const completion report
TRANSCRIPT
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CONSTRUCTION COMPLETION REPORT
SOIL VAPOR EXTRACTION & AIR SPARGE SYSTEM
ACME SOLVENT RECLAIMING, INC. SITE
ROCKFORD, ILLINOIS
Prepared For:
Acme-Rockford Group
Prepared By:
MWH Americas, Inc.
175 West Jackson Blvd., Suite 1900Chicago, Illinois 60604
MWH File No. 1009103
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TABLE OF CONTENTS
1.0 INTRODUCTION ................................................................................................... 4
1.1 Purpose....................................................................................................................... 4
1.2 Objectives .................................................................................................................. 4
1.3 Project Organization .................................................................................................. 5
1.4 Project Team Work Responsibilities ......................................................................... 5
2.0 SUMMARY OF CONSTRUCTION ACTIVITES ............................................... 7
2.1 Health and Safety ....................................................................................................... 7
2.2 Site Security ............................................................................................................... 7
2.3 Site Preparation .......................................................................................................... 7
2.4 Air Permit .................................................................................................................. 7
2.5 Site Surveys ............................................................................................................... 7
2.6 Well Installation ......................................................................................................... 8
2.6.1 SVE Wells...................................................................................................... 8
2.6.2 Air Sparge Points ........................................................................................... 8
2.6.3 Vapor Monitoring Points ............................................................................... 9
2.7 Conveyance Hose and Manifold ................................................................................ 9
2.8 Equipment Installation ............................................................................................... 9
2.8.1 Equipment Building ..................................................................................... 10
2.8.2 Oxidizer ....................................................................................................... 11
2.8.3 Control System ............................................................................................ 11
2.8.4 Telemetry System ........................................................................................ 11
2.8.5 Security Camera ........................................................................................... 12
2.9 Utilities..................................................................................................................... 12
2.10 System Commissioning & Startup ........................................................................... 12
2.10.1 Oxidizer Performance Sampling .................................................................. 12
2.10.2 Compliance Air Sampling ........................................................................... 13
2.11 Waste Disposal ........................................................................................................ 13
2.12 As-Built Drawings ................................................................................................... 14
3.0 REFERENCES ...................................................................................................... 15
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LIST OF TABLES
Table 1 Thermal Oxidizer Results for Method TO-15 (VOCs)
LIST OF FIGURES
Figure 1 Site Location Map
LIST OF APPENDICES
Appendix A Photographic Log
Appendix B As-built DrawingsB1 – MWH’s Construction As-Built Drawings
B2 – Maple Leaf Environmental Equipment’s As-Built Drawings
B3 – Intellishare’s As-Built Drawings
Appendix C Well Construction Diagrams
Appendix D Analytical Data
D1 - Air Sampling Analytical ResultsD2 - Soil Sampling Analytical Results
D3 - Purge Water Sampling Analytical Results
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LIST OF ACRONYMS AND ABBREVIATIONS
AS Air Sparge
Ballard Ballard Companies, Inc. bgs Below Ground surface
CCR Construction Completion ReportFirst Environmental First Environmental Laboratories, Inc.
GAC Granular Activated Carbon
GPM Gallons Per Minute
HASP Health and Safety PlanHOA Hand/off/auto
HP Horsepower
IEPA Illinois Environmental Protection AgencyIntellishare Intellishare Environmental Clean Air Solutions
JULIE Joint Utility Locating Information for ExcavatorsKVA Kilovolt-AmpereMidwest Midwest Mechanical Works, Inc.
Missman Stanley Missman Stanley & Associates, P.C.
MLEE Maple Leaf Environmental Equipment Inc.
MWH MWH Americas, Inc. Nicor Nicor, Inc.
PLC Programmable Logic Controller
PVC Polyvinyl chlorideRAP Remedial Action Plan
RAWP Remedial Action Work Plan
RDR Remedial Design ReportRDWP Remedial Design Work Plan
ROR Remedial Objectives ReportRPM Revolutions Per Minute
SCFM Standard cubic feet per minute
SIR Site Investigation ReportSite Acme Solvent Reclaiming, Inc. Site in Rockford, Illinois
SRO Site Remediation Objectives
SVE Soil Vapor Extraction
TACO Tiered Approach to Corrective Action ObjectivesTSC Testing Service Corporation
USEPA United States Environmental Protection AgencyVAC Voltage Alternating CurrentVLS Vapor Liquid Separator
VMPs Vapor Monitoring Points
VOCs Volatile organic compounds
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1.0 INTRODUCTION
1.1 PURPOSE
MWH Americas, Inc. (MWH) is a consultant for the Acme-Rockford Group, an
unincorporated association of parties allegedly liable for response action at the Acme SolventReclaiming, Inc. Site in Rockford, Illinois (Site). The Site location is shown in Figure 1.
The purpose of this report is to document the remedial system construction activities
performed at the Site. This report presents a summary of construction activities and as-builtdrawings for the full-scale soil vapor extraction (SVE) and air sparge (AS) systems.
Construction activities detailed in this report were performed in accordance with the
specifications of the Remedial Action Work Plan (RAWP) (MWH, December 2009).
This Construction Completion Report (CCR) was prepared utilizing information from thefollowing documents that are also listed in the reference section of this report:
• Site Investigation Report (SIR) (MWH, 2007)
• Remedial Objectives Report (ROR) (MWH, 2007)
• Remedial Action Plan (RAP) (MWH, 2008)
• Remedial Design Report (RDR) (MWH, 2009)
• Remedial Design Work Plan (RDWP) (MWH, 2009)
• Remedial Action Work Plan (RAWP) (MWH, 2009)
1.2 OBJECTIVES
The objectives of the remedial activities for the Site, as outlined in the ROR are to:
• Prevent potential human contact with contaminated groundwater through the institution
of a municipal ordinance to prohibit usage of groundwater in or from the groundwater
contaminant plume beneath and downgradient from the Site;
• Remediate contaminated soil to below Site specific Tier 2 Soil Remediation Objectives(SROs) for the soil component of the groundwater ingestion exposure route;
• Remediate contaminated soil to below the Tiered Approach to Corrective ActionObjectives (TACO) Tier 1 values for the ingestion exposure route;
• Remediate contaminated soil to below the TACO Tier 1 values for the inhalation
exposure route;
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• Evaluate residual concentrations of volatile organic compounds (VOCs) in the soil by
conducting confirmation soil sampling after the extracted vapors, sampled by a photoionization detector, shows that the VOC removal rate has reached asymptotic
concentrations;
• Monitor remedial progress by measuring total mass removed by the SVE/AS system;
and
• Provide a report to the Illinois Environmental Protection Agency (IEPA) summarizing
the history of operation of the SVE/AS system and tables summarizing the
confirmation soil sampling results and the mass removal sampling results. The reportwill be prepared when mass removal rate has reached an asymptotic state.
SROs for the chemicals of potential concern at the Site are listed in Table 8 of the ROR. Soil
confirmation samples will be collected by geoprobe at eight locations shown on Figure 9 of
the ROR and will be analyzed for VOCs. All of the objectives listed above are defined ingreater detail in Section 3.2 of the ROR.
1.3 PROJECT ORGANIZATION
MWH was retained by the Acme Rockford Group as the general remediation contractor for
this project. MWH retained the following subcontractors:
Company: Role:
JB Lawn Care LandscapingMissman Stanley & Associates, P.C. (Missman Stanley) Surveyors
Testing Service Corporation (TSC) Drillers
Midwest Mechanical Works, Inc. (Midwest) Mechanical
Ballard Companies, Inc. (Ballard) ElectricalFirst Environmental Laboratories, Inc. Soil/Water Laboratory
Stat Analysis Corporation Air Laboratory
The following personnel were involved in the Acme remediation project to date:
Name: Title: Organization:
Andrew Frierdich Project Manager IEPA
Peter Vagt Project Manager MWH
Chris Daly Licensed Project Engineer MWH
Robert Larrabee Construction Project Manager MWHJustin Finger Field Technician MWH
Denise Garcia Field Engineer MWH
1.4 PROJECT TEAM WORK RESPONSIBILITIES
MWH oversaw the construction of the SVE/AS system and the commissioning of the
SVE/AS system. Maple Leaf Environmental Equipment’s, Inc. (MLEE’s) out of Brockville,
Ontario, engineered the SVE/AS system and pre-assembled the equipment building
components and the logic control panel. MLEE’s SVE system included a thermal oxidizer
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that was engineered and manufactured by Intellishare Environmental Clean Air Solutions out
of Menomonie, Wisconsin. The oxidizer was assembled on Site and integrated electricallyand mechanically with the equipment building and utilities.
The mechanical contractor, Midwest of Byron, Illinois and electrical contractor, Ballard of
Rockford, Illinois assisted with placement and assembly of the equipment building andoxidizer. Ballard installed the electrical wiring for all the oxidizer’s sensor switches,
thermocouples, temperature and pressure gauges and installed conduit and electrical cable to
the control panel located inside the equipment building. Midwest installed the equipment building and installed the vapor conveyance piping, natural gas piping, and SVE extraction
conveyance hosing.
MLEE performed system integration and commissioning activities from
October 18 to 21, 2010.
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2.0 SUMMARY OF CONSTRUCTION ACTIVITES
This section describes the tasks conducted by MWH and its subcontractors as part of the
construction activities associated with the installation of the SVE/AS systems at the Site.
Construction began on September 10, 2010 and was completed on October 18, 2010.Commissioning of the SVE system occurred during October 18 thru 21, 2010. The system
formally began operations on October 21, 2010.
