# Ash SRE

Ash SRE Comment:
NE - miniburn - unknown if OPLs established as result of test


# Chlorine SRE

Chlorine SRE Comment:
NE - system was later modified to add carbon inj


# Condition Description

Report Name/Date:
Compliance Test Report - BIF Recertification of Compliance - Beaumont, Texas Facility; Aug, 1998

Cond Description:
CoC; max feedrate, production rate, comb temp

Content:
PM, HCl/Cl2, metals, CO emissions; metals, chlorine, and ash in feeds (As, Be, Cd, Cr, ash spiked)


Report Name/Date:
Boiler Trial Burn Report - Eastman Chemicals Company, Arkansas Eastman Div.; dated October 6, 1999


Cond Description:
Trial burn, risk burn; max conditions for feedrates and other parameters

Content:
PM, CO/HC, HCl/Cl2, metals, PCDD/PCDF, SVOCs/PAHs, DRE; POHCs, ash, metals, Cl feed analysis

Cl TE Rating Comments:
Chlorine only controlled through feedrate

Hg TE Rating Comments:
Normal, Haz waste feed is reported as zero

SVM SE Rating Comments:
Spiked Pb; made Pb and Cd stack gas; Tier I for Pb and Cd

D/F SE Rating Comments:
Conducted under max desired ESP oper temp


Report Name/Date:
Biennial RCRA Trial Burn Test Report - Rhone-Poulenc, Inc., Regeneration Unit No. 2; dated December 1996

Cond Description:
Trial burn; max cond for feedrates, comb temperature


Cond Description:
Trial burn; max cond for feedrates; min comb temp and O2

Content:
PM, CO, HCl/Cl2, DRE; POHC, ash, Cl feed analysis


Report Name/Date:
Recertification of Compliance for Tennessee Eastman Division Boilers 18, 19, and 20; dated March 24, 1998

Content:
PM, metals, CO, HCl/Cl2; feed analysis for metals, ash, HCl/Cl2


Report Name/Date:
Recertification of Compliance for Tennessee Eastman Division Boilers 21 and 22; dated August 11, 1997

Content:
PM, metals, CO, HCl/Cl2; feed analysis for metals, ash, chlorides

Cl SE Rating Comments:
no reported chlorine spiking, but Tier III

PM SE Rating Comments:
Run 2 had outlier PM level of > 0.10; not used


Report Name/Date:
Recertification of Compliance (ReCOC) for Celanese Boilers 9 & 10; No date, Report provided begins at Section 2.0

Content:
PM, CO, Cr emissions; feed analysis for metals, ash, chlorides


Content:
PM, Cr, CO emissions; feeds for metals, ash, chlorides


Report Name/Date:
Periodic Recertification of Compliance Hot Oil Heater No. 1 Down Draft Duct (EPN-12) Georgia Gulf Corporation, July 1998

Content:
PM, CO;  feedstream analysis metals, ash, chlorine


Report Name/Date:
Source Emissions Survey BASF Corp. WOD K541 Stack Risk Burn; No report date

Content:
Stack PM, HCl, Cl2, D/F, SVOC, Total Organics, CO, and O2;
Metals, D/F, Chlorine, VOCs characterization of waste feed steams.


Report Name/Date:
Source Emission Survey - Aristech Chemical Corp. - F-8 Boiler Stack (EPN 84); File No. 95-165B, September 1995

Content:
PM, HCl/Cl2, & CO emissions; metals, ash, & chlorine in waste feedstreams


Cond Description:
CoC; max feed waste liq 2EH and combined PA residue


Report Name/Date:
Recertification of Compliance Test Report for Boiler No. 2, 12/4/97; Compliance Emission Test Report - Boiler No. 2, 11/5/97

Content:
PM, CO, Cr and Cr+6 emissions; ash, Cl, and metals feeds


Report Name/Date:
Certification of Compliance for Boilers A/B & C; 5/23/97

Content:
PM, CO emissions; ash, chlorides, metals in feeds


Content:
PM, CO emissions; ash/chlorides/metals in feeds


Report Name/Date:
Recertification of Compliance for F-65630 Hot Oil Heater and Utility Boilers; 8/07/97


Report Name/Date:
Recertification of Compliance for F-65630 Hot Oil Heater and Utility Boilers; 8/31/98

Content:
PM, CO emissions only; feed analysis for ash, metals, chlorides


Report Name/Date:
Recertification of Compliance for F-57180 Hot Oil Heater; 9/06/96

Content:
PM, CO emissions, feed analysis for ash, metals, chlorides


Report Name/Date:
Test Report for Recertification of Compliance for F-57180 Hot Oil Heater; 3/09/99


Report Name/Date:
Re-Certification of Compliance for F-65630 Hot Oil Heater and Utility Boilers;8/6/97


Report Name/Date:
Re-Certification of Compliance for F-65630 Hot Oil Heater and Utility Boilers; 8/31/98


