GTLB NGAS U.S. EPA AP-42 -> Profile: 0014 2000 CEL0004 PM10 0.0332 0.67 1.50 7

0306 RECIP White Superior 12GTLB NGAS U.S. EPA AP-42 -> Profile: 0014 2000 CEL0005 PM2.5 0.0332 0.67 1.50 7

188

Table 3.3 Compilation of combustion emission factors for estimating GHG and CAC emissions.

Fact

or

Equ

ipm

ent

Typ

e

Identifier 1 Identifier 2 Identifier 3 Fuel Type

Factor Reference Y

ear CAS

Number Compound Emission

Factor (ng/J) L

ower

U

ncer

tain

ty

Upp

er

Unc

erta

inty

U

ncer

tain

ty

Ref

eren

ce

0306 RECIP White Superior 12GTLB NGAS Manufacturer 2003 CEL0006 VOC 65 0.27 0.27 1 0306 RECIP White Superior 12GTLB NGAS CH4 + VOC 2003 CEL0007 THC 603 0.52 0.52 1

0307 RECIP White Superior 12GTLE NGAS CHEMEX Labs -> Profile: 0014 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0307 RECIP White Superior 12GTLE NGAS Manufacturer 2003 630-08-0 CO 230 0.34 0.34 1

0307 RECIP White Superior 12GTLE NGAS U.S. EPA AP-42 -> Profile: 0014 2000 74-82-8 CH4 538 0.59 0.59 1

0307 RECIP White Superior 12GTLE NGAS Manufacturer 2003 CEL0002 NOx 230 0.09 0.09 1

0307 RECIP White Superior 12GTLE NGAS U.S. EPA AP-42 -> Profile: 0014 2000 CEL0003 TPM 0.0332 0.67 1.50 7

0307 RECIP White Superior 12GTLE NGAS U.S. EPA AP-42 -> Profile: 0014 2000 CEL0004 PM10 0.0332 0.67 1.50 7

0307 RECIP White Superior 12GTLE NGAS U.S. EPA AP-42 -> Profile: 0014 2000 CEL0005 PM2.5 0.0332 0.67 1.50 7

0307 RECIP White Superior 12GTLE NGAS Manufacturer 2003 CEL0006 VOC 86 0.27 0.27 1 0307 RECIP White Superior 12GTLE NGAS CH4 + VOC 2003 CEL0007 THC 624 0.51 0.51 1

0308 RECIP White Superior 12SGTB NGAS CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0308 RECIP White Superior 12SGTB NGAS Manufacturer 2003 630-08-0 CO 164 0.34 0.34 1

0308 RECIP White Superior 12SGTB NGAS U.S. EPA AP-42 -> Profile: 0016 2000 74-82-8 CH4 99 0.59 0.59 1

0308 RECIP White Superior 12SGTB NGAS Manufacturer 2003 CEL0002 NOx 177 0.09 0.09 1

0308 RECIP White Superior 12SGTB NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

0308 RECIP White Superior 12SGTB NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

0308 RECIP White Superior 12SGTB NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

0308 RECIP White Superior 12SGTB NGAS Manufacturer 2003 CEL0006 VOC 66 0.27 0.27 1 0308 RECIP White Superior 12SGTB NGAS CH4 + VOC 2003 CEL0007 THC 165 0.37 0.37 1

0309 RECIP White Superior 16G825 NGAS CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0309 RECIP White Superior 16G825 NGAS Manufacturer 2003 630-08-0 CO 211 0.34 0.34 1

0309 RECIP White Superior 16G825 NGAS U.S. EPA AP-42 -> Profile: 0016 2000 74-82-8 CH4 99 0.59 0.59 1

0309 RECIP White Superior 16G825 NGAS Manufacturer 2003 CEL0002 NOx 1759 0.09 0.09 1

189

Table 3.3 Compilation of combustion emission factors for estimating GHG and CAC emissions.

Fact

or

Equ

ipm

ent

Typ

e

Identifier 1 Identifier 2 Identifier 3 Fuel Type

Factor Reference Y

ear CAS

Number Compound Emission

Factor (ng/J) L

ower

U

ncer

tain

ty

Upp

er

Unc

erta

inty

U

ncer

tain

ty

Ref

eren

ce

0309 RECIP White Superior 16G825 NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

0309 RECIP White Superior 16G825 NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

0309 RECIP White Superior 16G825 NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

0309 RECIP White Superior 16G825 NGAS Manufacturer 2003 CEL0006 VOC 23 0.27 0.27 1 0309 RECIP White Superior 16G825 NGAS CH4 + VOC 2003 CEL0007 THC 122 0.48 0.48 1

0310 RECIP White Superior 16GTL NGAS CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0310 RECIP White Superior 16GTL NGAS Manufacturer 2003 630-08-0 CO 106 0.34 0.34 1

0310 RECIP White Superior 16GTL NGAS U.S. EPA AP-42 -> Profile: 0016 2000 74-82-8 CH4 99 0.59 0.59 1

0310 RECIP White Superior 16GTL NGAS Manufacturer 2003 CEL0002 NOx 1759 0.09 0.09 1

0310 RECIP White Superior 16GTL NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

0310 RECIP White Superior 16GTL NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

0310 RECIP White Superior 16GTL NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

0310 RECIP White Superior 16GTL NGAS Manufacturer 2003 CEL0006 VOC 59 0.27 0.27 1 0310 RECIP White Superior 16GTL NGAS CH4 + VOC 2003 CEL0007 THC 158 0.38 0.38 1

0311 RECIP White Superior 16GTLB NGAS CHEMEX Labs -> Profile: 0014 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0311 RECIP White Superior 16GTLB NGAS Manufacturer 2003 630-08-0 CO 160 0.34 0.34 1

0311 RECIP White Superior 16GTLB NGAS U.S. EPA AP-42 -> Profile: 0014 2000 74-82-8 CH4 538 0.59 0.59 1

0311 RECIP White Superior 16GTLB NGAS Manufacturer 2003 CEL0002 NOx 173 0.09 0.09 1

0311 RECIP White Superior 16GTLB NGAS U.S. EPA AP-42 -> Profile: 0014 2000 CEL0003 TPM 0.0332 0.67 1.50 7

0311 RECIP White Superior 16GTLB NGAS U.S. EPA AP-42 -> Profile: 0014 2000 CEL0004 PM10 0.0332 0.67 1.50 7

0311 RECIP White Superior 16GTLB NGAS U.S. EPA AP-42 -> Profile: 0014 2000 CEL0005 PM2.5 0.0332 0.67 1.50 7

0311 RECIP White Superior 16GTLB NGAS Manufacturer 2003 CEL0006 VOC 64 0.27 0.27 1 0311 RECIP White Superior 16GTLB NGAS CH4 + VOC 2003 CEL0007 THC 602 0.53 0.53 1

190

Table 3.3 Compilation of combustion emission factors for estimating GHG and CAC emissions.

Fact

or

Equ

ipm

ent

Typ

e

Identifier 1 Identifier 2 Identifier 3 Fuel Type

Factor Reference Y

ear CAS

Number Compound Emission

Factor (ng/J) L

ower

U

ncer

tain

ty

Upp

er

Unc

erta

inty

U

ncer

tain

ty

Ref

eren

ce

0312 RECIP White Superior 16SGTB NGAS CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0312 RECIP White Superior 16SGTB NGAS Manufacturer 2003 630-08-0 CO 154 0.34 0.34 1

0312 RECIP White Superior 16SGTB NGAS U.S. EPA AP-42 -> Profile: 0016 2000 74-82-8 CH4 99 0.59 0.59 1

0312 RECIP White Superior 16SGTB NGAS Manufacturer 2003 CEL0002 NOx 177 0.09 0.09 1

0312 RECIP White Superior 16SGTB NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

0312 RECIP White Superior 16SGTB NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

0312 RECIP White Superior 16SGTB NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

0312 RECIP White Superior 16SGTB NGAS Manufacturer 2003 CEL0006 VOC 66 0.27 0.27 1 0312 RECIP White Superior 16SGTB NGAS CH4 + VOC 2003 CEL0007 THC 165 0.37 0.37 1

0313 RECIP White Superior 1706G NGAS CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0313 RECIP White Superior 1706G NGAS Manufacturer 2003 630-08-0 CO 166 0.34 0.34 1

0313 RECIP White Superior 1706G NGAS U.S. EPA AP-42 -> Profile: 0016 2000 74-82-8 CH4 99 0.59 0.59 1

0313 RECIP White Superior 1706G NGAS Manufacturer 2003 CEL0002 NOx 178 0.09 0.09 1

0313 RECIP White Superior 1706G NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

0313 RECIP White Superior 1706G NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

0313 RECIP White Superior 1706G NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

0313 RECIP White Superior 1706G NGAS Manufacturer 2003 CEL0006 VOC 36 0.27 0.27 1 0313 RECIP White Superior 1706G NGAS CH4 + VOC 2003 CEL0007 THC 135 0.44 0.44 1

0314 RECIP White Superior 1712G NGAS CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0314 RECIP White Superior 1712G NGAS Manufacturer 2003 630-08-0 CO 279 0.34 0.34 1

0314 RECIP White Superior 1712G NGAS U.S. EPA AP-42 -> Profile: 0016 2000 74-82-8 CH4 99 0.59 0.59 1

0314 RECIP White Superior 1712G NGAS Manufacturer 2003 CEL0002 NOx 175 0.09 0.09 1

0314 RECIP White Superior 1712G NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

191

Table 3.3 Compilation of combustion emission factors for estimating GHG and CAC emissions.

Fact

or

Equ

ipm

ent

Typ

e

Identifier 1 Identifier 2 Identifier 3 Fuel Type

Factor Reference Y

ear CAS

Number Compound Emission

Factor (ng/J) L

ower

U

ncer

tain

ty

Upp

er

Unc

erta

inty

U

ncer

tain

ty

Ref

eren

ce

0314 RECIP White Superior 1712G NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

0314 RECIP White Superior 1712G NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

0314 RECIP White Superior 1712G NGAS Manufacturer 2003 CEL0006 VOC 70 0.27 0.27 1 0314 RECIP White Superior 1712G NGAS CH4 + VOC 2003 CEL0007 THC 169 0.36 0.36 1

0315 RECIP White Superior 2406G NGAS CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0315 RECIP White Superior 2406G NGAS Manufacturer 2003 630-08-0 CO 348 0.34 0.34 1

0315 RECIP White Superior 2406G NGAS U.S. EPA AP-42 -> Profile: 0016 2000 74-82-8 CH4 99 0.59 0.59 1

0315 RECIP White Superior 2406G NGAS Manufacturer 2003 CEL0002 NOx 112 0.09 0.09 1

0315 RECIP White Superior 2406G NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

0315 RECIP White Superior 2406G NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

0315 RECIP White Superior 2406G NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

0315 RECIP White Superior 2406G NGAS Manufacturer 2003 CEL0006 VOC 124 0.27 0.27 1 0315 RECIP White Superior 2406G NGAS CH4 + VOC 2003 CEL0007 THC 223 0.30 0.30 1

0316 RECIP White Superior 2408G NGAS CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0316 RECIP White Superior 2408G NGAS Manufacturer 2003 630-08-0 CO 348 0.34 0.34 1

0316 RECIP White Superior 2408G NGAS U.S. EPA AP-42 -> Profile: 0016 2000 74-82-8 CH4 99 0.59 0.59 1

0316 RECIP White Superior 2408G NGAS Manufacturer 2003 CEL0002 NOx 112 0.09 0.09 1

0316 RECIP White Superior 2408G NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

0316 RECIP White Superior 2408G NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

0316 RECIP White Superior 2408G NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

0316 RECIP White Superior 2408G NGAS Manufacturer 2003 CEL0006 VOC 124 0.27 0.27 1 0316 RECIP White Superior 2408G NGAS CH4 + VOC 2003 CEL0007 THC 223 0.30 0.30 1

0317 RECIP White Superior 2412G NGAS CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

192

Table 3.3 Compilation of combustion emission factors for estimating GHG and CAC emissions.