A photographic log is included in Appendix A and the as-built record drawings are included
in Appendix B.
2.1 HEALTH AND SAFETY
The Health and Safety Plan (HASP) associated with the construction activities for the
SVE/AS remedial systems is provided in the RAWP (MWH, December 2009).
2.2
SITE SECURITY
A chain-link fence was installed along the perimeter of the Site during pilot study activities
in 2009. An informational sign was posted at the northwest and east sides of the fence thatdirected the public to the Rockford Public Library and the ACMEcleanup.com website for
more information.
2.3 SITE PREPARATION
To allow access to the locations of SVE/AS wells, the equipment building, and the oxidizer,
the Site was prepared by removing oversized brush and mowing grassy areas. This task was
performed on September 10, 2010.
Prior to drilling activities, a Joint Utility Locating Information for Excavators (JULIE)
request provided utility location information.
2.4 AIR PERMIT
The IEPA air permit was issued October 12, 2010 for 12-month operation of the full scale
SVE system controlled by an oxidizer. Guidelines and compliance sampling requirementsoutlined in the permit were followed during the system commissioning and monthly
monitoring activities.
2.5
SITE SURVEYSOn September 13, 2010, Missman Stanley of Rockford, Illinois was at the Site to conduct
surveying activities. Missman Stanley surveyed the proposed locations and grade elevations
for the SVE wells, AS wells, vapor monitoring points (VMPs), the equipment building, andthe oxidizer.
On January 5, 2011, Missman Stanley returned to the Site and surveyed as-built locationsand grades of the SVE wells, AS wells, VMPs, equipment building, and oxidizer.
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2.6 WELL INSTALLATION
The SVE wells, AS wells and VMPs were installed from September 22, 2010 toOctober 1, 2010 by TSC. The well installation activities were overseen by a MWH field
technician.
2.6.1 SVE Wells
The SVE well locations are shown on Sheet 4 of Appendix B-1. Well construction diagrams
are provided in Appendix C. Two wells, SVE-01S and SVE-02D, were installed during the pilot study in 2009 and have been incorporated into the full-scale SVE system. A total of 21
SVE wells are utilized for vapor extraction in this SVE/AS system.
In 2010, 19 SVE wells (SVE-03S through SVE-22D) were installed with a 4¼-inch (inner
diameter) hollow-stem auger resulting in an eight-inch borehole. The wells were constructed
with three-inch diameter polyvinyl chloride (PVC) pipe with three-inch diameter PVCscreens placed at the bottom of each SVE boring. The screens were ten-feet in length with a
slot size of 0.010-inches. The annular space within the borehole was filled from the bottomto one foot above the top of the screen with silica sand. A one-foot thick seal of 3/8-inch bentonite chips was installed above the sand pack, and the remainder of the annular space
above the bentonite seal to the ground surface was filled with 20 percent solids bentonite
grout.
The following nine SVE wells (SVE-03S, SVE-04S, SVE-05S, SVE-06S, SVE-07S,
SVE-08S, SVE-09S, SVE-10S and SVE-11S) are screened in the shallow sandy layer with
total well depths between 19 and 21 feet below ground surface (bgs), and are defined asshallow wells.
The following ten SVE wells (SVE-12D, SVE-13D, SVE-14D, SVE-15D, SVE-16D,SVE-17D, SVE-18D, SVE-19D, SVE-20D and SVE-21D) are screened in the deep sandy
layer with total well depths between 33 and 35 feet bgs, and are defined as deep wells.
2.6.2 Air Sparge Points
AS well locations are shown on Sheet 4 of Appendix B-1. Well construction diagrams are
provided in Appendix C. One AS well, AS-01, was installed during the pilot study in 2009 at
an approximate depth of 42 feet bgs and has been incorporated into the full-scale system. Atotal of four AS wells are utilized for air sparging locations in this SVE/AS system.
In 2010, three AS wells (AS-02, AS-03 and AS-04) were constructed with two-inch diameter
PVC pipe to a depth of approximately 42 feet bgs. A four-foot screen with a slot size of0.010-inches was installed at the bottom of each well. The AS points were installed with a
4¼-inch (inner diameter) hollow-stem auger resulting in an eight-inch borehole. The annular
space within the borehole was filled from the bottom to one foot above the top of the screenwith silica sand. A one-foot thick seal of 3/8-inch bentonite chips was installed above the
sand pack, and the remainder of the annular space above the bentonite seal to the ground
surface was filled with 20 percent solids bentonite grout.
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2.6.3 Vapor Monitoring Points
The VMP locations are shown on Sheet 4 of Appendix B-1. Well construction diagrams are
provided in Appendix C. VMP-01S, VMP-02S, VMP-03D, and VMP-04D were installedduring the pilot study in 2009 and have been incorporated into the full-scale system. A total
of 12 VMP locations are utilized to monitor the radius of influence of the applied vacuum
across this SVE/AS system.
In 2010, eight additional vapor monitoring points (VMP-05S, VMP-06S, VMP-07S, VMP-
08D, VMP-09D, VMP-10D, VMP-11D, and VMP-12D) were installed to monitor the radiusof influence of the applied vacuum of the SVE system and were installed at varying distances
from the SVE wells. The VMPs were constructed of one-inch diameter PVC and installed
with two-inch diameter flight auger resulting in a four-inch borehole. A one-foot screen with
slot size of 0.010-inches was installed at the bottom of each VMP. The annular space withinthe borehole was filled from the bottom to one foot above the top of the screen with silica
sand. A one-foot thick seal of 3/8-inch bentonite chips was installed above the sand pack,
and the remainder of the annular space above the bentonite seal to the ground surface was
filled with 20 percent solids bentonite grout.
The shallow VMP points are screened from approximately nine to ten feet bgs and include
VMP-01S, VMP-02S, VMP-05S, VMP-06S and VMP-07S.
The deep VMP points are screened from approximately 29 to 30 feet bgs and include
VMP-03D, VMP-04D, VMP-08D, VMP-09D, VMP-10D, VMP-11D, and VMP-12D.
2.7 CONVEYANCE HOSE AND MANIFOLD
The AS and SVE conveyance hoses are two-inch flexible PVC hose with cam-lock fittings.
The conveyance hoses were installed by Midwest above grade and connect each well to amanifold located inside the equipment building. Inside the equipment building, each
SVE well has a dedicated riser pipe with a sample port, vacuum gauge, and differential pressure gauge (used to calculate the flow). Each AS well has a dedicated manifold with a
flow meter and a pressure gauge. Refer to MLEE’s as-built drawings in Appendix B-2 for
more information.
The hoses for connecting each SVE and AS well to the manifolds were delivered to the Site
on October 15, 2010 and connected the same day.
2.8 EQUIPMENT INSTALLATION
On October 4, 2010, the equipment building and oxidizer were delivered to the Site. A crane
was utilized to lift and place the building and the oxidizer chamber component into the
permanent location. Mechanical contractor, Midwest and electrical contractor, Ballardassisted with placement and assembly of the building and oxidizer. MWH reviewed the
system components to verify that all system components were constructed in accordance
with the approved designs.
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2.8.1 Equipment Building
The equipment building was prefabricated by MLEE prior to delivery to the Site. The
building is an eight-foot by 30-foot modified shipping container that contains all processequipment (except the thermal oxidizer), electrical, heating and ventilation systems. The
interior space of the building is divided into two rooms – the equipment room and the
electrical/control room.
The electrical/control room is seven-feet by eight-feet and contains the air compressor and
heat exchanger for the AS system, electrical panel, security camera interface and the programmable logic controller (PLC).
The AS air compressor (C-2201) is a Sutorbilt model 2M-RHC that is 1½ horsepower (HP),
38 standard cubic feet per minute (SCFM) and 3029 revolutions per minute (RPM). The ASheat exchanger (F-2501 XCH) is 1/3 HP, 38 SCFM and 1140 RPM. Both the AS air
compressor and the AS heat exchanger have a hand/off/auto (HOA) switch on the main
control panel that allows each equipment to be operated manually or automatically by the
PLC.
The Equipment Room is 23-feet by eight-feet and contains the SVE Blower, vapor liquid
separator (VLS) tank and pump, surge tank, discharge pump and two granular activated
carbon (GAC) treatment vessels.
The SVE blower is a Rotron 20 HP, 3600 RPM, 475 SCFM blower. A HOA switch on the
main control panel allows the blower to be operated manually or automatically by the PLC.
The VLS tank separates entrained water from the extracted vapor stream. The 90-gallon
VLS tank has level switches that activate a five-gallon per minute (gpm) centrifugal VLS
Goulds pump of ½ HP and 3500 RPM. The high level switch initiates pump operation andthe low level switch turns it off. A HOA switch on the main control panel allows the VLS
pump (P-401) to be operated manually or automatically by the PLC. The pump transfers the
captured water to the surge tank.
The surge tank is a high-density, linear polyethylene containment tank with a 150-gallon
capacity. A level switch located in the surge tank triggers the shut down the of SVE/ASsystem when the water reaches the high level switch. The discharge pump (P-7301 DISCH)
is a Goulds ½ HP, 3500 RPM, five-gpm centrifugal pump and is utilized to pump water from
the surge tank to the granular activated carbon vessels for treatment. A HOA switch on themain control panel allows the discharge pump to be operated manually or automatically by
the PLC.