Report Name/Date:
Test Report on Re-Certification of Compliance of Boiler No. 1 & Annual Performance Test on 2 CEMS installed on Blrs 1 & 2; 10/95

Content:
PM, HCl/Cl2, CO emissions; metals, ash, chlorides in feeds


Report Name/Date:
BIF Certification of Compliance Units H-K2-001 and H-K2-002, Dec. 1996


Report Name/Date:
Re-Certification of Compliance of Boiler - PO/MTBE Steam Generators; 11/97


Report Name/Date:
Recertification of Compliance Test Report - Huntsman Polymers C Boiler; Jan, 1999

Content:
PM, HCl/Cl2, CO emissions; metals, chlorine, and ash in feeds


Report Name/Date:
Source Emission Survey - Aristech Chemical Corp. - F-8 Boiler Stack (EPN 84); 2000

Content:
HCl/Cl2, CO, D/Fs, VOC/SVOC, total organics, aldehydes/ketones, & particle size emissions; metals, ash, & chlorine in waste feedstreams


Report Name/Date:
Boiler 16 Recertificatioin of Compliance, Oct 1996

Cond Description:
Compliance Test. Maximum combustion temperature condition

Content:
Feed analysis: 10 BIF metals (not chromium only), chlorides, and ash. 
PM, CO, and hexavalent and total Cr emissions.


Cond Description:
Risk burn at max. liquid waste feedrates + min. natural gas flowrate

Content:
VOC, Total Organics, SVOCs, PCDDs/PCDFs, Particle Size Distribution, aldehides, and ketones.


Report Name/Date:
Ticona, Boiler 16 baseline test for Chrome, May 2002


Report Name/Date:
Nebraska Boiler Trial  Burn Report, December 1997

Cond Description:
Trial burn, max waste feed, min comb temp

Content:
PM, HCl/Cl2, DRE for acetophenone, cumene, phenol


Content:
CO, DRE for acetophenone, cumene, phenol


Cond Description:
Trial burn, Cr+6 burn, max waste, ash, Cl, comb temp

PM SE Rating Comments:
PM Emissions exceeded current RCRA standard


Report Name/Date:
Trial Burn Report, Vinyl II Plant, Industrial Boiler F-410, Dow Chem., Louisiana Operations, Volume 1: Report, December 19, 1997

Cond Description:
Trial burn; not used for permit setting (max oper cond)


PM SE Rating Comments:
Used to establish operating limits?  Assume N


Cond Description:
Trial burn; max waste feedrates (Cr, ash spiking)


Report Name/Date:
Trial Burn Report, Glycol I Plant, Industrial Boiler R-4, Dow Chem., Louisiana Operations, Volume 1: Report, December 12, 1997

Cond Description:
Trial burn; min comb chamber temperature


Cond Description:
Trial burn; max waste feedrates (Cr, ash spiking), steam prod rate, min L/G


Report Name/Date:
Trial Burn Report, Chlorinated Methanes, Industrial Boiler R-750, Dow Chem., Louisiana Operations, Volume 1: Report, December 22, 1997


Cond Description:
Trial burn; min combustion chamber temperature


Report Name/Date:
Stationary Source Sampling Report Ref No. 6582A, Vulcan Materials Co Chem Div, T-11 Stack, February 19-26, 1990

Cond Description:
Trial burn -- max hex feed to burner No. 1 only


Cond Description:
Trial burn -- max D-40 groundwater phase feed to burner No. 2 only


Cond Description:
Trial burn -- similar to cond 1 but at lower feedrate


Cond Description:
Trial burn -- operation with both feeds and both burners


Report Name/Date:
Results of the Feb. 1999 Compliance Certification Testing of Energy Recovery Boiler No. 1, March 3, 1999

Content:
PM, CO in stack gas (metals, chlorine in feedstreams)


Cond Description:
CoC; max firing rate, high Btu, high ash


Report Name/Date:
Recertification of Compliance for the COEN Waste Fuel Boiler, November 6, 1998

Content:
CO in stack gas; metals/chlorine/ash in feeds


Report Name/Date:
1999 Revised BIF Compliance Certification, September 1999


Report Name/Date:
Certification of Compliance, Giant Cement Co., Boiler and Industrial Furnace Regulations, August 21, 1992; Source Test Report BIF Compliance Program, Giant Resource Recovery Company, Harleyville, SC, August 13, 1992, TRC Project No. 12667-E13

Cond Description:
CoC, MAX HW FEED, SPIKED METAL, SPIKED CHLORINE

Cl TE Rating Comments:
CT vs IB rating even though SRE is rated NA


Report Name/Date:
Giant Cement Company, BIF Recertification of Compliance, Cement Kin Nos. 2, 3, 4, and 5, November 1998