Fact

or

Equ

ipm

ent

Typ

e

Identifier 1 Identifier 2 Identifier 3 Fuel Type

Factor Reference Y

ear CAS

Number Compound Emission

Factor (ng/J) L

ower

U

ncer

tain

ty

Upp

er

Unc

erta

inty

U

ncer

tain

ty

Ref

eren

ce

0317 RECIP White Superior 2412G NGAS Manufacturer 2003 630-08-0 CO 348 0.34 0.34 1

0317 RECIP White Superior 2412G NGAS U.S. EPA AP-42 -> Profile: 0016 2000 74-82-8 CH4 99 0.59 0.59 1

0317 RECIP White Superior 2412G NGAS Manufacturer 2003 CEL0002 NOx 112 0.09 0.09 1

0317 RECIP White Superior 2412G NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

0317 RECIP White Superior 2412G NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

0317 RECIP White Superior 2412G NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

0317 RECIP White Superior 2412G NGAS Manufacturer 2003 CEL0006 VOC 124 0.27 0.27 1 0317 RECIP White Superior 2412G NGAS CH4 + VOC 2003 CEL0007 THC 223 0.30 0.30 1

0318 RECIP White Superior 2416G NGAS CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0318 RECIP White Superior 2416G NGAS Manufacturer 2003 630-08-0 CO 348 0.34 0.34 1

0318 RECIP White Superior 2416G NGAS U.S. EPA AP-42 -> Profile: 0016 2000 74-82-8 CH4 99 0.59 0.59 1

0318 RECIP White Superior 2416G NGAS Manufacturer 2003 CEL0002 NOx 112 0.09 0.09 1

0318 RECIP White Superior 2416G NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

0318 RECIP White Superior 2416G NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

0318 RECIP White Superior 2416G NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

0318 RECIP White Superior 2416G NGAS Manufacturer 2003 CEL0006 VOC 124 0.27 0.27 1 0318 RECIP White Superior 2416G NGAS CH4 + VOC 2003 CEL0007 THC 223 0.30 0.30 1

0319 RECIP White Superior 6G825 NGAS CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0319 RECIP White Superior 6G825 NGAS Manufacturer 2003 630-08-0 CO 211 0.34 0.34 1

0319 RECIP White Superior 6G825 NGAS U.S. EPA AP-42 -> Profile: 0016 2000 74-82-8 CH4 99 0.59 0.59 1

0319 RECIP White Superior 6G825 NGAS Manufacturer 2003 CEL0002 NOx 1759 0.09 0.09 1

0319 RECIP White Superior 6G825 NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

0319 RECIP White Superior 6G825 NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

193

Table 3.3 Compilation of combustion emission factors for estimating GHG and CAC emissions.

Fact

or

Equ

ipm

ent

Typ

e

Identifier 1 Identifier 2 Identifier 3 Fuel Type

Factor Reference Y

ear CAS

Number Compound Emission

Factor (ng/J) L

ower

U

ncer

tain

ty

Upp

er

Unc

erta

inty

U

ncer

tain

ty

Ref

eren

ce

0319 RECIP White Superior 6G825 NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

0319 RECIP White Superior 6G825 NGAS Manufacturer 2003 CEL0006 VOC 23 0.27 0.27 1 0319 RECIP White Superior 6G825 NGAS CH4 + VOC 2003 CEL0007 THC 122 0.48 0.48 1

0320 RECIP White Superior 6GTL NGAS CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0320 RECIP White Superior 6GTL NGAS Manufacturer 2003 630-08-0 CO 106 0.34 0.34 1

0320 RECIP White Superior 6GTL NGAS U.S. EPA AP-42 -> Profile: 0016 2000 74-82-8 CH4 99 0.59 0.59 1

0320 RECIP White Superior 6GTL NGAS Manufacturer 2003 CEL0002 NOx 1759 0.09 0.09 1

0320 RECIP White Superior 6GTL NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

0320 RECIP White Superior 6GTL NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

0320 RECIP White Superior 6GTL NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

0320 RECIP White Superior 6GTL NGAS Manufacturer 2003 CEL0006 VOC 59 0.27 0.27 1 0320 RECIP White Superior 6GTL NGAS CH4 + VOC 2003 CEL0007 THC 158 0.38 0.38 1

0321 RECIP White Superior 6GTLB NGAS CHEMEX Labs -> Profile: 0014 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0321 RECIP White Superior 6GTLB NGAS Manufacturer 2003 630-08-0 CO 359 0.34 0.34 1

0321 RECIP White Superior 6GTLB NGAS U.S. EPA AP-42 -> Profile: 0014 2000 74-82-8 CH4 538 0.59 0.59 1

0321 RECIP White Superior 6GTLB NGAS Manufacturer 2003 CEL0002 NOx 236 0.09 0.09 1

0321 RECIP White Superior 6GTLB NGAS U.S. EPA AP-42 -> Profile: 0014 2000 CEL0003 TPM 0.0332 0.67 1.50 7

0321 RECIP White Superior 6GTLB NGAS U.S. EPA AP-42 -> Profile: 0014 2000 CEL0004 PM10 0.0332 0.67 1.50 7

0321 RECIP White Superior 6GTLB NGAS U.S. EPA AP-42 -> Profile: 0014 2000 CEL0005 PM2.5 0.0332 0.67 1.50 7

0321 RECIP White Superior 6GTLB NGAS Manufacturer 2003 CEL0006 VOC 86 0.27 0.27 1 0321 RECIP White Superior 6GTLB NGAS CH4 + VOC 2003 CEL0007 THC 624 0.51 0.51 1

0322 RECIP White Superior 8G825 NGAS CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0322 RECIP White Superior 8G825 NGAS Manufacturer 2003 630-08-0 CO 211 0.34 0.34 1 0322 RECIP White Superior 8G825 NGAS U.S. EPA AP-42 - 2000 74-82-8 CH4 99 0.59 0.59 1

194

Table 3.3 Compilation of combustion emission factors for estimating GHG and CAC emissions.

Fact

or

Equ

ipm

ent

Typ

e

Identifier 1 Identifier 2 Identifier 3 Fuel Type

Factor Reference Y

ear CAS

Number Compound Emission

Factor (ng/J) L

ower

U

ncer

tain

ty

Upp

er

Unc

erta

inty

U

ncer

tain

ty

Ref

eren

ce

> Profile: 0016 0322 RECIP White Superior 8G825 NGAS Manufacturer 2003 CEL0002 NOx 1759 0.09 0.09 1

0322 RECIP White Superior 8G825 NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

0322 RECIP White Superior 8G825 NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

0322 RECIP White Superior 8G825 NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

0322 RECIP White Superior 8G825 NGAS Manufacturer 2003 CEL0006 VOC 23 0.27 0.27 1 0322 RECIP White Superior 8G825 NGAS CH4 + VOC 2003 CEL0007 THC 122 0.48 0.48 1

0323 RECIP White Superior 8GTL NGAS CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0323 RECIP White Superior 8GTL NGAS Manufacturer 2003 630-08-0 CO 106 0.34 0.34 1

0323 RECIP White Superior 8GTL NGAS U.S. EPA AP-42 -> Profile: 0016 2000 74-82-8 CH4 99 0.59 0.59 1

0323 RECIP White Superior 8GTL NGAS Manufacturer 2003 CEL0002 NOx 1759 0.09 0.09 1

0323 RECIP White Superior 8GTL NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

0323 RECIP White Superior 8GTL NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

0323 RECIP White Superior 8GTL NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

0323 RECIP White Superior 8GTL NGAS Manufacturer 2003 CEL0006 VOC 59 0.27 0.27 1 0323 RECIP White Superior 8GTL NGAS CH4 + VOC 2003 CEL0007 THC 158 0.38 0.38 1

0324 RECIP White Superior 8GTLB NGAS CHEMEX Labs -> Profile: 0014 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0324 RECIP White Superior 8GTLB NGAS Manufacturer 2003 630-08-0 CO 357 0.34 0.34 1

0324 RECIP White Superior 8GTLB NGAS U.S. EPA AP-42 -> Profile: 0014 2000 74-82-8 CH4 538 0.59 0.59 1

0324 RECIP White Superior 8GTLB NGAS Manufacturer 2003 CEL0002 NOx 237 0.09 0.09 1

0324 RECIP White Superior 8GTLB NGAS U.S. EPA AP-42 -> Profile: 0014 2000 CEL0003 TPM 0.0332 0.67 1.50 7

0324 RECIP White Superior 8GTLB NGAS U.S. EPA AP-42 -> Profile: 0014 2000 CEL0004 PM10 0.0332 0.67 1.50 7

0324 RECIP White Superior 8GTLB NGAS U.S. EPA AP-42 -> Profile: 0014 2000 CEL0005 PM2.5 0.0332 0.67 1.50 7

195

Table 3.3 Compilation of combustion emission factors for estimating GHG and CAC emissions.

Fact

or

Equ

ipm

ent

Typ

e

Identifier 1 Identifier 2 Identifier 3 Fuel Type

Factor Reference Y

ear CAS

Number Compound Emission

Factor (ng/J) L

ower

U

ncer

tain

ty

Upp

er

Unc

erta

inty

U

ncer

tain

ty

Ref

eren

ce

0324 RECIP White Superior 8GTLB NGAS Manufacturer 2003 CEL0006 VOC 90 0.27 0.27 1 0324 RECIP White Superior 8GTLB NGAS CH4 + VOC 2003 CEL0007 THC 628 0.50 0.50 1

0325 RECIP White Superior 8SGTB NGAS CHEMEX Labs -> Profile: 0016 1996 10024-97-2 N2O 5.72 0.18 5.45 3

0325 RECIP White Superior 8SGTB NGAS Manufacturer 2003 630-08-0 CO 357 0.34 0.34 1

0325 RECIP White Superior 8SGTB NGAS U.S. EPA AP-42 -> Profile: 0016 2000 74-82-8 CH4 99 0.59 0.59 1

0325 RECIP White Superior 8SGTB NGAS Manufacturer 2003 CEL0002 NOx 176 0.09 0.09 1

0325 RECIP White Superior 8SGTB NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0003 TPM 4.09 0.50 2.00 8

0325 RECIP White Superior 8SGTB NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0004 PM10 4.09 0.50 2.00 8

0325 RECIP White Superior 8SGTB NGAS U.S. EPA AP-42 -> Profile: 0016 2000 CEL0005 PM2.5 4.09 0.50 2.00 8

0325 RECIP White Superior 8SGTB NGAS Manufacturer 2003 CEL0006 VOC 106 0.27 0.27 1 0325 RECIP White Superior 8SGTB NGAS CH4 + VOC 2003 CEL0007 THC 106 0.61 0.61 1 0326 TURB NGAS U.S. EPA AP-42 2000 10024-97-2 N2O 1.29 0.18 5.45 3 0326 TURB NGAS U.S. EPA AP-42 2000 630-08-0 CO 35 0.95 0.95 1 0326 TURB NGAS U.S. EPA AP-42 2000 74-82-8 CH4 3.7 0.29 3.43 2 0326 TURB NGAS U.S. EPA AP-42 2000 CEL0002 NOx 138 0.21 0.21 1 0326 TURB NGAS U.S. EPA AP-42 2000 CEL0003 TPM 0.82 0.50 2.00 8 0326 TURB NGAS U.S. EPA AP-42 2000 CEL0004 PM10 0.82 0.50 2.00 8 0326 TURB NGAS U.S. EPA AP-42 2000 CEL0005 PM2.5 0.82 0.50 2.00 8 0326 TURB NGAS U.S. EPA AP-42 2000 CEL0006 VOC 0.9 0.75 1.33 1 0326 TURB NGAS U.S. EPA AP-42 2000 CEL0007 THC 4.7 0.66 1.51 1 0327 TURB Lean Premix NGAS U.S. EPA AP-42 2000 10024-97-2 N2O 1.29 0.18 5.45 3 0327 TURB Lean Premix NGAS U.S. EPA AP-42 2000 630-08-0 CO 6.5 0.95 0.95 1 0327 TURB Lean Premix NGAS U.S. EPA AP-42 2000 74-82-8 CH4 3.7 0.29 3.43 2 0327 TURB Lean Premix NGAS U.S. EPA AP-42 2000 CEL0002 NOx 43 0.21 0.21 1 0327 TURB Lean Premix NGAS U.S. EPA AP-42 2000 CEL0003 TPM 0.82 0.50 2.00 8 0327 TURB Lean Premix NGAS U.S. EPA AP-42 2000 CEL0004 PM10 0.82 0.50 2.00 8 0327 TURB Lean Premix NGAS U.S. EPA AP-42 2000 CEL0005 PM2.5 0.82 0.50 2.00 8 0327 TURB Lean Premix NGAS U.S. EPA AP-42 2000 CEL0006 VOC 0.9 0.75 1.33 1 0327 TURB Lean Premix NGAS U.S. EPA AP-42 2000 CEL0007 THC 4.7 0.66 1.51 1

0328 TURB Water-Steam Injection NGAS U.S. EPA AP-42 2000 10024-97-2 N2O 1.29 0.18 5.45 3

196

Table 3.3 Compilation of combustion emission factors for estimating GHG and CAC emissions.