The two GAC treatment units are Siemens Aqua-Scrub ASC200 drums with a maximumoperating flow rate of ten-gpm. A pressure gauge and a sample port are located at the inlets
to each vessel. Water from the surge tank is pumped through the GAC units and to one of
two storage tanks (each 550-gallons) located outside the equipment building.
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The equipment building was shipped by flatbed truck to the Site. The load was lifted by
crane into the designated location. The building was then shimmed and leveled.
Once the building was positioned, packaging that protected the equipment during shipping
was removed. Exterior hoods insulated for noise were installed over the exhaust fans and
louvers. Silencer filters were installed on the exterior of the building. Three fireextinguishers and a spill kit were placed inside the building.
2.8.2 Oxidizer
The oxidizer unit, manufactured by Intellishare, is a 500 SCFM chlorinated thermal oxidizer
with a heat exchanger (Model TO500). The oxidizer is designed to destroy the organic vapor
contaminants by operating at a temperature of 1,550 degrees Fahrenheit. The oxidizer unit
was delivered to the Site on October 4, 2010 and lifted by crane into the designated location.The base and chamber of the oxidizer were placed in the designated locations and the
oxidizer’s heat exchanger and the stack were assembled on Site as directed by an Intellishare
technician.
After the oxidizer was placed on Site, Midwest installed the vapor conveyance piping(five-inch carbon steel) connecting the SVE blower (in the equipment building) to the
oxidizer. The natural gas supply pipe (1 ½-inch carbon steel piping) was installed
connecting the gas meter (located at the north side of the Site) to the oxidizer.
Ballard installed the electrical wiring for all the oxidizer’s sensor switches, thermocouples,
temperature and pressure gauges and installed conduit and electrical cable to the control panel located inside the equipment building. These activities were completed on
October 8, 2010.
2.8.3
Control System
A PLC provides supervisory control and data acquisition for the system equipment. ThePLC is housed in the electrical/control room of the equipment building. Further details
regarding system controls are provided in the process and instrumentation diagrams included
with the as-built drawings (Appendix B).
2.8.4 Telemetry System
The telemetry system allows remote access via the internet to monitor and control the
SVE/AS system. The telemetry module is a MLEE Model SL-WP wireless remote accesssystem.
Through the program interface, installed on the MWH project engineers’ computers, users
can remotely control equipment by selecting hand, off or auto control, shut down or restartthe system, review system operating parameters and diagnose system alarms. The telemetry
system records critical operating data including equipment operating hours, oxidizer
temperatures, and vapor flow rate.
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2.8.5 Security Camera
A WatchNet-brand dome security camera was installed on the south east corner of the top of
the equipment building. The camera was positioned to provide a panoramic view of the Site,including access gates. The camera records information on a hard drive that is retrievable in
the event that a review of Site events or Site access is required. The hard drive provides
approximately 25 days of storage.
2.9 UTILITIES
To support system operation, electric power and natural gas supply were installed at the Site.
The existing electrical service available at the Site is 240 Voltage Alternating Current
(VAC). To boost the voltage from 240 VAC to the 480 VAC required by the system
equipment, an electrical transformer 75 Kilovolt-ampere (KVA) was installed. Thetransformer was installed to the west of the equipment building on October 8, 2010.
Commonwealth Edison connected the transformer with the main electrical service on
October 11, 2010. Ballard completed electrical terminations for the system equipment onOctober 12, 2010.
Natural gas is the main source of fuel for the oxidizer. Natural gas supply is provided locally by Nicor, Inc. (Nicor). Nicor installed the gas pipe at the north side of the Site on
September 22, 2010 and completed the installation of the gas meter on October 4, 2010.
Midwest completed installation of the gas supply line (1 ½-inch carbon steel) from the meterto the oxidizer on October 11, 2010.
2.10 SYSTEM COMMISSIONING & STARTUP
MLEE performed system integration and commissioning activities beginning on
October 18, 2010. MLEE tested the functionality of electrical, control and mechanicalcomponents to ensure the system operates as designed. Air samples were collected to verify
oxidizer performance with respect to the vendor’s specifications. The system commissioning
was completed on October 21, 2010.
System operation formally began upon completion of the commissioning task. Startup tasks
performed included initial measurements of system performance, balancing of flows across
the SVE well field, and collection of air samples per the IEPA Air Permit.
2.10.1 Oxidizer Performance Sampling
Air samples were collected to verify the oxidizer was performing within the vendor’s
specifications. Samples of the oxidizer influent and effluent were collected via Summacanister on October 20, 2010 and submitted to Air Toxics, Ltd. for analysis by United States
Environmental Protection Agency (USEPA) Method TO-15. The data from these samples
were used to calculate the destruction efficiency of the oxidizer. The calculated destruction
efficiency of the oxidizer was 97.59 percent which meets the required performance criteria(95 percent). Table 1 summarizes the analytical data and the associated calculation of
destruction efficiency. Laboratory analytical results are attached in Appendix D-1.
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2.10.2 Compliance Air Sampling
Air samples were collected in accordance with the startup provisions of the IEPA Air Permit.
Oxidizer effluent samples were collected at start-up, once per day for the first three days, andtwo times per week for the first two weeks. Air samples were collected via Summa canister
and analyzed for volatile organic compounds by USEPA Method TO-15 by Stat Analysis
Corporation of Chicago, Illinois. The analytical results provided in Appendix D-1demonstrate the system is operating in compliance with the air permit.
2.11 WASTE DISPOSAL
Soil cuttings collected during drilling activities and used personnel protective equipment
were containerized in a roll-off box on Site. A composite sample of soil from each well
location was collected and submitted to First Environmental Laboratories, Inc. (FirstEnvironmental) of Naperville, Illinois to be analyzed for waste characterization parameters.
The soil was analyzed for the following parameters by the following analytical methods.
Parameters Analytical Method
Flash point 1010MPaint filter 9095A
pH 4500H+B
Phenols 420.1
Reactive cyanide 7.3.3.2Reactive sulfide 7.3.4.2
TCLP herbicides 1311/8321A
TCLP pesticides 1311/8081ATCLP metals 1311/6010B and 1311/7470A
TCLP semi-volatile organic compounds 1311/8270C
TCLP VOCs 1311/8260BTotal sulfide 4500S2,C,D
Soil waste analytical results are attached in Appendix D-2. The results confirm that the
waste is categorized as Illinois special waste (i.e. not hazardous). The roll-off boxcontaining the soil waste and the disposable personal protective gear was hauled to
Winnebago Landfill Company located at 8403 Lindenwood Road in Rockford, Illinois for
disposal on November 24th
, 2010. The manifest was signed by Gary Letcher, Attorney Chairof Acme Rockford Group, and filed in MWH’s records.
Water generated during well development and decontamination activities was containerized
in four 55-gallon drums. Samples of the contents of each drum were collected to determineif the water could be discharged to the sanitary sewer under the Site’s wastewater discharge
permit. The samples were submitted to First Environmental for analysis of VOCs by method5030B/8260B. Purge water analytical results are attached in Appendix D-3. The results
indicated that concentrations of ethylbenzene, toluene and trichloroethane exceeded
permitted discharge limits. Therefore, the purge water was hauled off Site as
environmentally hazardous waste, for treatment and disposal, by Badger Disposal of WI, Inc
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located at 5611 West Hemlock Street in Milwaukee, Wisconsin on November 24, 2010. The
manifest was signed by Gary Letcher, Attorney Chair of Acme Rockford Group,and filed in MWH’s records.
A minimal amount of construction debris was generated during the construction activities.
Disposal of this waste was managed by MWH’s subcontractors at their facilities.
2.12 AS-BUILT DRAWINGS
As-built drawings are provided in Appendix B.
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3.0 REFERENCES
MWH, 2007. Site Investigation Report, Soil Vapor Extraction & Air Sparge System, Acme
Solvent Reclaiming, Inc. Site, Rockford, Illinois.
MWH, 2007. Remedial Objectives Report, Soil Vapor Extraction & Air Sparge System, Acme
Solvent Reclaiming, Inc. Site, Rockford, Illinois.
MWH, 2008. Remedial Action Plan, Soil Vapor Extraction & Air Sparge System, Acme
Solvent Reclaiming, Inc. Site, Rockford, Illinois.
MWH, 2009. Remedial Design Work Plan, Pilot Test, Soil Vapor Extraction/Air Sparge
System, Acme Solvent Reclaiming, Inc. Site, Rockford, Illinois.
MWH, 2009. Remedial Design Report, Soil Vapor Extraction & Air Sparge System, AcmeSolvent Reclaiming, Inc. Site, Rockford, Illinois.
MWH, 2009. Remedial Action Work Plan, Soil Vapor Extraction & Air Sparge System, Acme
Solvent Reclaiming, Inc. Site, Rockford, Illinois.