Cond Description:
CoC, Max operating mode waste feed, temp, prod rate

Content:
CO, HC, HCl/Cl2, metals (no Hg stack gas), PM


Report Name/Date:
Source Emission Test on Hazardous Waste Fuels No. 4 Kiln Baghouse Exhaust Giant Cement Company, Harleyville, South Carolina, May 1989, Davis and Floyd Job No. 6781.01


Report Name/Date:
Stationary Source Sampling Report, Reference No. 10181F, Giant Cement, Harleyville, South Carolina, Unit No. 4 Baghouse Outlet, July 9 adn 10, 1991


Report Name/Date:
Giant Cement Company Boiler and Industrial Furnace Compliance Recertification Report, prepared by Roy F. Weston, WO #06633-033-001, August 1995

Cond Description:
CoC, MAX HW FIRING, MAX TIER III METALS SPIKING, MAX SLURRY FEED


Report Name/Date:
Source Emssions Survey of E.I. Du Pont De Nemours & Company, Inc. Boiler Number 7 Stack, May 1999


Report Name/Date:
Trial Burn and Certification of Compliance Test Report, Holnam, Holly Hill, SC, August, 1992

Report Prepared:
Gossman Consulting and Team Environmental


Report Name/Date:
Trial Burn and Recertification of Compliance Test Report, Kiln No. 2, April 14, 2000

Cond Description:
Max comb temp, max metals, max chlorine, max prod rate, max waste

Content:
CO, HC, HCl/Cl2, metals, PM; arsenic, lead and nickel were spiked


Cond Description:
Max APCD temp, max CO, min DRE, min comb temp


D/F SE Rating Comments:
Not evaluated: not burning hazardous waste


Report Name/Date:
Recertification of Compliance Test Report, Kiln No. 2, Holnam Holly Hill, SC, August 8, 1995

Report Prepared:
Safety Kleen, DEECO, B3 Systems, Gossman Consulting

Cond Description:
CoC, MAX  COMB TEMPS AND MAX METALS/CHLORINE FEED RATES


Cond Description:
CoC, DEMONSTRATE POHC DRE WITH MIN COMB TEMP AND MAX CO


Report Name/Date:
Air Emissions Survey Emission Test Results for Kiln No. 1 and Kiln No. 2, Holnam Holly Hill South Carolina Facility, May 15-18, 1995, DEECO Report No. 080995-1190


Cond Description:
NORMAL WASTE DERIVED FUEL FIRING, LOW APCD TEMPERATURE


Report Name/Date:
Clean Harbors Technology Corporation 1996 Annual Performance Test Report, December 3, 1996


Report Name/Date:
Annual Performance Test Program on Fluidized Bed Incinerator, Prepared by TRC Environmental Corporation, Report No. EM 97-14, December 3, 1997


Report Name/Date:
Compliance Test Report for Clean Harbors Env. Services, IN., Kimball, Nebraska Facility, Test Dates: November 16-19, 1999


Report Name/Date:
Source Emissions Testing Report for Clean Harbors Environmental Services, Kimball, NE Incinerator Facility, Comprehensive Performance Test, November 2000, Project No. CLH0387


Report Name/Date:
Test Report for Trial Burn, Vol. 1, February 1996

Cond Description:
Trial burn, max pressure wave, max feedrate


Cond Description:
Trial burn, max clorine feed, max heat content


Report Name/Date:
Trial Burn for Explosive Waste Incinerator, July 1995

Report Prepared:
U.S. Army Center for Health Promotion and Preventive Medicine

SVM SE Rating Comments:
NE - Did not pass RCRA limits for Pb, Cd

SVM SRE Rating Comments:
NE - Did not pass RCRA limits for Pb, Cd


Report Name/Date:
Trial Burn Retest for Explosive Waste Incinerator, January 1996

PM SE Rating Comments:
Tests assumed to be same campaign; more recent test added new mode of operation


SVM SRE Rating Comments:
assumed normal for Pb, no cd emission data


Report Name/Date:
Compliance Evaluation, Liquid Waste Incinerator, Catalyst Resources, Inc., Elyria, Ohio, Jan 18, 1984

Cond Description:
Compliance evaluation with skim tank material


Report Name/Date:
MHI Emission Test Results, February 1995


Cl SRE Rating Comments:
Normal, Assume Cl not controlled; SRE set to 0


Report Name/Date:
Source Emission Survey of E.I. Du Pont De Nemours & Company, Inc. Boiler 3 and 4 Stack, June 1995