Fact

or

Equ

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ent

Typ

e

Identifier 1 Identifier 2 Identifier 3 Fuel Type

Factor Reference Y

ear CAS

Number Compound Emission

Factor (ng/J) L

ower

U

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ty

Upp

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Unc

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U

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0328 TURB Water-Steam Injection NGAS U.S. EPA AP-42 2000 630-08-0 CO 13 0.95 0.95 1

0328 TURB Water-Steam Injection NGAS U.S. EPA AP-42 2000 74-82-8 CH4 3.7 0.29 3.43 2

0328 TURB Water-Steam Injection NGAS U.S. EPA AP-42 2000 CEL0002 NOx 56 0.21 0.21 1

0328 TURB Water-Steam Injection NGAS U.S. EPA AP-42 2000 CEL0003 TPM 0.82 0.50 2.00 8

0328 TURB Water-Steam Injection NGAS U.S. EPA AP-42 2000 CEL0004 PM10 0.82 0.50 2.00 8

0328 TURB Water-Steam Injection NGAS U.S. EPA AP-42 2000 CEL0005 PM2.5 0.82 0.50 2.00 8

0328 TURB Water-Steam Injection NGAS U.S. EPA AP-42 2000 CEL0006 VOC 0.9 0.75 1.33 1

0328 TURB Water-Steam Injection NGAS U.S. EPA AP-42 2000 CEL0007 THC 4.7 0.66 1.51 1

0329 DSEL <=600 hp DIESEL

Canada's GHG Inventory - 1997 (EnvCan) 1997 10024-97-2 N2O 10.3 0.18 5.45 3

0329 DSEL <=600 hp DIESEL U.S. EPA AP-42 Table 3-3.1 1996 124-38-9 CO2 70520 0.08 0.08 3

0329 DSEL <=600 hp DIESEL U.S. EPA AP-42 Table 3-3.1 1996 630-08-0 CO 408.5 0.67 1.50 7

0329 DSEL <=600 hp DIESEL

9% of TOC is CH4 (AP-42 Table 3.4-1) 1996 74-82-8 CH4 13.5 0.56 1.78 1

0329 DSEL <=600 hp DIESEL U.S. EPA AP-42 Table 3-3.1 1996 7446-09-5 SO2 124.7 0.67 1.50 7

0329 DSEL <=600 hp DIESEL U.S. EPA AP-42 Table 3-3.1 1996 CEL0002 NOx 1896.3 0.67 1.50 7

0329 DSEL <=600 hp DIESEL U.S. EPA AP-42 Table 3-3.1 1996 CEL0003 TPM 133.3 0.67 1.50 8

0329 DSEL <=600 hp DIESEL U.S. EPA AP-42 Table 3-3.1 1996 CEL0004 PM10 133.3 0.67 1.50 8

0329 DSEL <=600 hp DIESEL U.S. EPA AP-42 Table 3-3.1 1996 CEL0005 PM2.5 133.3 0.67 1.50 8

197

Table 3.3 Compilation of combustion emission factors for estimating GHG and CAC emissions.

Fact

or

Equ

ipm

ent

Typ

e

Identifier 1 Identifier 2 Identifier 3 Fuel Type

Factor Reference Y

ear CAS

Number Compound Emission

Factor (ng/J) L

ower

U

ncer

tain

ty

Upp

er

Unc

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U

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Ref

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0329 DSEL <=600 hp DIESEL

91% of TOC is CH4 (AP-42 Table 3.4-1) 1996 CEL0006 VOC 137 0.67 1.50 7

0329 DSEL <=600 hp DIESEL U.S. EPA AP-42 Table 3-3.1 1996 CEL0007 THC 150.5 0.67 1.50 7

0330 DSEL >600 hp Uncontrolled DIESEL

Canada's GHG Inventory - 1997 (EnvCan) 1997 10024-97-2 N2O 10.3 0.18 5.45 3

0330 DSEL >600 hp Uncontrolled DIESEL U.S. EPA AP-42 Table 3-4.1 1996 124-38-9 CO2 70950 0.08 0.08 3

0330 DSEL >600 hp Uncontrolled DIESEL U.S. EPA AP-42 Table 3-4.1 1996 630-08-0 CO 365.5 1.00 1.00 6

0330 DSEL >600 hp Uncontrolled DIESEL U.S. EPA AP-42 Table 3-4.1 1996 74-82-8 CH4 3.5 0.56 1.78 1

0330 DSEL >600 hp Uncontrolled DIESEL U.S. EPA AP-42 Table 3-4.1 1996 7446-09-5 SO2 124.7 0.50 0.50 5

0330 DSEL >600 hp Uncontrolled DIESEL U.S. EPA AP-42 Table 3-4.1 1996 CEL0002 NOx 1376 0.50 0.50 5

0330 DSEL >600 hp Uncontrolled DIESEL U.S. EPA AP-42 Table 3-4.2 1996 CEL0003 TPM 26.7 0.50 0.50 5

0330 DSEL >600 hp Uncontrolled DIESEL U.S. EPA AP-42 Table 3-4.2 1996 CEL0004 PM10 21.3 0.50 0.50 5

0330 DSEL >600 hp Uncontrolled DIESEL U.S. EPA AP-42 Table 3-4.2 1996 CEL0005 PM2.5 20.6 0.50 0.50 5

0330 DSEL >600 hp Uncontrolled DIESEL U.S. EPA AP-42 Table 3-4.1 1996 CEL0006 VOC 35.2 0.50 2.00 8

0330 DSEL >600 hp Uncontrolled DIESEL U.S. EPA AP-42 Table 3-4.1 1996 CEL0007 THC 38.7 1.00 1.00 6

0331 DSEL >600 hp Controlled DIESEL

Canada's GHG Inventory - 1997 (EnvCan) 1997 10024-97-2 N2O 10.3 0.18 5.45 3

0331 DSEL >600 hp Controlled DIESEL U.S. EPA AP-42 Table 3-4.1 1996 124-38-9 CO2 70950 0.08 0.08 3

0331 DSEL >600 hp Controlled DIESEL U.S. EPA AP-42 Table 3-4.1 1996 630-08-0 CO 365.5 1.00 1.00 6

0331 DSEL >600 hp Controlled DIESEL U.S. EPA AP-42 1996 74-82-8 CH4 3.5 0.56 1.78 1

198

Table 3.3 Compilation of combustion emission factors for estimating GHG and CAC emissions.

Fact

or

Equ

ipm

ent

Typ

e

Identifier 1 Identifier 2 Identifier 3 Fuel Type

Factor Reference Y

ear CAS

Number Compound Emission

Factor (ng/J) L

ower

U

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Unc

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Table 3-4.1

0331 DSEL >600 hp Controlled DIESEL U.S. EPA AP-42 Table 3-4.1 1996 7446-09-5 SO2 124.7 0.50 0.50 5

0331 DSEL >600 hp Controlled DIESEL U.S. EPA AP-42 Table 3-4.1 1996 CEL0002 NOx 817 0.50 0.50 5

0331 DSEL >600 hp Controlled DIESEL U.S. EPA AP-42 Table 3-4.2 1996 CEL0003 TPM 26.7 0.50 0.50 5

0331 DSEL >600 hp Controlled DIESEL U.S. EPA AP-42 Table 3-4.2 1996 CEL0004 PM10 21.3 0.50 0.50 5

0331 DSEL >600 hp Controlled DIESEL U.S. EPA AP-42 Table 3-4.2 1996 CEL0005 PM2.5 20.6 0.50 0.50 5

0331 DSEL >600 hp Controlled DIESEL U.S. EPA AP-42 Table 3-4.1 1996 CEL0006 VOC 35.2 0.50 2.00 8

0331 DSEL >600 hp Controlled DIESEL U.S. EPA AP-42 Table 3-4.1 1996 CEL0007 THC 38.7 1.00 1.00 6

0332 FL NGAS U.S. EPA AP-42 Table 13.5-1 1991 10024-97-2 N2O 0 0.18 5.45 3

0332 FL NGAS U.S. EPA AP-42 Table 13.5-1 1991 630-08-0 CO 159.1 0.55 1.81 1

0332 FL NGAS

U.S. EPA AP-42 Table 13.5-1 (55% of THC) 1991 74-82-8 CH4 33.1 1.00 1.00 3

0332 FL NGAS U.S. EPA AP-42 Table 13.5-1 1991 CEL0002 NOx 29.2 0.50 0.50 5

0332 FL NGAS EPA Fire 6.22. Flaring landfill gas 1991 CEL0003 TPM 57 0.50 0.50 5

0332 FL NGAS EPA Fire 6.22. Flaring landfill gas 1991 CEL0004 PM10 57 0.50 0.50 5

0332 FL NGAS EPA Fire 6.22. Flaring landfill gas 1991 CEL0005 PM2.5 57 0.50 0.50 5

0332 FL NGAS

U.S. EPA AP-42 Table 13.5-1 (37% of THC) 1991 CEL0006 VOC 22.3 0.51 1.96 1

0332 FL NGAS U.S. EPA AP-42 Table 13.5-1 1991 CEL0007 THC 60.2 0.54 1.86 1

0333 HEAT DIESEL U.S. EPA AP-42 1998 10024-97-2 N2O 0.34 0.18 5.45 3

199

Table 3.3 Compilation of combustion emission factors for estimating GHG and CAC emissions.