DLG/CAD/CRS/JEF/PJVO:\1009100-1009199\1009103 Acme Design-Build\4.0 Execution (Project Deliverables)\4.9 CCR\Acme CCR (Final).doc
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TABLE
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Table 1
Thermal Oxidizer Results for Method TO-15 (VOCs)
ACME Site
Rockford, Illinois
Compounds Units
1,1,1-Trichloroethane ppbv 700 ND U 100.00%
1,1,2,2-Tetrachloroethane ppbv ND U ND U NC1,1,2-Trichloroethane ppbv ND U ND U NC
1,1-Dichloroethane ppbv 65 ND U 100.00%
1,1-Dichloroethene ppbv ND U ND U NC
1,2,4-Trimethylbenzene ppbv 79 15.00 81.01%
1,2-Dichloroethane ppbv ND U ND U NC
1,2-Dichloropropane ppbv ND U ND U NC
1,3,5-Trimethylbenzene ppbv 39 ND U 100.00%
2-Butanone (Methyl Ethyl Ketone) ppbv ND U ND U NC
2-Hexanone ppbv ND U ND U NC
4-Ethyltoluene ppbv 110 ND U 100.00%
4-Methyl-2-pentanone ppbv ND U ND U NC
Acetone ppbv ND U 560.00 NC
Benzene ppbv ND U ND U NC
Bromodichloromethane ppbv ND U ND U NC
Bromoform ppbv ND U ND U NC
Bromomethane ppbv ND U ND U NCCarbon Disulfide ppbv ND U ND U NC
Carbon Tetrachloride ppbv ND U ND U NC
Chlorobenzene ppbv ND U ND U NC
Chloroethane ppbv ND U ND U NC
Chloroform ppbv ND U ND U NC
Chloromethane ppbv ND U ND U NC
cis-1,2-Dichloroethene ppbv 440 ND U 100.00%
cis-1,3-Dichloropropene ppbv ND U ND U NC
Dibromochloromethane ppbv ND U ND U NC
Ethanol ppbv ND U 31.00 J NC
Ethyl Benzene ppbv 1,400 ND U 100.00%
Heptane ppbv 540 ND U 100.00%
m,p-Xylene ppbv 4,400 8.30 99.81%
Methylene Chloride ppbv 55 ND U 100.00%
o-Xylene ppbv 970 3.20 99.67%
Propylbenzene ppbv 30 ND U 100.00%
Styrene ppbv ND U ND U NC
Tetrachloroethene ppbv 140 5.90 95.79%
Toluene ppbv 17,000 4.30 99.97%
trans-1,2-Dichloroethene ppbv ND U ND U NC
trans-1,3-Dichloropropene ppbv ND U ND U NC
Trichloroethene ppbv 87 ND U 100.00%
Vinyl Chloride ppbv ND U ND U NC
Total ppbv 97.59%
Total lb/hr 99.37%
Notes: Qualifiers:
NC - Not calculated U - Below reported quantitation limit
ND - Not detected J - Result is estimated
ppbv - Parts per billion volume
lb/hr - Pounds per hour VOC - Volatile organic compounds
Destruction efficiencies were not calculated if either the influent or effluent samples were estimated.
Destruction efficiencies were also not calculated if the effluent result exceeded either influent result.
Total destruction efficiencies that include the estimated results of any individual compound will be considered an estimated val
System Date Temp Flow
(F) (scfm)
Oxidizer Inlet 10/20/10 57 778
Oxidizer Effluent 10/20/10 978 778
Temperatures and flow rates reported correspond to instantaneous readings.
627.7
Destruction
Efficiency
10/20/10
0.002
Oxidizer
26,055
0.316
Influent Effluent
ACB\DLGO:\1009100-1009199\1009103 Acme Design-Build\4.0 Execution (Project Deliverables)\4.7 Oxidizer Compliance\ACME Destruction Efficency.xls\Table 1 - TO-15 Oxidizer Page 1 of 1
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FIGURE
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J:\209\0754 Acme Rockford\MWDWGS\2090754_SITE_TOPO_MAP.dwg, 09/17/03 07:37:53 AM
SITE
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APPENDICES
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Appendix A: Photographic Log
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Customer: ACME-Rockford Group Project Name:
Site Name: ACME Site Location: 1915 20th Ave, Rockford, IL
Photograph ID: 001
Date: Sep 3, 2010
Location / Direction:
ACME Site /
South West
Comments:
Removal of storage container
located on Site
Photograph ID: 002
Date: Sep 10, 2010
Location / Direction:
ACME Site /
South
Comments:
Site prior to vegetative
clearing
Photographic Log - ACME
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Customer: ACME-Rockford Group Project Name:
Site Name: ACME Site Location: 1915 20th Ave, Rockford, IL
Photograph ID: 003
Date: Sep 10, 2010
Location / Direction:
ACME Site /
South
Comments:
Site prior to vegetative
clearing
Photograph ID: 004
Date: Sep 10, 2010
Location / Direction:
ACME Site /
South
Comments:
Clearing and mowing the Site
Photographic Log - ACME
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Customer: ACME-Rockford Group Project Name:
Site Name: ACME Site Location: 1915 20th Ave, Rockford, IL
Photograph ID: 005
Date: Sep 10, 2010
Location / Direction:
ACME Site /
South
Comments:
Site cleared of brush and
mowed
Photograph ID: 006
Date: Sep 13, 2010
Location / Direction:
ACME Site /
South West
Comments:
Survey locations marked for
SVE, AS and VMP wells
Photographic Log - ACME
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Customer: ACME-Rockford Group Project Name:
Site Name: ACME Site Location: 1915 20th Ave, Rockford, IL
Photograph ID: 007
Date: Sep 13, 2010
Location / Direction:
ACME Site /
South West
Comments:
Survey locations marked for
SVE, AS and VMP wells
Photograph ID: 008
Date: Sep 23, 2010
Location / Direction:
ACME Site /
North
Comments:
Natural gas piped into Site by
Nicor
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Customer: ACME-Rockford Group Project Name:
Site Name: ACME Site Location: 1915 20th Ave, Rockford, IL
Photograph ID: 009
Date: Sep 30, 2010
Location / Direction:
ACME Site /
East
Comments:
Drilling for SVE well
installation and placing soil
cuttings in roll-off box
Photograph ID: 010
Date: Sep 30, 2010
Location / Direction:
ACME Site /North East
Comments:
Installing SVE well
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Customer: ACME-Rockford Group Project Name:
Site Name: ACME Site Location: 1915 20th Ave, Rockford, IL
Photograph ID: 011
Date: Sep 30, 2010
Location / Direction:
ACME Site /
North
Comments:
Collecting purge water from
developing the SVE, AS and
VMP wells in 55-gallon drums
Photograph ID: 012
Date: Sep 30, 2010
Location / Direction:
ACME Site /
South
Comments:
After completing the
installation of all wells, the drill
equipment was
decontaminated before it was
mobilized off-Site
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Customer: ACME-Rockford Group Project Name:
Site Name: ACME Site Location: 1915 20th Ave, Rockford, IL
Photograph ID: 013
Date: Oct 1, 2010
Location / Direction:
ACME Site /
East
Comments:
Roll-off containing soil
cuttings from SVE, AS and
VMP wells
Photograph ID: 014
Date: Oct 1, 2010
Location / Direction:
ACME Site /
North
Comments:
Four 55-gallon drums
containing purged
groundwater from developing
the SVE, AS and VMP wells
Photographic Log - ACME
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Customer: ACME-Rockford Group Project Name:
Site Name: ACME Site Location: 1915 20th Ave, Rockford, IL
Photograph ID: 015
Date: Oct 4, 2010
Location / Direction:
ACME Site /
North
Comments:
Unloading the equipment
building containing blower and
manifold equipment
Photograph ID: 016
Date: Oct 4, 2010
Location / Direction:
ACME Site /North
Comments:
Lowering the equipment
building
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Customer: ACME-Rockford Group Project Name:
Site Name: ACME Site Location: 1915 20th Ave, Rockford, IL
Photograph ID: 017
Date: Oct 4, 2010
Location / Direction:
ACME Site /
North
Comments:
Positioning the equipment
building
Photograph ID: 018
Date: Oct 4, 2010
Location / Direction:
ACME Site /
North
Comments:
Interior view of southern side
of the equipment building
where extraction blower and
well manifold reside
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Customer: ACME-Rockford Group Project Name:
Site Name: ACME Site Location: 1915 20th Ave, Rockford, IL
Photograph ID: 019
Date: Oct 4, 2010
Location / Direction:
ACME Site /
North East
Comments:
Vapor extraction well
manifolds
Photograph ID: 020
Date: Oct 4, 2010
Location / Direction:
ACME Site /
South West
Comments:
Interior view of the northern
side of the equipment building
showing programmable logic
controller and electrical panel
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Customer: ACME-Rockford Group Project Name:
Site Name: ACME Site Location: 1915 20th Ave, Rockford, IL
Photograph ID: 021
Date: Oct 4, 2010
Location / Direction:
ACME Site /
North West
Comments:
Air sparge compressor
located in the northern side of
the equipment building
Photograph ID: 022
Date: Oct 4, 2010
Location / Direction:
ACME Site /
North
Comments:
Western side of the
equipment building
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Customer: ACME-Rockford Group Project Name:
Site Name: ACME Site Location: 1915 20th Ave, Rockford, IL
Photograph ID: 023
Date: Oct 4, 2010
Location / Direction:
ACME Site /
North
Comments:
Unloading the thermal
oxidizer unit
Photograph ID: 024
Date: Oct 4, 2010
Location / Direction:
ACME Site /North
Comments:
Unloading the thermal
oxidizer chamber
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Customer: ACME-Rockford Group Project Name:
Site Name: ACME Site Location: 1915 20th Ave, Rockford, IL
Photograph ID: 025
Date: Oct 4, 2010
Location / Direction:
ACME Site /
North
Comments:
Positioning the thermal
oxidizer chamber
Photograph ID: 026
Date: Oct 4, 2010
Location / Direction:
ACME Site /West
Comments:
Assembling the heat
exchanger and stack
component of the thermal
oxidizer
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Customer: ACME-Rockford Group Project Name:
Site Name: ACME Site Location: 1915 20th Ave, Rockford, IL
Photograph ID: 027
Date: Oct 4, 2010
Location / Direction:
ACME Site /
West
Comments:
Installing the heat exchanger
and stack
Photograph ID: 028
Date: Oct 4, 2010
Location / Direction:
ACME Site /West
Comments:
Positioning the heat
exchanger and stack
Photographic Log - ACME
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Customer: ACME-Rockford Group Project Name:
Site Name: ACME Site Location: 1915 20th Ave, Rockford, IL
Photograph ID: 029
Date: Oct 4, 2010
Location / Direction:
ACME Site /
West
Comments:
Adding the effluent line that
will carry treated vapors to the
heat exchanger and out the
stack.