Report Name/Date:
Dupont DRE Burn, Boiler No. 3 Stack, Victoria, TX, Feb. 1999


Report Name/Date:
Dupont Risk Burn, Boiler No. 3 Stack, Victoria, TX, Feb. 1999


Report Name/Date:
Dupont DRE Burn, Boiler No. 1 Stack, Victoria, TX, Feb. 1999


Report Name/Date:
Dupont Risk Burn, Boiler No. 1 Stack, Victoria, TX, Feb. 1999


Report Name/Date:
FTB-401 Trial Burn Report and Risk Report, May 26, 1998

Cond Description:
Trial burn, max prod rate, min APCS, max waste feed rate

SVM SE Rating Comments:
No Cd stack gas measurements; spiked Pb but not Tier III


Cond Description:
Trial burn, DRE, min comb temp, max stack gas flow rate


Content:
PCDD/F, stack gas metals, PSD, other organics


Report Name/Date:
FTB-603 Trial Burn Report and Risk Burn Report, June 30, 1998

Cond Description:
Trial burn, min comb temp, max stack gas flow rate


Report Name/Date:
FTB-603 Certificate of Compliance Burn, January 1997

Cond Description:
COC burn, max waste feed and production rate, max comb temp, min APCS


Report Name/Date:
Stationary Source Sampling Report, Reference No. 10000, Giant Cement, Harleyville, SC, Kiln No. 5 Dust Collector Outlet, January 30, 1991

Cond Description:
DRE TEST, also PM, metals, HCl; pre BIF rule


Report Name/Date:
Particulate Emission Evaluation No. 5 Kiln Exhaust Duct, Giant Cement Co, Harleyville, SC, Davis and Floyd, June 1989


Cond Description:
Trial burn, max waste feed, max op temp and prod rate, min APCS dP

Content:
PM, HCl/Cl2, Cr+6 (run 3 reported as run 5), CO (report only run 1, 2, and 5)


Cond Description:
Trial burn, min comb temp and max comb gas flow.


Report Name/Date:
Risk Rurn Report for Dow Facility ID No. F-2820, June 16, 2000

Cond Description:
Risk burn, normal operating cond of liq feed and comb temp


Report Name/Date:
Trial Burn Report for Boiler 53, July 2000

Cond Description:
Trial burn, max comb Temp, max steam prod rate, max feedrate, soot blow


Report Name/Date:
Trial Burn Report for Incinerator Unit 1 and 2 and Number 3 HAF Unit, October 2001


Report Name/Date:
Risk Burn Report for Incinerator Unit 1 and 2 and Number 3 HAF Unit, October 2001

Cond Description:
Risk burn, normal op cond, PCB containing material


Report Name/Date:
BIF Certification of Compliance Report, Holnam Artesia, Mississippi, prepared by SciTech, August 19, 1993


Report Name/Date:
Trial Burn and Recertification of Compliance Test Report, Sept 2000

Cond Description:
CoC: Max comb temp, max metal and chlorine feed rate, max prod rate, min ESP power

Content:
PM, HCl, metals (Cl2 not measured by accident)

SVM SE Rating Comments:
Run 3 (13) not used in cond avg since ESP went off line

LVM SE Rating Comments:
Run 3 (46) not used in cond avg since ESP went off-line


Cond Description:
CoC: Min comb temp. max feed rate, max ESP temp


Report Name/Date:
Annual Stack Test Report, Holnam Artesia, Mississippi; Stack Sampling Report, Holnam Inc., Artesia Mississippi, July 1994

Cond Description:
State of MS testing, ANNUAL STACK SAMPLING WITH SF6 SPIKE


Report Name/Date:
BIF Certification of Compliance Report, Holnam, Artesia MS, August 19, 1993


Report Name/Date:
Annual Stack Test Report, Holnam Artesia, Mississippi; Stack Sampling Report, Holnam Inc., Artesia Mississippi

Cond Description:
State of Mississippi required annual testing, DRE TEST USING SF6

LVM SE Rating Comments:
Not evaluated: No arsenic emissions data


Report Name/Date:
Recertification of Compliance Test Report, Holnam Artesia MS, August 16, 1996

Cond Description:
CoC, MAX COMB ZONE TEMP, MAX METALS/CHLORINE FEED RATES


Report Name/Date:
Trial Burn and Recertification of Compliance Report, prepared for Holnam Clarksville Missouri, prepared by Schreiber, Grana, and Yonley, September 10, 1996

Cond Description:
CoC, DRE, MIN COMB ZONE TEMP, MAX HWDF FEED RATE


Cond Description:
CoC, MAX COMB ZONE TEMP, MAX SLURRY/METALS FEED, MIN ESP POWER


Report Name/Date:
Particulate Matter Emissions Testing and Continuous Emission Rate Monitoring System Certification, Holnam, Clarksville, Missouri, Fugro Midwest Report 0895-2230, November 6, 1995

Cond Description:
PM EMISSIONS TESTING AND CEM CERTIFICATION


Report Name/Date:
Trial Burn and Certification of Compliance Test Report, Holnam, Safety Kleen, Clarksville, Missouri, Prepared by Gossman Consulting, July 1992