Fact

or

Equ

ipm

ent

Typ

e

Identifier 1 Identifier 2 Identifier 3 Fuel Type

Factor Reference Y

ear CAS

Number Compound Emission

Factor (ng/J) L

ower

U

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Table 1.3-8

0333 HEAT DIESEL U.S. EPA AP-42 Table 3-4.1 1996 124-38-9 CO2 70950 0.08 0.08 3

0333 HEAT DIESEL U.S. EPA AP-42 Table 1.3-1 1998 630-08-0 CO 15.5 0.25 0.25 4

0333 HEAT DIESEL U.S. EPA AP-42 Table 1.3-3 1998 74-82-8 CH4 0.16 1.00 1.00 3

0333 HEAT DIESEL

U.S. EPA AP-42 Table 1.3-1, S=0.05% CEPA 1998 7446-09-5 SO2 2.68 0.50 0.50 5

0333 HEAT DIESEL U.S. EPA AP-42 Table 1.3-1 1998 CEL0002 NOx 62 0.67 1.50 7

0333 HEAT DIESEL U.S. EPA AP-42 Table 1.3-1 1998 CEL0003 TPM 6.2 0.25 0.25 4

0333 HEAT DIESEL

U.S. EPA AP-42 Table 1.3-1, table 1.3-6 1998 CEL0004 PM10 3.1 0.50 2.00 8

0333 HEAT DIESEL

U.S. EPA AP-42 Table 1.3-1, table 1.3-6 1998 CEL0005 PM2.5 0.78 0.50 2.00 8

0333 HEAT DIESEL U.S. EPA AP-42 Table 1.3-3 1998 CEL0006 VOC 0.62 0.25 0.25 4

0333 HEAT DIESEL U.S. EPA AP-42 Table 1.3-3 1998 CEL0007 THC 0.78 0.25 0.25 4

0334 HEAT PROPANE U.S. EPA AP-42 Table 1.5-1 1996 10024-97-2 N2O 4.3 0.50 2.00 8

0334 HEAT PROPANE U.S. EPA AP-42 Table 1.5-1 1996 124-38-9 CO2 59166 0.08 0.08 3

0334 HEAT PROPANE U.S. EPA AP-42 Table 1.5-1 1996 630-08-0 CO 9 0.50 2.00 8

0334 HEAT PROPANE U.S. EPA AP-42 Table 1.5-1 1996 74-82-8 CH4 0.9 0.50 2.00 8

0334 HEAT PROPANE

UNION GAS (typical 5.5 mg/m3) 2000 7446-09-5 SO2 0.147 0.50 2.00 8

0334 HEAT PROPANE U.S. EPA AP-42 1996 CEL0002 NOx 66.3 0.50 2.00 8

200

Table 3.3 Compilation of combustion emission factors for estimating GHG and CAC emissions.

Fact

or

Equ

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ent

Typ

e

Identifier 1 Identifier 2 Identifier 3 Fuel Type

Factor Reference Y

ear CAS

Number Compound Emission

Factor (ng/J) L

ower

U

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Upp

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Table 1.5-1

0334 HEAT PROPANE U.S. EPA AP-42 Table 1.5-1 1996 CEL0003 TPM 1.9 0.50 2.00 8

0334 HEAT PROPANE U.S. EPA AP-42 Table 1.5-1 1996 CEL0004 PM10 1.9 0.50 2.00 8

0334 HEAT PROPANE U.S. EPA AP-42 Table 1.5-1 1996 CEL0005 PM2.5 1.9 0.50 2.00 8

0334 HEAT PROPANE U.S. EPA AP-42 Table 1.5-1 1996 CEL0006 VOC 1.5 0.50 2.00 8

0334 HEAT PROPANE U.S. EPA AP-42 Table 1.5-1 1996 CEL0007 THC 2.4 0.50 2.00 8

Uncertainty References

1. Calculated from variance in field data. 2. GRI/U.S. EPA. 1996. Methane Emissions from the Natural Gas Industry. Volume 11: Compressor Driver Exhaust. 3. Default uncertainty values published by IPCC (2000). 4. U.S. EPA AP-42 (1995 and Supplements). Emission Factor Rating A. 5. U.S. EPA AP-42 (1995 and Supplements). Emission Factor Rating B. 6. U.S. EPA AP-42 (1995 and Supplements). Emission Factor Rating C. 7. U.S. EPA AP-42 (1995 and Supplements). Emission Factor Rating D. 8. U.S. EPA AP-42 (1995 and Supplements). Emission Factor Rating E.

201

4.0 EQUIPMENT SCHEDULES Typical equipment schedules for estimating the number and type of potential leakage points on process units are presented in Tables 4.1. They are used to estimate emissions from fugitive equipment leaks (see section 7.1 in Volumes 3 and 4). Descriptions of the fields in Table 4.1 are:

• Equipment Type – type of process or equipment. • Component Type – type of component. These component types correspond to the

component types listed in the average emission factor tables presented earlier (Tables 3.1 and 3.2).

• Service – similar to the Natural Gas Type category, the type of stream a component contains has an affect on emissions from the component. The available services are:

o Gas/Vapour – all gas streams except Fuel Gas. o Fuel Gas – fuel piping tends to receive more modifications, is subjected to heat

and vibration and is generally odourless and, consequently, average emissions for fuel gas piping are greater.

o Light Liquid – the process fluid is a hydrocarbon liquid at the operating conditions and has a vapour pressure of 0.3 kPa or greater at 15ºC. Light/medium crude oil, condensate and NGLs fall into this category.

o Heavy Liquid – the process fluid is a hydrocarbon liquid at the operating conditions and has a vapour pressure of less than 0.3 kPa at 15ºC. Heavy crude oil and crude bitumen fall into this category.

• Count – the average number of the particular type of component typically used on specified type of process or equipment. These counts were determined from an analysis of field survey data.

• Lower and Upper Uncertainty – the uncertainty associated with the equipment component counts. These are the 95 confidence limits on the average number of components and were determined from an analysis of field survey data.

Tables 4.2 and 4.3 provide a summary of the number of pumps, compressors, and the number and type of vessels associated with each type of process used at natural gas processing plants. These data were used to bridge data gaps in the process equipment data collected as part of the industry survey. Equipment schedules for crude oil, HVP and LVP pipeline facilities are presented in Table 4.4, twelve modules are given for crude oil pump stations to reflect variations in the type of designs and sizes of facilities used by industry. The number of gas-operated instrument controllers assumed for each type of equipment is given in Table 4.5.

202

Table 4.1 Equipment schedules for facilities in the upstream oil and gas industry. Equipment Type Component Type Service Count Lower

UncertUpper Uncert

Adsorption Connectors Gas/Vapour 243 0.73 0.73Adsorption Controllers Fuel Gas 5 0.31 3.26Adsorption Pressure Relief Valves Gas/Vapour 8 0.51 1.96Adsorption Valves Gas/Vapour 63 0.50 0.50Adsorption Valves Light Liquid 2 0.83 1.20Absorption Connectors Gas/Vapour 200 0.73 0.73Absorption Connectors Light Liquid 46 0.90 0.90Absorption Controllers Fuel Gas 13 0.31 3.26Absorption Pressure Relief Valves Gas/Vapour 4 0.51 1.96Absorption Pump Seals Light Liquid 1 0.51 1.96Absorption Valves Gas/Vapour 82 0.50 0.50Absorption Valves Light Liquid 21 0.83 1.20Bullet Connectors Gas/Vapour 39 0.25 0.25Bullet Connectors Light Liquid 60 0.25 0.25Bullet Pressure Relief Valves Gas/Vapour 1 0.25 0.25Bullet Pressure Relief Valves Light Liquid 1 0.25 0.25Bullet Valves Gas/Vapour 15 0.25 0.25Bullet Valves Light Liquid 27 0.25 0.25Ethane Pipeline Connectors Gas/Vapour 10 0.23 0.23Ethane Pipeline Open-Ended Lines Gas/Vapour 1 0.81 1.24Ethane Pipeline Valves Gas/Vapour 3 0.28 0.28Propane Pipeline Connectors Gas/Vapour 10 0.23 0.23Propane Pipeline Open-Ended Lines Gas/Vapour 1 0.81 1.24Propane Pipeline Valves Gas/Vapour 3 0.28 0.28Butane Pipeline Connectors Gas/Vapour 10 0.23 0.23Butane Pipeline Open-Ended Lines Gas/Vapour 1 0.81 1.24Butane Pipeline Valves Gas/Vapour 3 0.28 0.28Pentanes Plus Pipeline Connectors Light Liquid 10 0.23 0.23Pentanes Plus Pipeline Open-Ended Lines Gas/Vapour 1 0.81 1.24Pentanes Plus Pipeline Valves Light Liquid 3 0.28 0.28Cold Bed Absorption Connectors Gas/Vapour 134 0.73 0.73Cold Bed Absorption Connectors Light Liquid 12 0.90 0.90Cold Bed Absorption Controllers Fuel Gas 6 0.31 3.26Cold Bed Absorption Pressure Relief Valves Gas/Vapour 1 0.51 1.96Cold Bed Absorption Valves Gas/Vapour 31 0.50 0.50Cold Bed Absorption Valves Light Liquid 7 0.83 1.20Crude Bitumen Cleaning Plant Connectors Gas/Vapour 659 0.60 0.60Crude Bitumen Cleaning Plant Connectors Heavy Liquid 362 0.55 0.55Crude Bitumen Cleaning Plant Connectors Light Liquid 1145 0.55 0.55Crude Bitumen Cleaning Plant Pressure Relief Valves Gas/Vapour 11 0.80 0.80Crude Bitumen Cleaning Plant Pressure Relief Valves Heavy Liquid 6 0.92 0.92Crude Bitumen Cleaning Plant Pressure Relief Valves Light Liquid 17 0.92 0.92Crude Bitumen Cleaning Plant Pump Seals Heavy Liquid 3 0.67 1.49Crude Bitumen Cleaning Plant Pump Seals Light Liquid 7 0.67 1.49Crude Bitumen Cleaning Plant Valves Gas/Vapour 202 0.54 0.54Crude Bitumen Cleaning Plant Valves Heavy Liquid 139 0.73 0.73Crude Bitumen Cleaning Plant Valves Light Liquid 440 0.73 0.73Centrifugal Compressor Connectors Fuel Gas 38 0.48 2.07Centrifugal Compressor Connectors Gas/Vapour 495 0.48 2.07

203

Table 4.1 Equipment schedules for facilities in the upstream oil and gas industry. Equipment Type Component Type Service Count Lower

UncertUpper Uncert

Centrifugal Compressor Connectors Light Liquid 11 0.48 2.07Centrifugal Compressor Controllers Fuel Gas 5 0.31 3.26Centrifugal Compressor Compressor Seals Gas/Vapour 2 0.48 2.10Centrifugal Compressor Open-Ended Lines Gas/Vapour 4 0.51 1.96Centrifugal Compressor Pressure Relief Valves Gas/Vapour 1 0.46 2.18Centrifugal Compressor Compressor Starts Fuel Gas 120 0.25 0.25Centrifugal Compressor Valves Fuel Gas 14 0.81 1.24Centrifugal Compressor Valves Gas/Vapour 32 0.81 1.24Centrifugal Compressor Valves Light Liquid 5 0.81 1.24Cent Comp Compressor Seals to Flare Connectors Fuel Gas 38 0.48 2.07Cent Comp Compressor Seals to Flare Connectors Gas/Vapour 495 0.48 2.07Cent Comp Compressor Seals to Flare Connectors Light Liquid 11 0.48 2.07Cent Comp Compressor Seals to Flare Controllers Fuel Gas 5 0.31 3.26Cent Comp Compressor Seals to Flare Open-Ended Lines Gas/Vapour 4 0.51 1.96Cent Comp Compressor Seals to Flare Pressure Relief Valves Gas/Vapour 1 0.46 2.18Cent Comp Compressor Seals to Flare Compressor Starts Fuel Gas 120 0.25 0.25Cent Comp Compressor Seals to Flare Valves Fuel Gas 14 0.81 1.24Cent Comp Compressor Seals to Flare Valves Gas/Vapour 32 0.81 1.24Cent Comp Compressor Seals to Flare Valves Light Liquid 5 0.81 1.24Gas-operated Chemical Pump Chemical Injection Pumps Fuel Gas 1 0.00 0.00Cond/NGL Header Tie-in Connectors Light Liquid 10 0.23 0.23Cond/NGL Header Tie-in Open-Ended Lines Gas/Vapour 1 0.81 1.24Cond/NGL Header Tie-in Valves Light Liquid 3 0.28 0.28Cond/NGL Header Tie-in Connectors Light Liquid 10 0.23 0.23Cond/NGL Header Tie-in Open-Ended Lines Gas/Vapour 1 0.81 1.24Cond/NGL Header Tie-in Valves Light Liquid 3 0.28 0.28Cond/NGL Header Tie-in Connectors Light Liquid 10 0.23 0.23Cond/NGL Header Tie-in Open-Ended Lines Gas/Vapour 1 0.81 1.24Cond/NGL Header Tie-in Valves Light Liquid 3 0.28 0.28Compressor Station Coolers Connectors Gas/Vapour 2937 0.48 2.07Compressor Station Coolers Valves Gas/Vapour 19 0.81 1.24Compressor Station Yard Piping Connectors Gas/Vapour 849 0.48 2.07Compressor Station Yard Piping Open-Ended Lines Gas/Vapour 36 0.51 1.96Compressor Station Yard Piping Pressure Relief Valves Gas/Vapour 3 0.46 2.18Compressor Station Yard Piping Valves Gas/Vapour 267 0.81 1.24Cycling Connectors Gas/Vapour 241 0.73 0.73Cycling Connectors Light Liquid 386 0.90 0.90Cycling Controllers Fuel Gas 12 0.31 3.26Cycling Compressor Seals Gas/Vapour 2 0.75 0.75Cycling Pressure Relief Valves Gas/Vapour 10 0.51 1.96Cycling Pump Seals Light Liquid 2 0.51 1.96Cycling Valves Gas/Vapour 131 0.50 0.50Cycling Valves Light Liquid 121 0.83 1.20De-butanizer Connectors Gas/Vapour 177 0.73 0.73De-butanizer Connectors Light Liquid 208 0.90 0.90De-butanizer Controllers Fuel Gas 10 0.31 3.26De-butanizer Pressure Relief Valves Gas/Vapour 6 0.51 1.96De-butanizer Pump Seals Light Liquid 2 0.51 1.96De-butanizer Valves Gas/Vapour 79 0.50 0.50De-butanizer Valves Light Liquid 80 0.83 1.20