Photograph ID: 030
Date: Oct 8, 2010
Location / Direction:
ACME Site /South West
Comments:
Installing the electrical
connection to ComEd's line
Photographic Log - ACME
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Customer: ACME-Rockford Group Project Name:
Site Name: ACME Site Location: 1915 20th Ave, Rockford, IL
Photograph ID: 031
Date: Oct 12, 2010
Location / Direction:
ACME Site /
South
Comments:
Western side of equipment
building. Installing vapor
piping connecting the building
to the thermal oxidizer inlet.
New transformer and
electrical conduit are shown.
Photograph ID: 032
Date: Oct 8, 2010
Location / Direction:
ACME Site /
West
Comments:
Electrical lines connecting
thermal oxidizer's sensors
and controls to the
transformer and the program
logic control system
Photographic Log - ACME
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Customer: ACME-Rockford Group Project Name:
Site Name: ACME Site Location: 1915 20th Ave, Rockford, IL
Photograph ID: 033
Date: Oct 12, 2010
Location / Direction:
ACME Site /
East
Comments:
Natural gas inlet train
Photograph ID: 034
Date: Oct 12, 2010
Location / Direction:
ACME Site /
East
Comments:
Electrically powered chamber
thermocouples
Photographic Log - ACME
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Customer: ACME-Rockford Group Project Name:
Site Name: ACME Site Location: 1915 20th Ave, Rockford, IL
Photograph ID: 035
Date: Oct 12, 2010
Location / Direction:
ACME Site /
East
Comments:
Electrically powered
thermocouples located on the
stack
Photograph ID: 036
Date: Oct 12, 2010
Location / Direction:
ACME Site /South West
Comments:
Painting the natural gas line
yellow
Photographic Log - ACME
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Customer: ACME-Rockford Group Project Name:
Site Name: ACME Site Location: 1915 20th Ave, Rockford, IL
Photograph ID: 037
Date: Oct 21, 2010
Location / Direction:
ACME Site /
South West
Comments:
Completed SVE/AS system
Photographic Log - ACME
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Appendix B: As-built Drawings
B1: MWH’s Construction As-built Drawings
B2: MLEE’s As-built Drawings
B3: Intellishare’s As-built Drawings
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Appendix B1: MWH’s Construction As-built Drawings
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Appendix B-2: MLEE’s As-Built Drawings
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Appendix B-3: Intellishare’s As-Built Drawings
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101.54
72.00
12.15
14.15
06.00
101.54
134.91
152.79
177.79
249.79
Shipping Break
Burner End View
28.83CL Fuel Train Inlet
JunctionBox
Fuel Train
With Enclosure1" FNPT
Heat Exchanger Module
InsulatedDuct
Right View
6" 150# Style Flange
(Process Connection)
CombustionAir Blower
BalancingDamper
Flame Arrestor CombustionAir Filter
HeatExchanger Air SpargeBlower
Air SpargeControl Valve
Left View
No Loss Stack
Oxidizer Skid
49.50
69.99
224.12
207.00
27.00
78.72
Top View
Pictorial View
Estimated Weight: 8000 lbs
78
8 7 6 5 4 3 2 1
6 5 4 3 2 1
ACME - Rockford, IL
MapleLeaf Environmental
LAST PLOTTED BY
Henry A
Henry A
GENERAL ARRANGMENT DRAWING
500 CFM CHLORINATED THERMALOXIDIZER
LAST DRAWN BY
APPROVED
CHECKED
DRAWN
TITLE
CUSTOMER
SOURCE
7/28/2010
DATE
DATE
8/2/2006
DATE
DATE
XXXXXX
1P AG E O F
DATE
N-10-0965-
DRAWING NO.
NTS
SCALE
N-10-0965-002
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E lement Termi nal # J K
1a W hi te Y el lo w
1b Red Red
2a W hi te Y el lo w
2b Red Red
3a W hi te Y el lo w
3b Red Red
TE2
TE2A
TE2B
Thermocouple Terminal Designations
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Appendix C: Well Construction Diagrams
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Appendix D: Analytical Data
D1: Air Sampling Analytical Results
D2: Soil Sampling Analytical Results
D3: Purge Water Sampling Analytical Results
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Appendix D1: Air Sampling Analytical Results
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Summary of Air Sampling Results
ACME Site
Rockford, IL
Inlet TO 0965 ACME-TOXINF-110910 Outlet TO 0965 ACME-TOXEFF-102110 ACME-TOXEFF-102210
10/20/2010 11/09/2010 10:10 10/20/2010 10/21/2010 16:16 10/22/2010 12:21
Analyte Test Method Units
Sample ID :
Date Collected :
Influent to Thermal Oxidizer
Hexane TO-15 ppbv ND 110 ND ND ND
Isopropyl Alcohol TO-15 ppbv NA ND NA ND ND
m,p-Xylene TO-15 ppbv 4400 760000 8.3 27 460
Methyl tert-butyl ether TO-15 ppbv ND ND ND ND ND
Methylene chloride TO-15 ppbv 55 ND ND ND ND
o-Xylene TO-15 ppbv 970 210000 3.2 7 150
Propene TO-15 ppbv NA ND NA ND ND
Propylbenzene TO-15 ppbv 30 NA ND NA NA
Styrene TO-15 ppbv ND 3800 ND ND 2.1
Tetrachloroethene TO-15 ppbv 140 6900 5.9 ND 7.9
Tetrahydrofuran TO-15 ppbv ND ND ND 2.7 ND
Toluene TO-15 ppbv 17000 450000 4.3 19 350
trans-1,2-Dichloroethene TO-15 ppbv ND ND ND ND ND
trans-1,3-Dichloropropene TO-15 ppbv ND ND ND ND ND
Trichloroethene TO-15 ppbv 87 1100 ND ND ND
Trichlorofluoromethane TO-15 ppbv NA ND NA ND ND
Vinyl acetate TO-15 ppbv NA ND NA ND ND
Vinyl chloride TO-15 ppbv ND ND ND ND ND
Xylenes, Total TO-15 ppbv 5370 970000 11.5 34 610
Total ppbv 26,055.00 1,627,276.00 627.70 1,880.93 1,551.32
Notes:
ppbv - Parts per billion volume
ND - Not detected
NA - Not Analyzed
Qualifiers:
J - Result is estimated
DLG/JEF
O:\1009100-1009199\1009103 Acme Design-Build\4.0 Execution (Project Deliverables)\4.4 Analtyical Data\Air Sampling\Summary Air Sampling Results.xls Page 2
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10/25/2010
Mr. Gary Wolf
Intellishare Environmental1422 Indian Head Drive East
Menomonie WI 54751
Project Name: Rockford, IL
Project #: N-10-0965
Dear Mr. Gary Wolf
The following report includes the data for the above referenced project for sample(s)received on 10/22/2010 at Air Toxics Ltd.
The data and associated QC analyzed by Modified TO-15 are compliant with theproject requirements or laboratory criteria with the exception of the deviations noted inthe attached case narrative.
Thank you for choosing Air Toxics Ltd. for your air analysis needs. Air Toxics Ltd. iscommitted to providing accurate data of the highest quality. Please feel free to contact
the Project Manager: Jacquelyn Luta at 916-985-1000 if you have any questionsregarding the data in this report.
Regards,
Jacquelyn Luta
Project Manager
Workorder #: 1010482
180 BLUE RAVINE ROAD, SUITE B FOLSOM, CA - 95630
(916) 985-1000 .FAX (916) 985-1020
Hours 6:30 A.M to 5:30 PST
Page 1 of 24
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Mr. Gary Wolf
Intellishare Environmental
1422 Indian Head Drive East
Menomonie, WI 54751
WORK ORDER #: 1010482
CLIENT: BILL TO:
PHONE:
Mr. Gary Wolf
Intellishare Environmental
1422 Indian Head Drive East
Menomonie, WI 54751
715-233-6115 x115
10/22/2010DATE COMPLETED: 10/15/2010
P.O. # 20266
PROJECT # N-10-0965 Rockford, IL
Work Order Summary
FAX:
DATE RECEIVED: CONTACT: Jacquelyn Luta
NAMEFRACTION # TEST VAC./PRES.
RECEIPT
PRESSUR
FINAL
01A OUTLET TO 0965 Modified TO-15 5.2 "Hg 15 psi
02A INLET TO 0965 Modified TO-15 6.0 "Hg 15 psi
03A Lab Blank Modified TO-15 NA NA
03B Lab Blank Modified TO-15 NA NA
04A CCV Modified TO-15 NA NA
04B CCV Modified TO-15 NA NA
05A LCS Modified TO-15 NA NA
05AA LCSD Modified TO-15 NA NA
05B LCS Modified TO-15 NA NA
05BB LCSD Modified TO-15 NA NA
CERTIFIED BY:
Laboratory Director
DATE:
Name of Accrediting Agency: NELAP/Florida Department of Health, Scope of Application: Clean Air Act,
Accreditation number: E87680, Effective date: 07/01/09, Expiration date: 06/30/11
180 BLUE RAVINE ROAD, SUITE B FOLSOM, CA - 95630
(916) 985-1000 . (800) 985-5955 . FAX (916) 985-1020
10/25/10
Page 2 of 24
This report shall not be reproduced, except in full, without the written approval of Air Toxics Ltd.