Testing Firm:
Team Environmental, Air Compliance Technologies


Cond Description:
BASELINE, no hazardous waste firing, MAX COMB TEMP


Report Name/Date:
Engineering Evaluation Test Report, Testing During Four Test Conditions for Dioxin/Furan Emissions, HCl, SO2, and Kiln Dust from Kiln Discharge Stack and Dust Collector, DEECO Report No. 94-1124A and B, July 18, 1994


Report Name/Date:
Engineering Evaluation Test Report, Testing During Four Test Conditions for Dioxin/Furan Emissions, HCl, SO2, and Kiln Dust from Kiln Discharge Stack and Dust Collector, DEECO Report No. 94-1124B, July 18, 1994


Cond Description:
CoC, MAX GAS FLOW RATE, MAX CHLORINE FEED, MAX APCD TEMP


Report Name/Date:
Trial Burn and Recertification of Compliance Test Report, Kiln No. 1, July 31, 2000

Cond Description:
Max comb temp, max metals, max chlorine, max prod rate


Cond Description:
Max APCD temp, max CO, max feed, min comb temp


Report Name/Date:
Recertification of Compliance Test Report, Kiln No. 1, Holnam Holly Hill, SC, September 15, 1995

Cond Description:
ReCoC, HIGH COMB TEMP, HIGH METALS FEED, HIGH CHLORINE


Report Name/Date:
Memo from Charles Kellet to H. Rigo, "Holnam Holly Hill Kiln 1 Normal Data," August 17, 1995


Cond Description:
BASELINE, NO WASTE DERIVED FUEL, NORMAL APCD INLET TEMP

PM SE Rating Comments:
Not evaluated: not burning hazardous waste


Report Name/Date:
BIF Compliance Certification, Cement Kiln Number One, Keystone Cement, Bath PA, August 1992,  Amendments submitted January 1993

Cond Description:
CoC, MAX PROD, MAX TIER III SPIKE, MAX SLURRY FEED


Report Name/Date:
BIF Recertification of Compliance, Number 1 Kiln, Keystone Cement Company, Bath, Pennsylvania, November 6, 1998

Cond Description:
CoC; max metals, chlorine, waste, slurry, min ESP power


Report Name/Date:
RCRA Trial Burn Test Report, Keystone Cement Company, Kilns No. 1 and No. 2, Bath, PA, Test Dates: 7-10 December 1999, April 2000

Cond Description:
Trial burn; Low temp POHC DRE, PCDD/PCDF


Report Name/Date:
BIF Recertification of Compliance, Cement Kiln No. 1, W. O. No. 02329.030.001, October 4, 2000


Cond Description:
CoC, MAX PROD, >25% TIER III SPIKE, MAX SLURRY FEED


Report Name/Date:
Keystone Cement Company, Bath, Pennsylvania, Source Emissions Compliance Test Report, Test Dates October 28 - November 1, 1996, January 1997, Work Order No. 0239-019-001


Report Name/Date:
BIF Compliance Certification, Cement Kiln Number Two, Keystone Cement, Bath PA, August 1992,  Amendments submitted January 1993


Report Name/Date:
BIF Recertification of Compliance, Number 2 Kiln, Keystone Cement Company, Bath, Pennsylvania, November 6, 1998


Content:
POHC DRE, PM, HCl/Cl2, HC, metals (no spiking)


Report Name/Date:
Stationary Source Sampling Report, Reference No. 10816, LWD Inc., Calvert City, KY, Unit No. 3, January 1993


Report Name/Date:
Stationary Source Sampling Report, Reference No. 12563, LWD, Calvert City, KY, Unit No. 3, January 1994


Report Name/Date:
Stationary Source Sampling Report, Reference # 11658, LWD, Inc., Hazardous Waste Incineration Testing, Unit No. 1, Calvert City, Kentucky, Prepared by Entropy, March 1993


Report Name/Date:
Stationary Source Sampling Report, Reference # 11606, LWD, Inc., Hazardous Waste Incineration Testing, Unit No. 2, Calvert City, Kentucky, Prepared by Entropy, March 1993


Report Name/Date:
RES(TX) Trial Burn Program Incinerator Train II Emission Test Results, Rollins Environmental Services, Deer Park, Texas, Prepared by Alliance Technologies, Project # 5-888-999, August 1998


Report Name/Date:
April 1994 Quarterly Test Emission Results for Lead and Particulate Matter, Waste Technologies Industries, E. Liverpool, Ohio, Prepared by ENSR Consulting and Engineering, Project # 7136-014-400, January 1995

Cond Description:
QUARTERLY EMISSION TEST FOR PB AND PM, CARBON INJECTION


Report Name/Date:
Quarterly Test Emission Results for Lead and Particulate Matter, Waste Technologies Industries, E. Liverpool, Ohio, Prepared by ENSR Consulting and Engineering, Project # 7136-015-400, March 1995


Report Name/Date:
1995 Annual Performance Test Emission Results, Waste Technologies Industries, E. Liverpool, Ohio, Prepared by ENSR Consulting and Engineering, Project # 7136-017-400, November 1995