204

Table 4.1 Equipment schedules for facilities in the upstream oil and gas industry. Equipment Type Component Type Service Count Lower

UncertUpper Uncert

Deepcut Connectors Gas/Vapour 241 0.73 0.73Deepcut Connectors Light Liquid 386 0.90 0.90Deepcut Controllers Fuel Gas 14 0.31 3.26Deepcut Compressor Seals Gas/Vapour 2 0.75 0.75Deepcut Pressure Relief Valves Gas/Vapour 10 0.51 1.96Deepcut Pump Seals Light Liquid 2 0.51 1.96Deepcut Valves Gas/Vapour 131 0.50 0.50Deepcut Valves Light Liquid 121 0.83 1.20Dessicant Dehydrator Connectors Gas/Vapour 100 0.42 0.42Dessicant Dehydrator Connectors Light Liquid 14 0.82 0.82Dessicant Dehydrator Controllers Fuel Gas 5 0.31 3.26Dessicant Dehydrator Pressure Relief Valves Gas/Vapour 1 0.83 1.20Dessicant Dehydrator Valves Gas/Vapour 24 0.53 0.53Dessicant Dehydrator Valves Light Liquid 7 0.64 1.55De-ethanizer Connectors Gas/Vapour 177 0.73 0.73De-ethanizer Connectors Light Liquid 208 0.90 0.90De-ethanizer Controllers Fuel Gas 10 0.31 3.26De-ethanizer Pressure Relief Valves Gas/Vapour 6 0.51 1.96De-ethanizer Pump Seals Light Liquid 2 0.51 1.96De-ethanizer Valves Gas/Vapour 79 0.50 0.50De-ethanizer Valves Light Liquid 80 0.83 1.20Diglycolamine Connectors Gas/Vapour 702 0.73 0.73Diglycolamine Connectors Light Liquid 3 0.90 0.90Diglycolamine Controllers Fuel Gas 13 0.31 3.26Diglycolamine Open-Ended Lines Gas/Vapour 3 0.68 1.46Diglycolamine Pressure Relief Valves Gas/Vapour 2 0.51 1.96Diglycolamine Pump Seals Light Liquid 1 0.51 1.96Diglycolamine Valves Gas/Vapour 60 0.50 0.50Diglycolamine Valves Light Liquid 1 0.83 1.20Deep Gas Well (>1000 m) Connectors Gas/Vapour 19 0.22 0.22Deep Gas Well (>1000 m) Connectors Light Liquid 1 0.51 1.96Deep Gas Well (>1000 m) Valves Gas/Vapour 6 0.17 0.17De-propanizer Connectors Gas/Vapour 177 0.73 0.73De-propanizer Connectors Light Liquid 208 0.90 0.90De-propanizer Controllers Fuel Gas 10 0.31 3.26De-propanizer Pressure Relief Valves Gas/Vapour 6 0.51 1.96De-propanizer Pump Seals Light Liquid 2 0.51 1.96De-propanizer Valves Gas/Vapour 79 0.50 0.50De-propanizer Valves Light Liquid 80 0.83 1.20Desiccant Connectors Gas/Vapour 100 0.42 0.42Desiccant Connectors Light Liquid 14 0.82 0.82Desiccant Controllers Fuel Gas 5 0.31 3.26Desiccant Pressure Relief Valves Gas/Vapour 1 0.83 1.20Desiccant Valves Gas/Vapour 24 0.53 0.53Desiccant Valves Light Liquid 7 0.64 1.55Deethanizing Connectors Gas/Vapour 177 0.73 0.73Deethanizing Connectors Light Liquid 208 0.90 0.90Deethanizing Controllers Fuel Gas 10 0.31 3.26Deethanizing Pressure Relief Valves Gas/Vapour 6 0.51 1.96Deethanizing Pump Seals Light Liquid 2 0.51 1.96

205

Table 4.1 Equipment schedules for facilities in the upstream oil and gas industry. Equipment Type Component Type Service Count Lower

UncertUpper Uncert

Deethanizing Valves Gas/Vapour 79 0.50 0.50Deethanizing Valves Light Liquid 80 0.83 1.20Electric Reciprocating Comp Connectors Gas/Vapour 275 0.18 0.18Electric Reciprocating Comp Connectors Light Liquid 2 0.77 0.77Electric Reciprocating Comp Controllers Fuel Gas 5 0.31 3.26Electric Reciprocating Comp Compressor Seals Gas/Vapour 2 0.75 0.75Electric Reciprocating Comp Open-Ended Lines Gas/Vapour 4 0.58 0.58Electric Reciprocating Comp Valves Gas/Vapour 20 0.16 0.16Electric Reciprocating Comp Valves Light Liquid 1 0.77 0.77ESD Station Connectors Gas/Vapour 10 0.73 0.73ESD Station Valves Gas/Vapour 2 0.50 0.50Fractionation Connectors Gas/Vapour 241 0.73 0.73Fractionation Connectors Light Liquid 386 0.90 0.90Fractionation Controllers Fuel Gas 12 0.31 3.26Fractionation Pressure Relief Valves Gas/Vapour 10 0.51 1.96Fractionation Pump Seals Light Liquid 2 0.51 1.96Fractionation Valves Gas/Vapour 131 0.50 0.50Fractionation Valves Light Liquid 121 0.83 1.20Flare KnockOut Drum Connectors Gas/Vapour 26 0.73 0.73Flare KnockOut Drum Connectors Light Liquid 20 0.90 0.90Flare KnockOut Drum Controllers Fuel Gas 1 0.31 3.26Flare KnockOut Drum Valves Gas/Vapour 3 0.50 0.50Flare KnockOut Drum Valves Light Liquid 1 0.83 1.20Flow Line Header Tie-in Connectors Light Liquid 10 0.23 0.23Flow Line Header Tie-in Open-Ended Lines Gas/Vapour 1 0.81 1.24Flow Line Header Tie-in Valves Light Liquid 3 0.28 0.28Flow Line Header Tie-in Connectors Light Liquid 10 0.23 0.23Flow Line Header Tie-in Open-Ended Lines Gas/Vapour 1 0.81 1.24Flow Line Header Tie-in Valves Light Liquid 3 0.28 0.28Flow Line Header Tie-in Connectors Light Liquid 10 0.23 0.23Flow Line Header Tie-in Open-Ended Lines Gas/Vapour 1 0.81 1.24Flow Line Header Tie-in Valves Light Liquid 3 0.28 0.28Flowing Oil Well Connectors Light Liquid 57 0.18 0.18Flowing Oil Well Valves Light Liquid 14 0.07 0.07Gas Boot Connectors Gas/Vapour 37 0.73 0.73Gas Boot Connectors Light Liquid 40 0.90 0.90Gas Boot Controllers Fuel Gas 1 0.31 3.26Gas Boot Valves Gas/Vapour 2 0.50 0.50Gas Boot Valves Light Liquid 2 0.83 1.20Gas-operated Chemical Pump Chemical Injection Pumps Fuel Gas 1 0.00 0.00Glycol Dehydrator Connectors Gas/Vapour 100 0.42 0.42Glycol Dehydrator Connectors Light Liquid 14 0.82 0.82Glycol Dehydrator Controllers Fuel Gas 5 0.31 3.26Glycol Dehydrator Pressure Relief Valves Gas/Vapour 1 0.83 1.20Glycol Dehydrator Valves Gas/Vapour 24 0.53 0.53Glycol Dehydrator Valves Light Liquid 7 0.64 1.55Gas-fired Unit Heater Connectors Fuel Gas 10 0.07 0.07Gas-fired Unit Heater Valves Fuel Gas 1 0.11 0.11Gas Injection Well Connectors Gas/Vapour 19 0.22 0.22

206

Table 4.1 Equipment schedules for facilities in the upstream oil and gas industry. Equipment Type Component Type Service Count Lower

UncertUpper Uncert

Gas Injection Well Valves Gas/Vapour 6 0.17 0.17Gas Line Header Tie-in Connectors Gas/Vapour 10 0.23 0.23Gas Line Header Tie-in Open-Ended Lines Gas/Vapour 1 0.81 1.24Gas Line Header Tie-in Valves Gas/Vapour 3 0.28 0.28Gas Line Header Tie-in Connectors Gas/Vapour 10 0.23 0.23Gas Line Header Tie-in Open-Ended Lines Gas/Vapour 1 0.81 1.24Gas Line Header Tie-in Valves Gas/Vapour 3 0.28 0.28Gas Line Header Tie-in Connectors Gas/Vapour 10 0.23 0.23Gas Line Header Tie-in Open-Ended Lines Gas/Vapour 1 0.81 1.24Gas Line Header Tie-in Valves Gas/Vapour 3 0.28 0.28Gas Sweetening: Amine Connectors Gas/Vapour 702 0.73 0.73Gas Sweetening: Amine Connectors Light Liquid 3 0.90 0.90Gas Sweetening: Amine Controllers Fuel Gas 13 0.31 3.26Gas Sweetening: Amine Open-Ended Lines Gas/Vapour 3 0.68 1.46Gas Sweetening: Amine Pressure Relief Valves Gas/Vapour 2 0.51 1.96Gas Sweetening: Amine Pump Seals Light Liquid 1 0.51 1.96Gas Sweetening: Amine Valves Gas/Vapour 60 0.50 0.50Gas Sweetening: Amine Valves Light Liquid 1 0.83 1.20Gas Sweetening: Sulfreen Connectors Gas/Vapour 134 0.73 0.73Gas Sweetening: Sulfreen Connectors Light Liquid 12 0.90 0.90Gas Sweetening: Sulfreen Controllers Fuel Gas 6 0.31 3.26Gas Sweetening: Sulfreen Pressure Relief Valves Gas/Vapour 1 0.51 1.96Gas Sweetening: Sulfreen Valves Gas/Vapour 31 0.50 0.50Gas Sweetening: Sulfreen Valves Light Liquid 7 0.83 1.20Gas Sweetening: Iron Sponge Connectors Gas/Vapour 134 0.73 0.73Gas Sweetening: Iron Sponge Connectors Light Liquid 12 0.90 0.90Gas Sweetening: Iron Sponge Controllers Fuel Gas 2 0.31 3.26Gas Sweetening: Iron Sponge Pressure Relief Valves Gas/Vapour 1 0.51 1.96Gas Sweetening: Iron Sponge Valves Gas/Vapour 31 0.50 0.50Gas Sweetening: Iron Sponge Valves Light Liquid 7 0.83 1.20Gas Sweetening: Sulfinol Connectors Gas/Vapour 702 0.73 0.73Gas Sweetening: Sulfinol Connectors Light Liquid 3 0.90 0.90Gas Sweetening: Sulfinol Controllers Fuel Gas 12 0.31 3.26Gas Sweetening: Sulfinol Open-Ended Lines Gas/Vapour 3 0.68 1.46Gas Sweetening: Sulfinol Pressure Relief Valves Gas/Vapour 2 0.51 1.96Gas Sweetening: Sulfinol Pump Seals Light Liquid 1 0.51 1.96Gas Sweetening: Sulfinol Valves Gas/Vapour 60 0.50 0.50Gas Sweetening: Sulfinol Valves Light Liquid 1 0.83 1.20Group Treater Connectors Gas/Vapour 178 0.21 0.21Group Treater Connectors Light Liquid 56 0.62 0.62Group Treater Controllers Fuel Gas 2 0.31 3.26Group Treater Open-Ended Lines Gas/Vapour 1 0.81 1.24Group Treater Open-Ended Lines Light Liquid 1 0.81 1.24Group Treater Valves Gas/Vapour 21 0.36 0.36Group Treater Valves Light Liquid 17 0.70 0.70Heavy Oil Cleaning Plant Connectors Gas/Vapour 137 0.60 0.60Heavy Oil Cleaning Plant Connectors Heavy Liquid 120 0.55 0.55Heavy Oil Cleaning Plant Connectors Light Liquid 237 0.55 0.55Heavy Oil Cleaning Plant Pressure Relief Valves Light Liquid 6 0.92 0.92Heavy Oil Cleaning Plant Pump Seals Heavy Liquid 2 0.67 1.49