Air Toxics Ltd. certifies that the test results contained in this report meet all requirements of the NELAC standards
Certfication numbers: CA NELAP - 02110CA, LA NELAP/LELAP- AI 30763,
NY NELAP - 11291, UT NELAP - 9166389892, AZ Licensure AZ0719
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LABORATORY NARRATIVEEPA Method TO-15
Intellishare EnvironmentalWorkorder# 1010482
Two 1 Liter Summa Canister samples were received on October 22, 2010. The laboratory performed
analysis via modified EPA Method TO-15 using GC/MS in the full scan mode.
This workorder was independently validated prior to submittal using 'USEPA National Functional
Guidelines' as generally applied to the analysis of volatile organic compounds in air. A rules-based, logic
driven, independent validation engine was employed to assess completeness, evaluate pass/fail of relevant
project quality control requirements and verification of all quantified amounts.
There were no receiving discrepancies.
Receiving Notes
All Quality Control Limit exceedences and affected sample results are noted by flags. Each flag is defined
at the bottom of this Case Narrative and on each Sample Result Summary page. Target compound
non-detects in the samples that are associated with high bias in QC analyses have not been flagged.
Dilutions were performed on samples OUTLET TO 0965 and INLET TO 0965 due to the presence of
high level target species.
Analytical Notes
Eight qualifiers may have been used on the data analysis sheets and indicates as follows:
B - Compound present in laboratory blank greater than reporting limit (background subtraction not
performed).
J - Estimated value.
E - Exceeds instrument calibration range.
S - Saturated peak.
Q - Exceeds quality control limits.
U - Compound analyzed for but not detected above the reporting limit.
UJ- Non-detected compound associated with low bias in the CCV
N - The identification is based on presumptive evidence.
File extensions may have been used on the data analysis sheets and indicates
as follows:
a-File was requantified
b-File was quantified by a second column and detector
r1-File was requantified for the purpose of reissue
Definition of Data Qualifying Flags
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MODIFIED EPA METHOD TO-15 GC/MS FULL SCAN
Summary of Detected Compounds
Client Sample ID: OUTLET TO 0965
Lab ID#: 1010482-01A
(ug/m3)(ug/m3)(ppbv)(ppbv)Compound
AmountR t. LimitAmountR t. Limit
12 31 J 23 59 JEthanol
12 560 29 1300 Acetone
3.0 4.3 11 16Toluene
3.0 5.9 21 40Tetrachloroethene
3.0 8.3 13 36m,p-Xylene
3.0 3.2 13 14o-Xylene
3.0 15 15 741,2,4-Trimethylbenzene
Client Sample ID: INLET TO 0965
Lab ID#: 1010482-02A
(ug/m3)(ug/m3)(ppbv)(ppbv)Compound
AmountRpt. LimitAmountR t. Limit
29 55 99 190Methylene Chloride
29 65 120 2601,1-Dichloroethane
29 440 110 1700cis-1,2-Dichloroethene
29 700 160 38001,1,1-Trichloroethane
29 540 120 2200Heptane
29 87 150 470Trichloroethene
29 17000 110 64000Toluene
29 140 190 960Tetrachloroethene
29 1400 120 5900Ethyl Benzene
29 4400 120 19000m,p-Xylene
29 970 120 4200o-Xylene
29 30 140 150Propylbenzene
29 110 140 5604-Ethyltoluene
29 39 140 1901,3,5-Trimethylbenzene
29 79 140 3901,2,4-Trimethylbenzene
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Client Sample ID: OUTLET TO 0965
Lab ID#: 1010482-01A
MODIFIED EPA METHOD TO-15 GC/MS FULL SCAN
p102241File Name:
Dil. Factor: 6.10
Date of Collection: 10/20/10 10:00:00 A
Date of Analysis: 10/23/10 03:32 PM
(ug/m3)(ug/m3)(ppbv)(ppbv)Compound
AmountRpt. LimitAmountR t. Limit
3.0 Not Detected 15 Not DetectedFreon 12
3.0 Not Detected 21 Not DetectedFreon 114
12 Not Detected 25 Not DetectedChloromethane
3.0 Not Detected 7.8 Not DetectedVinyl Chloride
3.0 Not Detected 6.7 Not Detected1,3-Butadiene
3.0 Not Detected 12 Not DetectedBromomethane
3.0 Not Detected 8.0 Not DetectedChloroethane
3.0 Not Detected 17 Not DetectedFreon 11
12 31 J 23 59 JEthanol
3.0 Not Detected 23 Not DetectedFreon 113
3.0 Not Detected 12 Not Detected1,1-Dichloroethene
12 560 29 1300 Acetone
12 Not Detected 30 Not Detected2-Propanol
3.0 Not Detected 9.5 Not DetectedCarbon Disulfide
12 Not Detected 38 Not Detected3-Chloropropene
3.0 Not Detected 10 Not DetectedMethylene Chloride
3.0 Not Detected 11 Not DetectedMethyl tert-butyl ether
3.0 Not Detected 12 Not Detectedtrans-1,2-Dichloroethene3.0 Not Detected 11 Not DetectedHexane
3.0 Not Detected 12 Not Detected1,1-Dichloroethane
3.0 Not Detected 9.0 Not Detected2-Butanone (Methyl Ethyl Ketone)
3.0 Not Detected 12 Not Detectedcis-1,2-Dichloroethene
3.0 Not Detected 9.0 Not DetectedTetrahydrofuran
3.0 Not Detected 15 Not DetectedChloroform
3.0 Not Detected 17 Not Detected1,1,1-Trichloroethane
3.0 Not Detected 10 Not DetectedCyclohexane
3.0 Not Detected 19 Not DetectedCarbon Tetrachloride
3.0 Not Detected 14 Not Detected2,2,4-Trimethylpentane
3.0 Not Detected 9.7 Not DetectedBenzene
3.0 Not Detected 12 Not Detected1,2-Dichloroethane3.0 Not Detected 12 Not DetectedHeptane
3.0 Not Detected 16 Not DetectedTrichloroethene
3.0 Not Detected 14 Not Detected1,2-Dichloropropane
12 Not Detected 44 Not Detected1,4-Dioxane
3.0 Not Detected 20 Not DetectedBromodichloromethane
3.0 Not Detected 14 Not Detectedcis-1,3-Dichloropropene
3.0 Not Detected 12 Not Detected4-Methyl-2-pentanone
3.0 4.3 11 16Toluene
3.0 Not Detected 14 Not Detectedtrans-1,3-Dichloropropene
3.0 Not Detected 17 Not Detected1,1,2-Trichloroethane
3.0 5.9 21 40Tetrachloroethene
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Client Sample ID: OUTLET TO 0965
Lab ID#: 1010482-01A
MODIFIED EPA METHOD TO-15 GC/MS FULL SCAN
p102241File Name:
Dil. Factor: 6.10
Date of Collection: 10/20/10 10:00:00 A
Date of Analysis: 10/23/10 03:32 PM
(ug/m3)(ug/m3)(ppbv)(ppbv)Compound
AmountRpt. LimitAmountR t. Limit
12 Not Detected 50 Not Detected2-Hexanone
3.0 Not Detected 26 Not DetectedDibromochloromethane
3.0 Not Detected 23 Not Detected1,2-Dibromoethane (EDB)
3.0 Not Detected 14 Not DetectedChlorobenzene
3.0 Not Detected 13 Not DetectedEthyl Benzene
3.0 8.3 13 36m,p-Xylene
3.0 3.2 13 14o-Xylene
3.0 Not Detected 13 Not DetectedStyrene
3.0 Not Detected 32 Not DetectedBromoform
3.0 Not Detected 15 Not DetectedCumene
3.0 Not Detected 21 Not Detected1,1,2,2-Tetrachloroethane
3.0 Not Detected 15 Not DetectedPropylbenzene
3.0 Not Detected 15 Not Detected4-Ethyltoluene
3.0 Not Detected 15 Not Detected1,3,5-Trimethylbenzene
3.0 15 15 741,2,4-Trimethylbenzene
3.0 Not Detected 18 Not Detected1,3-Dichlorobenzene
3.0 Not Detected 18 Not Detected1,4-Dichlorobenzene
3.0 Not Detected 16 Not Detectedalpha-Chlorotoluene3.0 Not Detected 18 Not Detected1,2-Dichlorobenzene
12 Not Detected 90 Not Detected1,2,4-Trichlorobenzene
12 Not Detected 130 Not DetectedHexachlorobutadiene
J = Estimated value due to bias in the CCV.