Cond Description:
ANNUAL PERFORMANCE TEST, NORM WASTE FEED, CARBON INJECTION


Report Name/Date:
Quarterly Test Emission Results, Waste Technologies Industries, E. Liverpool, Ohio, Prepared by ENSR Consulting and Engineering, August 1994

Cond Description:
QUARTERLY COMPLIANCE, NORMAL CONDITIONS, CARBON  INJECTION


Report Name/Date:
Quarterly Test Emission Results, Waste Technologies Industries, E. Liverpool, Ohio, Prepared by ENSR Consulting and Engineering, December 1994

Cond Description:
QUARTERLY COMPLIANCE, NORMAL CONDITIONS, CARBON INJECTION


Report Name/Date:
Mercury Removal Efficiency Stack Testing Report, WTI Facility, East Liverpool, Ohio, December 2, 1993

Cond Description:
HG STACK TESTING W/ENHANCED CARBON INJECTION SYSTEM


Report Name/Date:
Final Trial Burn Report for the Rotary Kiln Incinerator, Waste Technologies Industries, East Liverpool, Ohio, Prepared by ENSR, Document Number 7136-001-800, May 1993

Cond Description:
MAX FEED METALS,CL2,SCC TEMP,KILN AQEOUS, NO CARBON INJ

Cl SE Rating Comments:
NE - system was later modified to add carbon inj

Cl SRE Rating Comments:
NE - system was later modified to add carbon inj

LVM SE Rating Comments:
NE - carbon injection system not used, old APCS


Report Name/Date:
1997 Annual Performance Test Emission Results


Report Name/Date:
1998 Annual Performance Test Emission Results


Report Name/Date:
1999 Annual Performance Test Emission Results


Report Name/Date:
CY 2000 Annual Performance Test Emission Results


Cond Description:
MAX FEED SLUDGE,SCC AQ.LIQ, NO CARBON INJECTION


Cond Description:
MAX FEED SOLIDS, MIN SCC TEMP., NO CARBON INJECTION


Report Name/Date:
Preliminary Testing Results for the Enhanced Carbon Injection System, July 30, 1993


Report Name/Date:
Demonstration of Carbon Injection Testing System, Provided by Region 5 EPA, February 1994


Report Name/Date:
Final Trial Burn Report for Condition 2, Waste Technologies Industries, East Liverpool, Ohio, Prepared by ENSR, Document Number 7136-071-400, April 1994


Report Name/Date:
April 1994 Quarterly Test Emission Results for PCDDs/PCDFs and Particulate Matter, Waste Technologies Industries, E. Liverpool, Ohio, Prepared by ENSR Consulting and Engineering, Project # 7136-009-400, May 1994


Report Name/Date:
Quarterly Test Emission Results for Lead and Particulate Matter, Waste Technologies Industries, E. Liverpool, Ohio, Prepared by ENSR Consulting and Engineering, Project # 7136-009-400, June 1994

Cond Description:
QUARTERLY EMISSION TEST FOR PM AND PB, CARBON INJECTION


Report Name/Date:
Quarterly Test Emission Results for Lead and Particulate Matter, Waste Technologies Industries, E. Liverpool, Ohio, Prepared by ENSR Consulting and Engineering, Project # 7136-012-400, September 1994


Report Name/Date:
Ash Grove Foreman Arkansas, RCRA Trial Burn Report and Certification of Compliance for Kiln No. 2, May 1992

Cond Description:
CoC, APCD TEMP > 450, MAX HW FEED, MAX PROD


Report Name/Date:
RCRA Cement Kiln Test Burn Report Kiln 3, April 1998

Cl SE Rating Comments:
Source 403 currently represents this kiln for metals/chlorine

PM SE Rating Comments:
Not evaluated: failed Run 1 (> 0.08 gr/dscf)


Cond Description:
D/F test at max APCD temp and max CO, APCD worst case


Report Name/Date:
RCRA Cement Kiln Test Burn Report Kiln 1 and 2, April 1998


SVM SE Rating Comments:
Data from source 403 represents current emissions from this kiln for metals

SVM SRE Rating Comments:
Data from source 403 represents current performance of this kiln for metals

LVM SE Rating Comments:
Data from source 403 currently represents this kilns emissions

LVM SRE Rating Comments:
Data from source 403 currently represents this kilns emissions

LVM TE Rating Comments:
Data from source 403 currently represents this kilns emissions


Report Name/Date:
Ash Grove Foreman Arkansas, Report on Destruction and Removal Efficiency Determined at Minimum Combustion Chamber Temperature, Kiln No 2, submitted July 1993


Report Name/Date:
Data contained in letter from Steven Bales (Ash Grove) to Warren Owens (REI), dated November 18, 1993

Cond Description:
TO STUDY THE FORMATION OF DIOXINS/FURANS


Report Name/Date:
Source Emission Survey of Ash Grove Foreman Cement, Kiln No 2 North and Sorth Stacks, Foreman Arkansas, October 1988, METCO File Number 88-170