207

Table 4.1 Equipment schedules for facilities in the upstream oil and gas industry. Equipment Type Component Type Service Count Lower

UncertUpper Uncert

Heavy Oil Cleaning Plant Pump Seals Light Liquid 2 0.67 1.49Heavy Oil Cleaning Plant Valves Gas/Vapour 40 0.54 0.54Heavy Oil Cleaning Plant Valves Heavy Liquid 52 0.73 0.73Heavy Oil Cleaning Plant Valves Light Liquid 111 0.73 0.73Heavy Oil Well - Primary Connectors Light Liquid 22 0.18 0.18Heavy Oil Well - Primary Valves Light Liquid 9 0.07 0.07Heavy Oil Well - Thermal Connectors Light Liquid 22 0.18 0.18Heavy Oil Well - Thermal Valves Light Liquid 9 0.07 0.07Heavy Oil Satellite Battery Connectors Gas/Vapour 42 0.60 0.60Heavy Oil Satellite Battery Connectors Heavy Liquid 42 0.55 0.55Heavy Oil Satellite Battery Connectors Light Liquid 84 0.55 0.55Heavy Oil Satellite Battery Pressure Relief Valves Light Liquid 1 0.92 0.92Heavy Oil Satellite Battery Pump Seals Heavy Liquid 1 0.67 1.49Heavy Oil Satellite Battery Pump Seals Light Liquid 1 0.67 1.49Heavy Oil Satellite Battery Valves Gas/Vapour 10 0.54 0.54Heavy Oil Satellite Battery Valves Heavy Liquid 13 0.73 0.73Heavy Oil Satellite Battery Valves Light Liquid 24 0.73 0.73Heavy Oil Single-Well Battery Connectors Gas/Vapour 22 0.60 0.60Heavy Oil Single-Well Battery Connectors Heavy Liquid 60 0.55 0.55Heavy Oil Single-Well Battery Connectors Light Liquid 54 0.55 0.55Heavy Oil Single-Well Battery Pressure Relief Valves Light Liquid 2 0.92 0.92Heavy Oil Single-Well Battery Pump Seals Heavy Liquid 1 0.67 1.49Heavy Oil Single-Well Battery Pump Seals Light Liquid 1 0.67 1.49Heavy Oil Single-Well Battery Valves Gas/Vapour 10 0.54 0.54Heavy Oil Single-Well Battery Valves Heavy Liquid 26 0.73 0.73Heavy Oil Single-Well Battery Valves Light Liquid 22 0.73 0.73Heat Exchanger - Gas Connectors Gas/Vapour 13 0.73 0.73Heat Exchanger - Gas Valves Gas/Vapour 7 0.50 0.50Heat Exchanger - Liquid Connectors Light Liquid 13 0.90 0.90Heat Exchanger - Liquid Valves Light Liquid 7 0.83 1.20Incinerator Connectors Gas/Vapour 10 0.07 0.07Incinerator Valves Gas/Vapour 1 0.11 0.11Catalytic Incinerator Connectors Gas/Vapour 10 0.07 0.07Catalytic Incinerator Valves Gas/Vapour 1 0.11 0.11Inlet Separator Connectors Gas/Vapour 66 0.20 0.20Inlet Separator Connectors Light Liquid 41 0.27 0.27Inlet Separator Controllers Fuel Gas 2 0.31 3.26Inlet Separator Valves Gas/Vapour 11 0.30 0.30Inlet Separator Valves Light Liquid 11 0.55 0.55Thermal incinerator Connectors Gas/Vapour 10 0.07 0.07Thermal incinerator Valves Gas/Vapour 1 0.11 0.11Joule-Thomson Refrigeration Connectors Gas/Vapour 79 0.20 0.20Joule-Thomson Refrigeration Connectors Light Liquid 41 0.27 0.27Joule-Thomson Refrigeration Controllers Fuel Gas 2 0.31 3.26Joule-Thomson Refrigeration Valves Gas/Vapour 19 0.30 0.30Joule-Thomson Refrigeration Valves Light Liquid 11 0.55 0.55Line Heater Connectors Fuel Gas 145 0.07 0.07Line Heater Connectors Gas/Vapour 40 0.07 0.07Line Heater Controllers Fuel Gas 2 0.31 3.26Line Heater Pressure Relief Valves Gas/Vapour 1 0.81 1.24

208

Table 4.1 Equipment schedules for facilities in the upstream oil and gas industry. Equipment Type Component Type Service Count Lower

UncertUpper Uncert

Line Heater Valves Fuel Gas 10 0.11 0.11Line Heater Valves Gas/Vapour 10 0.11 0.11Main Line Block Valve Connectors Gas/Vapour 30 0.73 0.73Main Line Block Valve Open-Ended Lines Gas/Vapour 1 0.68 1.46Main Line Block Valve Valves Gas/Vapour 7 0.50 0.50Metering Connectors Gas/Vapour 70 0.92 1.09Metering Pressure Relief Valves Gas/Vapour 2 0.66 1.51Metering Valves Gas/Vapour 24 0.81 1.23Main Line Meter Station Connectors Gas/Vapour 1704 0.33 0.33Main Line Meter Station Open-Ended Lines Gas/Vapour 76 0.45 2.22Main Line Meter Station Pressure Relief Valves Gas/Vapour 15 0.59 1.67Main Line Meter Station Valves Gas/Vapour 570 0.12 0.12Meter/Regulator Station Connectors Gas/Vapour 94 0.71 0.71Meter/Regulator Station Pressure Relief Valves Gas/Vapour 2 0.66 1.51Meter/Regulator Station Valves Gas/Vapour 34 0.78 0.78Meter Station Connectors Gas/Vapour 70 0.92 0.92Meter Station Pressure Relief Valves Gas/Vapour 2 0.66 1.51Meter Station Valves Gas/Vapour 34 0.81 1.23Molecular Sieve Connectors Gas/Vapour 100 0.73 0.73Molecular Sieve Connectors Light Liquid 14 0.90 0.90Molecular Sieve Controllers Fuel Gas 5 0.31 3.26Molecular Sieve Pressure Relief Valves Gas/Vapour 1 0.51 1.96Molecular Sieve Valves Gas/Vapour 24 0.50 0.50Molecular Sieve Valves Light Liquid 7 0.83 1.20Flow Line Header Tie-in Connectors Light Liquid 10 0.23 0.23Flow Line Header Tie-in Open-Ended Lines Gas/Vapour 1 0.81 1.24Flow Line Header Tie-in Valves Light Liquid 3 0.28 0.28Flow Line Header Tie-in Connectors Light Liquid 10 0.23 0.23Flow Line Header Tie-in Open-Ended Lines Gas/Vapour 1 0.81 1.24Flow Line Header Tie-in Valves Light Liquid 3 0.28 0.28Oil Pump (Recycle/Shipping) Connectors Light Liquid 10 0.55 0.55Oil Pump (Recycle/Shipping) Pump Seals Light Liquid 1 0.67 1.49Oil Pump (Recycle/Shipping) Valves Light Liquid 3 0.73 0.73Other Pumps Connectors Light Liquid 10 0.55 0.55Other Pumps Pump Seals Light Liquid 1 0.67 1.49Other Pumps Valves Light Liquid 3 0.73 0.73Process Boiler Connectors Fuel Gas 25 0.07 0.07Process Boiler Valves Fuel Gas 2 0.11 0.11Power Generator Connectors Fuel Gas 74 0.07 0.07Power Generator Valves Fuel Gas 5 0.11 0.11Pump Jack Connectors Light Liquid 57 0.18 0.18Pump Jack Pump Seals Light Liquid 1 0.48 2.08Pump Jack Valves Light Liquid 14 0.07 0.07Pop Tank (100 bbl) Connectors Light Liquid 24 0.55 0.55Pop Tank (100 bbl) Pump Seals Light Liquid 1 0.67 1.49Pop Tank (100 bbl) Valves Light Liquid 10 0.73 0.73Pop Tank (400 bbl) Connectors Light Liquid 24 0.55 0.55Pop Tank (400 bbl) Pump Seals Light Liquid 1 0.67 1.49Pop Tank (400 bbl) Valves Light Liquid 10 0.73 0.73

209

Table 4.1 Equipment schedules for facilities in the upstream oil and gas industry. Equipment Type Component Type Service Count Lower

UncertUpper Uncert

Pumping Oil Well Connectors Light Liquid 57 0.18 0.18Pumping Oil Well Pump Seals Light Liquid 1 0.48 2.08Pumping Oil Well Valves Light Liquid 14 0.07 0.07Pump Station Connectors Gas/Vapour 22 0.60 0.60Pump Station Connectors Light Liquid 647 0.55 0.55Pump Station Pressure Relief Valves Gas/Vapour 2 0.80 0.80Pump Station Pressure Relief Valves Light Liquid 17 0.92 0.92Pump Station Pump Seals Light Liquid 7 0.67 1.49Pump Station Valves Gas/Vapour 7 0.54 0.54Pump Station Valves Light Liquid 227 0.73 0.73Pig Trap Connectors Gas/Vapour 11 0.60 0.60Pig Trap Valves Gas/Vapour 3 0.54 0.54Production Tank (400 bbl) Connectors Gas/Vapour 2 0.20 0.20Production Tank (400 bbl) Connectors Light Liquid 24 0.55 0.55Production Tank (400 bbl) Pump Seals Light Liquid 1 0.67 1.49Production Tank (400 bbl) Valves Gas/Vapour 1 0.30 0.30Production Tank (400 bbl) Valves Light Liquid 10 0.73 0.73Production Tank (500 bbl) Connectors Gas/Vapour 2 0.20 0.20Production Tank (500 bbl) Connectors Light Liquid 24 0.55 0.55Production Tank (500 bbl) Pump Seals Light Liquid 1 0.67 1.49Production Tank (500 bbl) Valves Gas/Vapour 1 0.30 0.30Production Tank (500 bbl) Valves Light Liquid 10 0.73 0.73Production Tank (750 bbl) Connectors Gas/Vapour 2 0.20 0.20Production Tank (750 bbl) Connectors Light Liquid 24 0.55 0.55Production Tank (750 bbl) Pump Seals Light Liquid 1 0.67 1.49Production Tank (750 bbl) Valves Gas/Vapour 1 0.30 0.30Production Tank (750 bbl) Valves Light Liquid 10 0.73 0.73Production Tank (1000 bbl) Connectors Gas/Vapour 2 0.20 0.20Production Tank (1000 bbl) Connectors Light Liquid 24 0.55 0.55Production Tank (1000 bbl) Pump Seals Light Liquid 1 0.67 1.49Production Tank (1000 bbl) Valves Gas/Vapour 1 0.30 0.30Production Tank (1000 bbl) Valves Light Liquid 10 0.73 0.73Production Tank (2000 bbl) Connectors Gas/Vapour 2 0.20 0.20Production Tank (2000 bbl) Connectors Light Liquid 24 0.55 0.55Production Tank (2000 bbl) Pump Seals Light Liquid 1 0.67 1.49Production Tank (2000 bbl) Valves Gas/Vapour 1 0.30 0.30Production Tank (2000 bbl) Valves Light Liquid 10 0.73 0.73Prop Sweetening Connectors Gas/Vapour 200 0.73 0.73Prop Sweetening Connectors Light Liquid 46 0.90 0.90Prop Sweetening Controllers Fuel Gas 13 0.31 3.26Prop Sweetening Pressure Relief Valves Gas/Vapour 4 0.68 1.46Prop Sweetening Pump Seals Light Liquid 1 0.51 1.96Prop Sweetening Valves Gas/Vapour 82 0.50 0.50Prop Sweetening Valves Light Liquid 21 0.83 1.20Refrigeration Connectors Gas/Vapour 170 0.73 0.73Refrigeration Connectors Light Liquid 31 0.90 0.90Refrigeration Controllers Fuel Gas 6 0.31 3.26Refrigeration Compressor Seals Gas/Vapour 2 0.75 0.75Refrigeration Pressure Relief Valves Gas/Vapour 2 0.51 1.96Refrigeration Pump Seals Light Liquid 2 0.51 1.96

210

Table 4.1 Equipment schedules for facilities in the upstream oil and gas industry. Equipment Type Component Type Service Count Lower

UncertUpper Uncert

Refrigeration Valves Gas/Vapour 65 0.50 0.50Refrigeration Valves Light Liquid 13 0.83 1.20Reciprocating Compressor Connectors Fuel Gas 145 0.18 0.18Reciprocating Compressor Connectors Gas/Vapour 275 0.18 0.18Reciprocating Compressor Connectors Light Liquid 2 0.77 0.77Reciprocating Compressor Controllers Fuel Gas 5 0.31 3.26Reciprocating Compressor Compressor Seals Gas/Vapour 2 0.75 0.75Reciprocating Compressor Open-Ended Lines Gas/Vapour 4 0.58 0.58Reciprocating Compressor Compressor Starts Fuel Gas 12 0.25 0.25Reciprocating Compressor Valves Fuel Gas 6 0.16 0.16Reciprocating Compressor Valves Gas/Vapour 20 0.16 0.16Reciprocating Compressor Valves Light Liquid 1 0.77 0.77Recip Comp Compressor Seals to Flare Connectors Fuel Gas 145 0.18 0.18Recip Comp Compressor Seals to Flare Connectors Gas/Vapour 275 0.18 0.18Recip Comp Compressor Seals to Flare Connectors Light Liquid 2 0.77 0.77Recip Comp Compressor Seals to Flare Controllers Fuel Gas 5 0.31 3.26Recip Comp Compressor Seals to Flare Open-Ended Lines Gas/Vapour 4 0.58 0.58Recip Comp Compressor Seals to Flare Compressor Starts Fuel Gas 12 0.25 0.25Recip Comp Compressor Seals to Flare Valves Fuel Gas 6 0.16 0.16Recip Comp Compressor Seals to Flare Valves Gas/Vapour 20 0.16 0.16Recip Comp Compressor Seals to Flare Valves Light Liquid 1 0.77 0.77Reciprocating Compressor -Elec Connectors Gas/Vapour 275 0.18 0.18Reciprocating Compressor -Elec Connectors Light Liquid 2 0.77 0.77Reciprocating Compressor -Elec Compressor Seals Gas/Vapour 2 0.75 0.75Reciprocating Compressor -Elec Open-Ended Lines Gas/Vapour 4 0.58 0.58Reciprocating Compressor -Elec Valves Gas/Vapour 20 0.16 0.16Reciprocating Compressor -Elec Valves Light Liquid 1 0.77 0.77Reciprocating Compressor -Elec Connectors Gas/Vapour 275 0.18 0.18Reciprocating Compressor -Elec Connectors Light Liquid 2 0.77 0.77Reciprocating Compressor -Elec Open-Ended Lines Gas/Vapour 4 0.58 0.58Reciprocating Compressor -Elec Valves Gas/Vapour 20 0.16 0.16Reciprocating Compressor -Elec Valves Light Liquid 1 0.77 0.77Regulator Station Connectors Gas/Vapour 24 0.76 1.32Regulator Station Valves Gas/Vapour 10 0.98 1.02Production Tank (400 bbl) Connectors Gas/Vapour 2 0.20 0.20Production Tank (400 bbl) Connectors Light Liquid 24 0.55 0.55Production Tank (400 bbl) Pump Seals Light Liquid 1 0.67 1.49Production Tank (400 bbl) Valves Gas/Vapour 1 0.30 0.30Production Tank (400 bbl) Valves Light Liquid 10 0.73 0.73Production Tank (500 bbl) Connectors Gas/Vapour 2 0.20 0.20Production Tank (500 bbl) Connectors Light Liquid 24 0.55 0.55Production Tank (500 bbl) Pump Seals Light Liquid 1 0.67 1.49Production Tank (500 bbl) Valves Gas/Vapour 1 0.30 0.30Production Tank (500 bbl) Valves Light Liquid 10 0.73 0.73Production Tank (750 bbl) Connectors Gas/Vapour 2 0.20 0.20Production Tank (750 bbl) Connectors Light Liquid 24 0.55 0.55Production Tank (750 bbl) Pump Seals Light Liquid 1 0.67 1.49Production Tank (750 bbl) Valves Gas/Vapour 1 0.30 0.30Production Tank (750 bbl) Valves Light Liquid 10 0.73 0.73Production Tank (1000 bbl) Connectors Gas/Vapour 2 0.20 0.20

211

Table 4.1 Equipment schedules for facilities in the upstream oil and gas industry. Equipment Type Component Type Service Count Lower

UncertUpper Uncert

Production Tank (1000 bbl) Connectors Light Liquid 24 0.55 0.55Production Tank (1000 bbl) Pump Seals Light Liquid 1 0.67 1.49Production Tank (1000 bbl) Valves Gas/Vapour 1 0.30 0.30Production Tank (1000 bbl) Valves Light Liquid 10 0.73 0.73Production Tank (2000 bbl) Connectors Gas/Vapour 2 0.20 0.20Production Tank (2000 bbl) Connectors Light Liquid 24 0.55 0.55Production Tank (2000 bbl) Pump Seals Light Liquid 1 0.67 1.49Production Tank (2000 bbl) Valves Gas/Vapour 1 0.30 0.30Production Tank (2000 bbl) Valves Light Liquid 10 0.73 0.73Stabilization Connectors Gas/Vapour 80 0.48 0.48Stabilization Connectors Light Liquid 247 0.66 0.66Stabilization Controllers Fuel Gas 8 0.31 3.26Stabilization Pressure Relief Valves Gas/Vapour 3 0.51 1.96Stabilization Pump Seals Light Liquid 1 0.51 1.96Stabilization Valves Gas/Vapour 20 0.67 0.67Stabilization Valves Light Liquid 77 0.52 0.52Satellite Battery Connectors Gas/Vapour 66 0.60 0.60Satellite Battery Connectors Light Liquid 231 0.55 0.55Satellite Battery Controllers Fuel Gas 2 0.31 3.26Satellite Battery Open-Ended Lines Gas/Vapour 1 0.85 1.18Satellite Battery Open-Ended Lines Light Liquid 1 0.41 0.41Satellite Battery Pressure Relief Valves Gas/Vapour 2 0.80 0.80Satellite Battery Valves Gas/Vapour 11 0.54 0.54Satellite Battery Valves Light Liquid 57 0.73 0.73Salt Bath Heater Connectors Fuel Gas 25 0.07 0.07Salt Bath Heater Controllers Fuel Gas 1 0.31 3.26Salt Bath Heater Valves Fuel Gas 2 0.11 0.11Screw Compressor Connectors Gas/Vapour 228 0.03 0.03Screw Compressor Compressor Seals Gas/Vapour 1 0.00 0.00Screw Compressor Control Valves Gas/Vapour 1 0.53 0.53Screw Compressor Pressure Relief Valves Gas/Vapour 2 0.18 0.18Screw Compressor Pressure Regulators Gas/Vapour 2 0.53 0.53Screw Compressor Valves Gas/Vapour 35 0.22 0.22Screw Comp Compressor Seals to Flare Connectors Gas/Vapour 228 0.03 0.03Screw Comp Compressor Seals to Flare Control Valves Gas/Vapour 1 0.53 0.53Screw Comp Compressor Seals to Flare Pressure Relief Valves Gas/Vapour 2 0.18 0.18Screw Comp Compressor Seals to Flare Pressure Regulators Gas/Vapour 2 0.53 0.53Screw Comp Compressor Seals to Flare Valves Gas/Vapour 35 0.22 0.22Shallow Gas Well (<1000 m) Connectors Gas/Vapour 10 0.22 0.22Shallow Gas Well (<1000 m) Valves Gas/Vapour 3 0.17 0.17Separation Connectors Gas/Vapour 40 0.20 0.20Separation Connectors Light Liquid 58 0.27 0.27Separation Controllers Fuel Gas 3 0.31 3.26Separation Pump Seals Light Liquid 1 0.51 1.96Separation Valves Gas/Vapour 12 0.30 0.30Separation Valves Light Liquid 17 0.55 0.55Sulphur Recovery Connectors Gas/Vapour 100 0.73 0.73Sulphur Recovery Controllers Fuel Gas 2 0.31 3.26Sulphur Recovery Valves Gas/Vapour 10 0.50 0.50Single Well Oil Battery Connectors Gas/Vapour 68 0.60 0.60

212

Table 4.1 Equipment schedules for facilities in the upstream oil and gas industry. Equipment Type Component Type Service Count Lower