Container Type: 1 Liter Summa Canister
Limits%RecoverySurrogates
Method
100 70-130Toluene-d8
96 70-1301,2-Dichloroethane-d4
99 70-1304-Bromofluorobenzene
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Client Sample ID: INLET TO 0965
Lab ID#: 1010482-02A
MODIFIED EPA METHOD TO-15 GC/MS
w102512File Name:
Dil. Factor: 5.72
Date of Collection: 10/20/20 10:00:00 A
Date of Analysis: 10/25/10 03:31 PM
(ug/m3)(ug/m3)(ppbv)(ppbv)Compound
AmountRpt. LimitAmountR t. Limit
29 Not Detected 140 Not DetectedFreon 12
29 Not Detected 200 Not DetectedFreon 114
110 Not Detected 240 Not DetectedChloromethane
29 Not Detected 73 Not DetectedVinyl Chloride
29 Not Detected 63 Not Detected1,3-Butadiene
29 Not Detected 110 Not DetectedBromomethane
29 Not Detected 75 Not DetectedChloroethane
29 Not Detected 160 Not DetectedFreon 11
110 Not Detected 220 Not DetectedEthanol
29 Not Detected 220 Not DetectedFreon 113
29 Not Detected 110 Not Detected1,1-Dichloroethene
110 Not Detected 270 Not Detected Acetone
110 Not Detected 280 Not Detected2-Propanol
29 Not Detected 89 Not DetectedCarbon Disulfide
110 Not Detected 360 Not Detected3-Chloropropene
29 55 99 190Methylene Chloride
29 Not Detected 100 Not DetectedMethyl tert-butyl ether
29 Not Detected 110 Not Detectedtrans-1,2-Dichloroethene29 Not Detected 100 Not DetectedHexane
29 65 120 2601,1-Dichloroethane
29 Not Detected 84 Not Detected2-Butanone (Methyl Ethyl Ketone)
29 440 110 1700cis-1,2-Dichloroethene
29 Not Detected 84 Not DetectedTetrahydrofuran
29 Not Detected 140 Not DetectedChloroform
29 700 160 38001,1,1-Trichloroethane
29 Not Detected 98 Not DetectedCyclohexane
29 Not Detected 180 Not DetectedCarbon Tetrachloride
29 Not Detected 130 Not Detected2,2,4-Trimethylpentane
29 Not Detected 91 Not DetectedBenzene
29 Not Detected 120 Not Detected1,2-Dichloroethane29 540 120 2200Heptane
29 87 150 470Trichloroethene
29 Not Detected 130 Not Detected1,2-Dichloropropane
110 Not Detected 410 Not Detected1,4-Dioxane
29 Not Detected 190 Not DetectedBromodichloromethane
29 Not Detected 130 Not Detectedcis-1,3-Dichloropropene
29 Not Detected 120 Not Detected4-Methyl-2-pentanone
29 17000 110 64000Toluene
29 Not Detected 130 Not Detectedtrans-1,3-Dichloropropene
29 Not Detected 160 Not Detected1,1,2-Trichloroethane
29 140 190 960Tetrachloroethene
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Client Sample ID: INLET TO 0965
Lab ID#: 1010482-02A
MODIFIED EPA METHOD TO-15 GC/MS
w102512File Name:
Dil. Factor: 5.72
Date of Collection: 10/20/20 10:00:00 A
Date of Analysis: 10/25/10 03:31 PM
(ug/m3)(ug/m3)(ppbv)(ppbv)Compound
AmountRpt. LimitAmountR t. Limit
110 Not Detected 470 Not Detected2-Hexanone
29 Not Detected 240 Not DetectedDibromochloromethane
29 Not Detected 220 Not Detected1,2-Dibromoethane (EDB)
29 Not Detected 130 Not DetectedChlorobenzene
29 1400 120 5900Ethyl Benzene
29 4400 120 19000m,p-Xylene
29 970 120 4200o-Xylene
29 Not Detected 120 Not DetectedStyrene
29 Not Detected 300 Not DetectedBromoform
29 Not Detected 140 Not DetectedCumene
29 Not Detected 200 Not Detected1,1,2,2-Tetrachloroethane
29 30 140 150Propylbenzene
29 110 140 5604-Ethyltoluene
29 39 140 1901,3,5-Trimethylbenzene
29 79 140 3901,2,4-Trimethylbenzene
29 Not Detected 170 Not Detected1,3-Dichlorobenzene
29 Not Detected 170 Not Detected1,4-Dichlorobenzene
29 Not Detected 150 Not Detectedalpha-Chlorotoluene29 Not Detected 170 Not Detected1,2-Dichlorobenzene
110 Not Detected 850 Not Detected1,2,4-Trichlorobenzene
110 Not Detected 1200 Not DetectedHexachlorobutadiene
Container Type: 1 Liter Summa Canister
Limits%RecoverySurrogates
Method
98 70-1301,2-Dichloroethane-d4
98 70-130Toluene-d8
102 70-1304-Bromofluorobenzene
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Client Sample ID: Lab Blank
Lab ID#: 1010482-03A
MODIFIED EPA METHOD TO-15 GC/MS FULL SCAN
p102222File Name:
Dil. Factor: 1.00
Date of Collection: NA
Date of Analysis: 10/22/10 11:40 PM
(ug/m3)(ug/m3)(ppbv)(ppbv)Compound
AmountRpt. LimitAmountR t. Limit
0.50 Not Detected 2.5 Not DetectedFreon 12
0.50 Not Detected 3.5 Not DetectedFreon 114
2.0 Not Detected 4.1 Not DetectedChloromethane
0.50 Not Detected 1.3 Not DetectedVinyl Chloride
0.50 Not Detected 1.1 Not Detected1,3-Butadiene
0.50 Not Detected 1.9 Not DetectedBromomethane
0.50 Not Detected 1.3 Not DetectedChloroethane
0.50 Not Detected 2.8 Not DetectedFreon 11
2.0 Not Detected 3.8 Not DetectedEthanol
0.50 Not Detected 3.8 Not DetectedFreon 113
0.50 Not Detected 2.0 Not Detected1,1-Dichloroethene
2.0 Not Detected 4.8 Not Detected Acetone
2.0 Not Detected 4.9 Not Detected2-Propanol
0.50 Not Detected 1.6 Not DetectedCarbon Disulfide
2.0 Not Detected 6.3 Not Detected3-Chloropropene
0.50 Not Detected 1.7 Not DetectedMethylene Chloride
0.50 Not Detected 1.8 Not DetectedMethyl tert-butyl ether
0.50 Not Detected 2.0 Not Detectedtrans-1,2-Dichloroethene0.50 Not Detected 1.8 Not DetectedHexane
0.50 Not Detected 2.0 Not Detected1,1-Dichloroethane
0.50 Not Detected 1.5 Not Detected2-Butanone (Methyl Ethyl Ketone)
0.50 Not Detected 2.0 Not Detectedcis-1,2-Dichloroethene
0.50 Not Detected 1.5 Not DetectedTetrahydrofuran
0.50 Not Detected 2.4 Not DetectedChloroform
0.50 Not Detected 2.7 Not Detected1,1,1-Trichloroethane
0.50 Not Detected 1.7 Not DetectedCyclohexane
0.50 Not Detected 3.1 Not DetectedCarbon Tetrachloride
0.50 Not Detected 2.3 Not Detected2,2,4-Trimethylpentane
0.50 Not Detected 1.6 Not DetectedBenzene
0.50 Not Detected 2.0 Not Detected1,2-Dichloroethane0.50 Not Detected 2.0 Not DetectedHeptane
0.50 Not Detected 2.7 Not DetectedTrichloroethene
0.50 Not Detected 2.3 Not Detected1,2-Dichloropropane
2.0 Not Detected 7.2 Not Detected1,4-Dioxane
0.50 Not Detected 3.4 Not DetectedBromodichloromethane
0.50 Not Detected 2.3 Not Detectedcis-1,3-Dichloropropene
0.50 Not Detected 2.0 Not Detected4-Methyl-2-pentanone
0.50 Not Detected 1.9 Not DetectedToluene
0.50 Not Detected 2.3 Not Detectedtrans-1,3-Dichloropropene
0.50 Not Detected 2.7 Not Detected1,1,2-Trichloroethane
0.50 Not Detected 3.4 Not DetectedTetrachloroethene
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Client Sample ID: Lab Blank
Lab ID#: 1010482-03A
MODIFIED EPA METHOD TO-15 GC/MS FULL SCAN
p102222File Name:
Dil. Factor: 1.00
Date of Collection: NA
Date of Analysis: 10/22/10 11:40 PM
(ug/m3)(ug/m3)(ppbv)(ppbv)Compound
AmountRpt. LimitAmountR t. Limit
2.0 Not Detected 8.2 Not Detected2-Hexanone
0.50 Not Detected 4.2 Not DetectedDibromochloromethane
0.50 Not Detected 3.8 Not Detected1,2-Dibromoethane (EDB)
0.50 Not Detected 2.3 Not DetectedChlorobenzene
0.50 Not Detected 2.2 Not DetectedEthyl Benzene
0.50 Not Detected 2.2 Not Detectedm,p-Xylene
0.50 Not Detected 2.2 Not Detectedo-Xylene
0.50 Not Detected 2.1 Not DetectedStyrene
0.50 Not Detected 5.2 Not DetectedBromoform
0.50 Not Detected 2.4 Not DetectedCumene
0.50 Not Detected 3.4 Not Detected1,1,2,2-Tetrachloroethane
0.50 Not Detected 2.4 Not DetectedPropylbenzene
0.50 Not Detected 2.4 Not Detected4-Ethyltoluene