Report Name/Date:
Trial Burn Report, Acrylonitrile Boiler Solutia Chocolate Bayou Plant

Testing Firm:
ENSR of Acton, Mass. & Maxim Corp. of Houston TX

Cond Description:
Trial burn; low temp "worst-case" organic destruction

Content:
DRE for HCN; PM, HCl/Cl2, CO, PCDD/PCDF, PICs emissions; metals, ash, chlorine, HCN in feedstreams


Cond Description:
Trial burn; max waste feed, max prod rate

Content:
DRE for HCN; PM, HCl/Cl2, CO, metals, PCDD/PCDF, PICs emissions; metals, ash, chlorine, HCN in feedstreams


Content:
DRE for HCN; CO emissions; metals, ash, chlorine, HCN in feedstreams


Cond Description:
TB, One kiln operating, max metals feed, Worst case for spiked metals (As, Be, Cr), max temp


Cond Description:
TB, Two kilns operating, worst case for PM and HCl, min temp, no spiking


Report Name/Date:
Trial Burn Report for Incinerator Unit 1 and 2, October 2001


Cond Description:
Trial burn, higher temp for DRE and metals

LVM SRE Rating Comments:
Metals taken for info purposes only, normal


Report Name/Date:
Risk Burn Report for Incinerator Unit 1 and 2, October 2001

Cond Description:
Risk burn, normal op cond, non-PCB containing material


Report Name/Date:
Trial Burn Report for Dow Chemical U.S.A. Louisiana Division Solvents Incinerator


Report Name/Date:
RCRA Compliance Test Results - Final Report, October 1993

Cond Description:
Trial burn, mixed agent VX/munitions feed

PM SE Rating Comments:
Tests assumed to be same campaign; 93 test added new mode of operation

Hg SE Rating Comments:
Tests considered to be the same campaign; recent test added new mode of operation


Report Name/Date:
RCRA Compliance Test Results - Final Report, April 1992

Cond Description:
Trial burn, mixed agent HD/munitions feed


Report Name/Date:
Results of the Chromium Emissions Report, May 1993


Report Name/Date:
RCRA Compliance Test Results for the Ton Container Heel Tests on the Metals Parts Furnace with Agent VX, Chemical Agent Munitions Disposal System (CAMDS), Tooele, Utah, Final Report, December 1994.

Report Prepared:
Science Applications International Corporation and TRC

Content:
PM, HCl/Cl2, metals, DRE, PCDD/F,VOC/SVOC (Runs 2, 4, 5)

PM SE Rating Comments:
Tests assumed to be same campaign; 95 test added new mode of operation


Report Name/Date:
Test Burn Report - Metals Parts Furnace Performance Standard Demonstration Burn Using Ton Containers with GB Heels

Content:
PM, HCl/Cl2, metals, DRE, PCDD/F,VOC/SVOC (Runs 4-6)


Cond Description:
Baseline - one run w/nat gas only without agent GB

Content:
PM, HCl/Cl2, metals, DRE, PCDD/F,VOC/SVOC


Report Name/Date:
Tooele Chemical Agent Disposal Facility (TOCDF), RCRA Agent Trial Burn Report for the Liquid Incinerator System #2, Revision 1, June 19, 1998

LVM SE Rating Comments:
Assumed metals not spiked and operating limits not established

LVM SRE Rating Comments:
Assumed metals not spiked and operating limits not established


Report Name/Date:
LIC Metals Demonstration Test Report, September 28, 2001

PM SE Rating Comments:
Tests assumed to be same campaign; 00 test added new mode of operation


Cond Description:
Worst case mini-burn to demo compliance with HWC MACT stnds

PM SE Rating Comments:
NE - unclear if mini-burn was used to establish operating limits


Report Name/Date:
Cytec Industries, Willow Island, West Virginia, Preliminary Compliance Determination for the Fluidized Bed Incinerator Pursuant to HWC MACT Regulations, ENSR, February 29, 2000, Project No. 0270-047-400

Cond Description:
Normal wastes, APCD operation, low comb temp


Cond Description:
Normal wastes, APCD operation, high comb temp


Report Name/Date:
Cytec Industries, Willow Island, West Virginia, Phase II, Preliminary Compliance Determination for the Fluidized Bed Incinerator Pursuant to HWC MACT Regulations, ENSR, September 7, 2000, Project No. 0270-047-900


Report Name/Date:
TEAD-N Incinerator Trial Burn Report, 6 December 1993, Air Pollution Emission Assessment No. 42-21-M665-93, RCRA Trial Burn for Deactivation Furnace, Tooele, Utah, 9-31 Autust 1993, Prepared by the U.S. Army Environmental Hygiene Agency


Cond Description:
Trial burn, 0.5 caliber M17 tracer/ Cr powder. Max oper cond.