UncertUpper Uncert

Single Well Oil Battery Connectors Light Liquid 15 0.55 0.55Single Well Oil Battery Controllers Fuel Gas 2 0.31 3.26Single Well Oil Battery Open-Ended Lines Gas/Vapour 1 0.85 1.18Single Well Oil Battery Open-Ended Lines Light Liquid 1 0.41 0.41Single Well Oil Battery Pressure Relief Valves Gas/Vapour 1 0.80 0.80Single Well Oil Battery Pump Seals Light Liquid 1 0.67 1.49Single Well Oil Battery Valves Gas/Vapour 12 0.54 0.54Single Well Oil Battery Valves Light Liquid 21 0.73 0.73SWB With a Treater Connectors Gas/Vapour 246 0.60 0.60SWB With a Treater Connectors Light Liquid 71 0.55 0.55SWB With a Treater Controllers Fuel Gas 4 0.31 3.26SWB With a Treater Open-Ended Lines Light Liquid 1 0.41 0.41SWB With a Treater Pressure Relief Valves Gas/Vapour 2 0.80 0.80SWB With a Treater Pump Seals Light Liquid 1 0.67 1.49SWB With a Treater Valves Gas/Vapour 33 0.54 0.54SWB With a Treater Valves Light Liquid 38 0.73 0.73Storage Tank Connectors Light Liquid 12 0.55 0.55Storage Tank Valves Light Liquid 3 0.73 0.73Turbo Expander Connectors Gas/Vapour 123 0.48 2.07Turbo Expander Connectors Light Liquid 9 0.48 2.07Turbo Expander Controllers Fuel Gas 1 0.31 3.26Turbo Expander Compressor Seals Gas/Vapour 2 0.48 2.10Turbo Expander Pressure Relief Valves Gas/Vapour 6 0.46 2.18Turbo Expander Valves Gas/Vapour 48 0.81 1.24Turbo Expander Valves Light Liquid 2 0.81 1.24Tank Farm Connectors Light Liquid 190 0.55 0.55Tank Farm Pump Seals Light Liquid 6 0.67 1.49Tank Farm Valves Light Liquid 94 0.73 0.73Tail Gas Cleanup Connectors Gas/Vapour 25 0.73 0.73Tail Gas Cleanup Valves Gas/Vapour 5 0.50 0.50Tank Heater Connectors Fuel Gas 10 0.07 0.07Tank Heater Connectors Light Liquid 2 0.51 1.96Tank Heater Valves Fuel Gas 2 0.11 0.11Pump Station Tanks Connectors Light Liquid 12 0.55 0.55Pump Station Tanks Valves Light Liquid 3 0.73 0.73Pipeline Terminal Tanks Connectors Light Liquid 12 0.55 0.55Pipeline Terminal Tanks Valves Light Liquid 3 0.73 0.73Test Separator Connectors Gas/Vapour 49 0.54 0.54Test Separator Connectors Light Liquid 25 0.40 0.40Test Separator Controllers Fuel Gas 2 0.31 3.26Test Separator Pressure Relief Valves Gas/Vapour 1 0.70 1.42Test Separator Valves Gas/Vapour 15 0.50 0.50Test Separator Valves Light Liquid 15 0.59 0.59Test Treater Connectors Gas/Vapour 178 0.21 0.21Test Treater Connectors Light Liquid 56 0.62 0.62Test Treater Controllers Fuel Gas 2 0.31 3.26Test Treater Open-Ended Lines Gas/Vapour 1 0.81 1.24Test Treater Pressure Relief Valves Gas/Vapour 1 0.70 1.42Test Treater Valves Gas/Vapour 21 0.36 0.36Test Treater Valves Light Liquid 17 0.70 0.70

213

Table 4.1 Equipment schedules for facilities in the upstream oil and gas industry. Equipment Type Component Type Service Count Lower

UncertUpper Uncert

Tank Farm Tanks Connectors Light Liquid 12 0.55 0.55Tank Farm Tanks Valves Light Liquid 3 0.73 0.73Utility Boiler Connectors Fuel Gas 25 0.07 0.07Utility Boiler Valves Fuel Gas 2 0.11 0.11Unit Heater Connectors Fuel Gas 10 0.07 0.07Unit Heater Connectors Light Liquid 2 0.51 1.96Unit Heater Valves Fuel Gas 2 0.11 0.11Vapour Recovery Compressor Connectors Gas/Vapour 25 0.18 0.18Vapour Recovery Compressor Connectors Light Liquid 2 0.77 0.77Vapour Recovery Compressor Controllers Fuel Gas 1 0.31 3.26Vapour Recovery Compressor Compressor Seals Gas/Vapour 1 0.75 0.75Vapour Recovery Compressor Valves Gas/Vapour 5 0.16 0.16Vapour Recovery Compressor Valves Light Liquid 3 0.77 0.77Water Pump (Recycle/Shipping) Connectors Light Liquid 5 0.55 0.55Water Pump (Recycle/Shipping) Pump Seals Light Liquid 1 0.67 1.49Water Pump (Recycle/Shipping) Valves Light Liquid 2 0.73 0.73

214

Table 4.2 Summary of the number of vessels, compressors and pumps associated with

various natural gas processes. Process Vessels Compressors Pumps Absorption 13 0 1 Adsorption 5 1 0 Chemsweet 5 1 0 Cold Bed Absorption 6 0 0 Compression 4 1 0 Cycling 12 1 2 DEA – Diethanolamine 13 0 1 DGA – Diglycolamine 13 0 1 Deepcut 14 1 2 Deethanizing 10 1 2 Dehydration 5 1 0 Demethanizing 10 1 2 Desiccant 5 1 0 Dewpoint 6 2 2 Fractionation 12 1 2 Iron Sponge 6 0 0 LoCat 5 1 0 MCRC – Sub-dewpoint sulphur recovery 6 0 0 MDEA – Monodiethanolamine 13 0 1 MEA – Monoethanolamine 13 0 1 Molecular Sieve 5 1 0 NGL – Natural gas liquid 14 1 2 Physical Solvent 12 1 1 Proprietary Sweetening 13 0 1 Refrigeration 6 2 2 Selexol 12 1 1 Separation 3 0 1 Sluri-sweet 13 0 1 Stabilization 8 0 1 Sulfacheck 12 1 1 Sulfinol 12 1 1 Sulfreen 6 0 0 Sweetening 13 0 1 Turbo Expander 1 1 0

215

Table 4.3 Summary of the types of vessels associated with various natural gas

processes.

Process Vessels Potential VOC Source Vessels Absorption DEA Sweetening DGA Sweetening MDEA Sweetening Proprietary Sweetening Slurri-Sweet Sweetening

13 Inlet Gas Scrubber (1), Contactor (1), Flash Drum (1), Regenerator Overhead Condenser (1), Regenerator Reflux Drum (1), Exchanger (2), Condensate Drum (2), Outlet Separator (1), Regenerator (1), Regenerator Reboiler (2)

Adsorption Chemsweet Dehydration Desiccant LoCat Molecular Sieve

5 Feed Separator (1), Dehydration Tower (2), Regeneration Gas Separator (1), Regeneration Gas Cooler (1)

Cold Bed Absorption Iron Sponge MCRC Sulfreen

6 Acid Gas Scrubber (1), Acid Gas Burner (1), Waste Heat Boiler (1), Tail Gas Coalescer (1), Reaction Furnace (1), Tail Gas Incinerator (1)

Compression 4 Suction Scrubber (1), Interstage Scrubber (1), Intercooler (1), Knock-out drum (1)

Claus Sulphur Recovery 4 Knock-out drum (1), Reaction Furnace (1), Acid Gas Burner (1), Waste Heat Boiler (1)

Cycling Fractionation

12 Fractionation Column (3), Reboiler (3), Air Cooler (2), Separator (3), Heat Exchanger (1)

Deepcut NGL

14 Separator (1), Heat Exchanger (4), Chiller (1), Condenser (2), Reboiler (2), Fractionation Column (2), Reflux Accumulator (1), Reboiler Condensate Drum (1)

Deethanizing Demethanizing

10 Separator (1), Heat Exchanger (2), Chiller (1), Condenser (2), Reboiler (1), Fractionation Column (1), Reflux Accumulator (1), Reboiler Condensate Drum (1)

Physical Solvent Selexol Sulfacheck Sulfinol

12 Flash Tank (4), Heater (2), Cooler (2), Contactor (1), Stripper (1), Separator (2)

Refrigeration Dewpoint

6 Suction Scrubber (1), Chiller (1), Heat Exchanger (1), Condenser (1), Accumulator (1), Reclaimer (1)

Separation 3 Separator (1), Flash Drum (1),Cooler (1) Stabilization 8 Stabilizer Feed Drum (1), Stabilizer (1), Reboiler (2),

Overhead Condenser (1), Reflux Drum (1), Exchanger (2)

Turbo Expander Inlet Separator (1)

216

Table 4.4 Summary of equipment schedules used for facilities on crude oil, HVP and LVP pipelines.

Number of Emission Sources Associated with the

Facility Gas Service Liquid Service Product Facility

V1 C2 PRV3 V C PRV PS4 Tank Farm 0 0 0 94 190 0 6Pipeline Terminal

0 0 0 525 1 933 19 10

Pump Station (Module 1)

0 0 0 97 363

0 7

(Module 2) 0 0 0 37 124 0 1(Module 3) 0 0 0 12 38 0 2(Module 4) 0 0 0 21 37 0 2(Module 5) 0 0 0 20 52 0 2(Module 6) 0 0 0 43 109 4 2(Module 7) 0 0 0 123 315 5 6(Module 8) 8 34 0 191 501 4 12(Module 9) 32 88 12 461 1 397 43 3(Module 10) 23 71 3 454 1 290 36 14(Module 11) 0 0 0 281 898 12 5

Crude Oil

(Module 12) 2 13 1 479 1 280 46 16HVP5 Pump Station

(Module 8)

0 0 0 64 142

2 3Tank Farm 0 0 0 9 32 0 1Pipeline Terminal

0 0 0 42 108 0 2LVP6

Pump Station 0 0 0 7 24 0 11 Valves 2 Connectors 3 Pressure Relief Valves 4 Pump Seals 5 High Vapour Pressure Products (e.g., ethanes, propanes and butanes) 6 Low Vapour Pressure Products (e.g., pentanes-plus)

217

Table 4.5 Summary of the number of instrument controllers assumed for different types

of equipment. Equipment Number of Instrument Controllers Compressor 3 Dehydrator 3 Line Heater 1 Separator 1 Treater 2 Inlet Separator 3 Note: In addition to the controllers on the inlet separator and any compressors present, one controller per vessel is

assumed for gas plants.

218

5.0 UNCERTAINTY DATA Uncertainties associated with the average emission factors for estimating emissions from fugitive equipment leaks are presented in Tables 3.1 and 3.2 for gas production/processing facilities and oil production facilities, respectively. The uncertainties for equipment schedules are in Table 4.1 and those for combustion emission factors are in Table 3.3. Production volume uncertainties are provided in Table 5.1. Table 5.2 lists a number of other quantities used in emission calculations and their assumed uncertainty limits. Table 5.1 Compilation of uncertainties associated with production volumes.

Facility Type Quantity Production Volume Range Uncertainty (±%)

< 100 m3/d 1 Oil Production > 100 m3/d 0.5 >500 m3/d 3 > 500 m3/d flared 5

Oil Batteries1

Gas Production

< 500 m3/d 20 >30 m3/d 5 >6 and ≤30 m3/d 10 >2 and ≤6 m3/d 20

Oil Proration1 Oil Production

≤2 m3/d 40 Gas Production/ Processing1

Gas production All 3

Gas Proration1 Gas Production All 15 Flared Volumes2 All 15 Fuel Volumes2 All 15 Propane Fuel3 All 25 Reported Venting Based on Company GOR3 25

All Facilities

Based on Provincial Average GOR3 50 1 Based on measurement accuracy requirements outlined in EUB ID 94-1. 2 IPCC (2000) Good Practice Guidance and Uncertainty Management. 3 Based on engineering judgement and industry consultations.

219

Table 5.2 Compilation of uncertainties used in GHG and CAC emission estimation

calculations.

Item Description Uncertainty (±%)

From industry survey 10 From government or industry publications 25

Number of Specific Equipment Items at a Site

Assumed based on typical facility layouts 100 Speciation Profiles Individual species mole fractions 10 Stream Molecular Weights Calculated from speciation profiles 10 Stream High Heating Value Calculated from speciation profiles 10 Fuel Proration Calculated fraction of fuel associated with

each gas fired unit at a site 25

Glycol Dehydrators Emission Factors 25 Emission Factors 25 Vapour Pressures 25

Loading/Unloading

Loading Temperature 10 Storage Tanks Vapour Pressures 25 Emission Factors (flashing losses) 13.6 Storage Temperature 25 Drilling/Service Diesel fuel consumption 25

H2S Concentration 25 Sour Gas Flaring/Incineration Sulphur Recovery Efficiency 25

Sulphur Production Emission Factor 25