0.50 Not Detected 2.4 Not Detected1,3,5-Trimethylbenzene
0.50 Not Detected 2.4 Not Detected1,2,4-Trimethylbenzene
0.50 Not Detected 3.0 Not Detected1,3-Dichlorobenzene
0.50 Not Detected 3.0 Not Detected1,4-Dichlorobenzene
0.50 Not Detected 2.6 Not Detectedalpha-Chlorotoluene0.50 Not Detected 3.0 Not Detected1,2-Dichlorobenzene
2.0 Not Detected 15 Not Detected1,2,4-Trichlorobenzene
2.0 Not Detected 21 Not DetectedHexachlorobutadiene
Container Type: NA - Not Applicable
Limits%RecoverySurrogates
Method
96 70-130Toluene-d8
92 70-1301,2-Dichloroethane-d4
92 70-1304-Bromofluorobenzene
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Client Sample ID: Lab Blank
Lab ID#: 1010482-03B
MODIFIED EPA METHOD TO-15 GC/MS FULL SCAN
w102506File Name:
Dil. Factor: 1.00
Date of Collection: NA
Date of Analysis: 10/25/10 10:49 AM
(ug/m3)(ug/m3)(ppbv)(ppbv)Compound
AmountRpt. LimitAmountR t. Limit
0.50 Not Detected 2.5 Not DetectedFreon 12
0.50 Not Detected 3.5 Not DetectedFreon 114
2.0 Not Detected 4.1 Not DetectedChloromethane
0.50 Not Detected 1.3 Not DetectedVinyl Chloride
0.50 Not Detected 1.1 Not Detected1,3-Butadiene
0.50 Not Detected 1.9 Not DetectedBromomethane
0.50 Not Detected 1.3 Not DetectedChloroethane
0.50 Not Detected 2.8 Not DetectedFreon 11
2.0 Not Detected 3.8 Not DetectedEthanol
0.50 Not Detected 3.8 Not DetectedFreon 113
0.50 Not Detected 2.0 Not Detected1,1-Dichloroethene
2.0 Not Detected 4.8 Not Detected Acetone
2.0 Not Detected 4.9 Not Detected2-Propanol
0.50 Not Detected 1.6 Not DetectedCarbon Disulfide
2.0 Not Detected 6.3 Not Detected3-Chloropropene
0.50 Not Detected 1.7 Not DetectedMethylene Chloride
0.50 Not Detected 1.8 Not DetectedMethyl tert-butyl ether
0.50 Not Detected 2.0 Not Detectedtrans-1,2-Dichloroethene0.50 Not Detected 1.8 Not DetectedHexane
0.50 Not Detected 2.0 Not Detected1,1-Dichloroethane
0.50 Not Detected 1.5 Not Detected2-Butanone (Methyl Ethyl Ketone)
0.50 Not Detected 2.0 Not Detectedcis-1,2-Dichloroethene
0.50 Not Detected 1.5 Not DetectedTetrahydrofuran
0.50 Not Detected 2.4 Not DetectedChloroform
0.50 Not Detected 2.7 Not Detected1,1,1-Trichloroethane
0.50 Not Detected 1.7 Not DetectedCyclohexane
0.50 Not Detected 3.1 Not DetectedCarbon Tetrachloride
0.50 Not Detected 2.3 Not Detected2,2,4-Trimethylpentane
0.50 Not Detected 1.6 Not DetectedBenzene
0.50 Not Detected 2.0 Not Detected1,2-Dichloroethane0.50 Not Detected 2.0 Not DetectedHeptane
0.50 Not Detected 2.7 Not DetectedTrichloroethene
0.50 Not Detected 2.3 Not Detected1,2-Dichloropropane
2.0 Not Detected 7.2 Not Detected1,4-Dioxane
0.50 Not Detected 3.4 Not DetectedBromodichloromethane
0.50 Not Detected 2.3 Not Detectedcis-1,3-Dichloropropene
0.50 Not Detected 2.0 Not Detected4-Methyl-2-pentanone
0.50 Not Detected 1.9 Not DetectedToluene
0.50 Not Detected 2.3 Not Detectedtrans-1,3-Dichloropropene
0.50 Not Detected 2.7 Not Detected1,1,2-Trichloroethane
0.50 Not Detected 3.4 Not DetectedTetrachloroethene
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Client Sample ID: Lab Blank
Lab ID#: 1010482-03B
MODIFIED EPA METHOD TO-15 GC/MS FULL SCAN
w102506File Name:
Dil. Factor: 1.00
Date of Collection: NA
Date of Analysis: 10/25/10 10:49 AM
(ug/m3)(ug/m3)(ppbv)(ppbv)Compound
AmountRpt. LimitAmountR t. Limit
2.0 Not Detected 8.2 Not Detected2-Hexanone
0.50 Not Detected 4.2 Not DetectedDibromochloromethane
0.50 Not Detected 3.8 Not Detected1,2-Dibromoethane (EDB)
0.50 Not Detected 2.3 Not DetectedChlorobenzene
0.50 Not Detected 2.2 Not DetectedEthyl Benzene
0.50 Not Detected 2.2 Not Detectedm,p-Xylene
0.50 Not Detected 2.2 Not Detectedo-Xylene
0.50 Not Detected 2.1 Not DetectedStyrene
0.50 Not Detected 5.2 Not DetectedBromoform
0.50 Not Detected 2.4 Not DetectedCumene
0.50 Not Detected 3.4 Not Detected1,1,2,2-Tetrachloroethane
0.50 Not Detected 2.4 Not DetectedPropylbenzene
0.50 Not Detected 2.4 Not Detected4-Ethyltoluene
0.50 Not Detected 2.4 Not Detected1,3,5-Trimethylbenzene
0.50 Not Detected 2.4 Not Detected1,2,4-Trimethylbenzene
0.50 Not Detected 3.0 Not Detected1,3-Dichlorobenzene
0.50 Not Detected 3.0 Not Detected1,4-Dichlorobenzene
0.50 Not Detected 2.6 Not Detectedalpha-Chlorotoluene0.50 Not Detected 3.0 Not Detected1,2-Dichlorobenzene
2.0 Not Detected 15 Not Detected1,2,4-Trichlorobenzene
2.0 Not Detected 21 Not DetectedHexachlorobutadiene
Container Type: NA - Not Applicable
Limits%RecoverySurrogates
Method
98 70-130Toluene-d8
99 70-1301,2-Dichloroethane-d4
100 70-1304-Bromofluorobenzene
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Client Sample ID: CCV
Lab ID#: 1010482-04A
MODIFIED EPA METHOD TO-15 GC/MS FULL SCAN
p102216File Name:
Dil. Factor: 1.00
Date of Collection: NA
Date of Analysis: 10/22/10 06:51 PM
%RecoveryCompound
97Freon 12
101Freon 114
90Chloromethane
98Vinyl Chloride
941,3-Butadiene
99Bromomethane
87Chloroethane
92Freon 11
132 QEthanol
99Freon 113
961,1-Dichloroethene
90 Acetone
942-Propanol
85Carbon Disulfide
973-Chloropropene
91Methylene Chloride
110Methyl tert-butyl ether
94trans-1,2-Dichloroethene100Hexane
921,1-Dichloroethane
1012-Butanone (Methyl Ethyl Ketone)
96cis-1,2-Dichloroethene
95Tetrahydrofuran
96Chloroform
981,1,1-Trichloroethane
101Cyclohexane
96Carbon Tetrachloride
982,2,4-Trimethylpentane
100Benzene
951,2-Dichloroethane108Heptane
98Trichloroethene
971,2-Dichloropropane
1041,4-Dioxane
97Bromodichloromethane
101cis-1,3-Dichloropropene
1014-Methyl-2-pentanone
98Toluene
107trans-1,3-Dichloropropene
1001,1,2-Trichloroethane
100Tetrachloroethene
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Client Sample ID: CCV
Lab ID#: 1010482-04A
MODIFIED EPA METHOD TO-15 GC/MS FULL SCAN
p102216File Name:
Dil. Factor: 1.00
Date of Collection: NA
Date of Analysis: 10/22/10 06:51 PM
%RecoveryCompound
1072-Hexanone
104Dibromochloromethane
1011,2-Dibromoethane (EDB)
100Chlorobenzene
105Ethyl Benzene
110m,p-Xylene
109o-Xylene
114Styrene
103Bromoform
116Cumene
981,1,2,2-Tetrachloroethane
112Propylbenzene
1114-Ethyltoluene
1181,3,5-Trimethylbenzene
1211,2,4-Trimethylbenzene
1051,3-Dichlorobenzene
1051,4-Dichlorobenzene
111alpha-Chlorotoluene1061,2-Dichlorobenzene
1001,2,4-Trichlorobenzene
99Hexachlorobutadiene
Q = Exceeds Quality Control limits.
Container Type: NA - Not Applicable
Limits%RecoverySurrogates
Method
101 70-130Toluene-d8
95 70-1301,2-Dichloroethane-d4
104 70-1304-Bromofluorobenzene
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Client Sample ID: CCV
Lab ID#: 1010482-04B
MODIFIED EPA METHOD TO-15 GC/MS FULL SCAN
w102502File Name:
Dil. Factor: 1.00
Date of Collection: NA
Date of Analysis: 10/25/10 08:23 AM
%RecoveryCompound
127Freon 12
124Freon 114
129Chloromethane
123Vinyl Chloride
1251,3-Butadiene
108Bromomethane
122Chloroethane
117Freon 11
116Ethanol
115Freon 113
1151,1-Dichloroethene
114 Acetone
1182-Propanol
117Carbon Disulfide
1153-Chloropropene
109Methylene Chloride
123Methyl tert-butyl ether
112trans-1,2-Dichloroethene119Hexane
1151,1-Dichloroethane
1132-Butanone (Methyl Ethyl Ketone)
116cis-1,2-Dichlor