PM SE Rating Comments:
Both 00 and 01 tests assumed to be same campaign; 00 test added new mode of operation

LVM SE Rating Comments:
Assumed no spiking and that risk burn reflected normal ops even though emissions were higher than previous compliance test


Report Name/Date:
Results of the February 25, 1986, Performance Evaluation Test on the Incinerator Scrubber at the Waste Research and Reclamation Plant in Eau Claire, Wisconsin, March 7, 1986


Report Name/Date:
Results of the July 1-3, 1986, Performance Tests on the Hazardous Waste Solvent Incinerator at the WR&R Plant in Eau Claire, Wisconsin, August 18, 1986

SVM SE Rating Comments:
NE - failed PM test, negative SVM SRE?, no Cd emission data


SVM SE Rating Comments:
NE - failed PM test, no Cd emission data


Report Name/Date:
Results of the July 24, 1986, Diagnostic Test on the Incinerator Scrubber at the WR&R Plant in Eau Claire, Wisconsin, July 31, 1986, Report Number 6-2250


Report Name/Date:
Results of the February 19, 1987, Particulate and Carbon Monoxide Emission Compliance Test on the Hazardous Waste Incinerator Wet Scrubber Stack at the WR&R Plant in Eau Claire, Wisconsin, February 23, 1987, Report Number 7-2336

SVM SE Rating Comments:
NE - no Cd emission data, negative SVM SRE?


Report Name/Date:
B.I.F. Certification of Compliance, C.O.C. Report & Attachments, Stack Test Report and Appendix, Submitted August 20, 1992

Testing Firm:
Air Pollution Characterization and Control, Ltd.

PM SE Rating Comments:
Not evaluated: failed run 1 (> 0.08 gr/dscf)


Report Name/Date:
RCRA Trial Burn for the Burning of Waste-Derived Fuels for Energy Recovery at Essroc Cement Corp., Logansport, Indiana, APCC Project 98062, March 1999

Report Prepared:
Air Pollution Characterization and Control, LTD

Cond Description:
CoC; Min temp, max CO, POHC DRE, min ESP power

Content:
PM, HCl/Cl2, CO, HC, D/F, SVOC, VOC, TOE


Cond Description:
CoC; Max operating temp, max temp, feedrates


Content:
PM/PSD, D/F, organics (SVOC, VOC), HCl/Cl2, CO, HC


Report Name/Date:
Particulate Emissions, ESP Collection Efficiency, and Dioxin/Furan (PCDD/PCDF) Emission Testing at Essroc Materials Inc., Logansport, Indiana, prepared by Air Pollution Characterization and Control, Ltd., September 1993, APCC Project No. 93023

Report Prepared:
Air Pollution Characterization and Control, Ltd.


Report Name/Date:
Supplemental Fuel Trial Burn, Coplay Cement, Logansport Indiana, May 1987, prepared by TRC, TRC project No. 3919-E71, September 1987


LVM SE Rating Comments:
Not evaluated: pre-BIF Rule data; no Be emissions data


LVM SRE Rating Comments:
Not evaluated: pre-BIF Rule data; SRE based on As and Cr only


Cond Description:
Trial burn, high waste feedrate, min temp oper


Cond Description:
Trial burn, high wet solids feed rate, low temp oper


Cond Description:
Trial burn, high viscous liquid feed rate, low temp oper


Cond Description:
Trial burn, high nonviscous liquid feed rate, max comb temp


Report Name/Date:
Clean Harbors Technology Corp 1995 Annual Performance Test Report, January 15, 1996


Cond Description:
Trial burn, max feedrate, max #3 hearth temp


Report Name/Date:
Trial Burn Test Report for the Eastman Kodak B-95 Multiple Hearth Incinerator, March 2002

Cond Description:
Trial Burn, min secondary comb chamber (SCC) operating temp

Content:
PM, HCl/Cl2, CO, HC, VOC/SVOC, POHC DRE, D/F


Cond Description:
Trial Burn, max waste feed, max SCC operating temp


Report Name/Date:
Third and Fourth Mini Burn Report. October 1995

Cond Description:
Mini-burn, max feedrate, max temp at 1685 °F


Cond Description:
Mini-burn, max feedrate, max temp at 1615 °F


Cond Description:
Mini-burn, max feedrate, max temp at 1600 °F


Cond Description:
Mini-burn, max feedrate, max temp at 1505 °F


Cond Description:
Mini-burn, max feedrate, max #3 hearth temp


Report Name/Date:
Final Trial Burn Report for Caloric 1 Incinerator. November 1998


Report Name/Date:
Final Trial Burn Report for Caloric 2 Incinerator. November 1998


Report Name/Date:
Trial Burn Report for No.2 Fixed Box Incinerator, Vol-1, July 9, 1992

Report Prepared:
Industrial and Environmental Analysts(IEA), