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    GMRC Eng ine Ana ly zer & Re l iab i l i t y W or k shopNashville, TN

    July 27-29, 2011

    COMPRESSOR EMI SSI ONS

    TECHNOLOGY REVI EW

    Cra ig Mar t inApplications Engineering Supervisor

    Aleksey Dubrov enskyProject Engineer

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    Pot en t ia l Leak Po in t s

    Oil WiperPacking

    Packing CaseNose Gasket

    Between Packing Case Cups

    Distance PieceVent/Drain

    Outer Head

    Gasket

    Valve CoverGasket

    Valve UnloaderPacking

    Packing Case Vent

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    Pack in g Leak age Fact or s

    Failure to account for em issions escap ing in t o t hed is t ance p iece may result in underestimation of

    packing related emissions by up to 4 0 % .- U.S. EPA Natural Gas STAR Reducing Methane Emissions From Compressor Rod

    Packing Systems, July 2003

    + + + + + =LEAKAGE AT

    FRAMEBREATHER

    LEAKAGE AT

    SECONDARYDISTANCEPIECE VENT

    LEAKAGE AT

    DISTANCEPIECE DRAIN

    LEAKAGE AT

    DISTANCEPIECE VENT

    LEAKAGE AT

    PACKING CASE

    LEAKAGE AT

    VALVEUNLOADERPACKING

    TOTALLEAKAGE

    SECONDARY DISTANCEPIECE DRAIN

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    New Em issions Regu lat ions

    EPA: Best Available Measurement Methods must beused to measure all greenhouse gas (GHG) emissions

    Required by July 31st or September 30th, 2011

    Petroleum & Natural Gas Systems of the Greenhouse Reporting Rule:Subpart W (40 CFR Parts 98)

    EPA defines GHG as any gas that absorbs infraredradiation

    Water vapor

    CH4

    N2O

    CFCs

    SF6

    CO2 HCFCs

    HFCs

    PFCs

    1

    Source: EPA Climate Change Directory http://www.epa.gov/climatechange/index.html1

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    For ces Dr iv in g Em ission s Redu ct ion s

    New emissions regulations

    Currently limited to emissions measurement

    Possibly future cap-and-trade restrictions on emissions

    Economics

    Lost production is very costly

    Payback on upgrades typically less than one year

    Reliability Increase lifecycle of equipment

    Operating efficiency becoming a competitive necessity

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    Em ission s Man agem ent

    Vapor Recovery System

    Channel emissions back to a controlled source

    Can be expensive and complicated

    Modify Existing Packing Case to Reduce Leakage WAT ring used to restrict gas flow into the vent

    Field testing confirms low leakage

    Additional frictional heat loading on piston rod

    Application temperatures should be reviewed

    Low-Friction Seal Technology

    Low Leak Packing Technology

    Possibly able to utilize existing cases Documented results from years of field applications

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    WAT Ring

    Side-loaded ring, single-acting

    Seals well at low pressures

    Vent Rin gs

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    Tr ad i t ion a l Pack in g Seal Rin gs

    Basic functionality of a single-acting seal ring:

    During discharge stroke, high pressure gas enterspacking case

    Pressure loads ring against sealing surfaces

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    Traditional setup

    Several seal rings

    Standard vent seal

    Outdated design

    St an dar d Pr essu r e Pack in g

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    Low Leak Pack in g Tech n o log y

    More effective seals

    Fewer rings required

    Years of documented field results

    Near-zero leakage

    Longer packing life

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    Seal Rin gs

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    Seal Rin gs

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    Seal Rin gs

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    Seal Rin gs

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    100

    150

    200

    250

    300

    350

    0 500 1000 1500 2000 2500 3000 3500

    DISCHARGE PRESSURE ~ PSI

    RODTEMPERATURE~F

    Conventional Packing

    Low Leak Technology

    Pist on Rod Tem per a t u r e

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    WAT Ring

    Side-loaded ring, single-acting

    Seals well at low pressures

    Vent Rin gs

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    Ven t Seal Rin gs

    Vent Seal RingUpstream of Vent

    Typical Low LeakPacking Design

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    Pist on Rod Tem per a t u r e:

    Vent -Seal Ring Ups t r eam o f Ven t Cu p

    0

    100

    200

    300

    400

    Standard Packing Vent Seal Ring Upstreamof Vent Cup

    Tempera

    ture(F)

    Test 1

    Test 2Test 3

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    Low - Fr ict ion Seal Tech n o log y

    Restricts gas flow into the vent

    Reduced frictional heat on piston rod

    Friction causes increased piston rod temperatures

    Increased leakage rates

    Decreased packing lifespan

    Controls leakage in standby mode

    Confirmed field and lab results

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    FI ELD DATA

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    Static cylinders can resultin significant leakage Cylinder 1 8.93 SCFM

    $38,675 / yr (based on$8 / decatherm)

    * Year based on8,760 run hours

    Std. BronzeLow Leak

    Low Leak

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    It is possible to obtain lowrates (~0.1 SCFM) in

    running conditions.

    Leak rates are below 0.1

    SCFM

    * Year based on8,760 run hours

    Low Leak

    Low LeakStd. Bronze

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    A small number of cylinderscan cause a large amount of

    the total leakage.

    96% of the total packing leakagecomes from Cylinder 1 24

    SCFM - ~$100K / yr!

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    Distance Piece leakage cancontribute a significant amount

    to the total leakage.

    23% of the total leakageis coming from thedistance piece vent

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    Unknown packing and Low Leak packing maintained

    low leak rates. Standard bronze packing hasdeveloped a moderate leak at 12,900 hours.

    Std.

    Low Leak =

    Low Leak =

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    Cu m u la t i ve Leak age Com par ison

    The area under the curve represents the totalleakage throughout the life of the packing

    STANDARD

    UpgradedPacking Case

    Low LeakTechnology

    Standard PackingSeal Rings

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    STANDARD

    Cu m u la t i ve Leak age Com par ison

    The area under the curve represents the totalleakage throughout the life of the packing

    UpgradedPacking Case

    Low LeakTechnology

    Standard PackingSeal Rings

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    STANDARD

    Cu m u la t i ve Leak age Com par ison

    The area under the curve represents the totalleakage throughout the life of the packing

    UpgradedPacking Case

    Low LeakTechnology

    Standard PackingSeal Rings

    Jus t i f i ca t ionfo r Pack in g

    Rep lacement

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    Packing case maintenance

    Upgrade nose gasket to a spiral wound gasket

    Replace existing BD vent rings to a WAT

    Lap cups 4 light bands flatness

    Verify parallelism of cup faces

    Within .001

    Verify cup depths & ring clearances Verify rod surface finish

    8-12 Ra for induction-hardened rod

    6-8 Ra for TC-coated or nitrided rod

    Verify packing case alignment Ensure proper bolt tightening procedures

    Best Pr act ices

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    CASE STUDI ES

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    Case St u d y I

    Measured packing vent flow

    Two identical H2 machines

    Five-throw Worthington BDCs

    Utilized thermal mass flow meterto gather emissions data

    Provided options for emissions

    measurement

    Permanent installation

    Portable installation

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    Resul ts

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    Case St u dy I I

    24 cylinders

    Standard packing

    Measured packing vent leakage on-site

    Changed all cases over to Low Leak technology

    Measured leakage after upgrades

    Below measurable range of flow meter

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    Leak age Com par ison ( SCFM)

    0.0

    0.5

    1.0

    1.5

    2.0

    2.5

    3.0

    Low Leak StandardLeakage

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    OTHER EMI SSI ONS

    SOURCES

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    Dr esser Ran d KVR Un loader

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    Before After

    Air Cylinder

    Rope Packing

    Seal

    Cartridge

    Plug

    Actuator Rod

    Indicator Pin

    Up gr ade t o Seal Car t r idg e

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    Com pr essor Va lve

    Un load er & Act u at o r

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    Jack Bo l t St y le Ret a iner s

    Poor sealingaround the jack

    bolt results infugitiveemissions, whichcan be hazardous

    to people and theenvironment

    Potential Leak

    Hi h S h R i

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    High St r en g t h Ret a in er

    Replace the single jam nutwith a multiple jam nutdesign

    O-ring around the cagejack bolt provide superiorsealing

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    Th an k You !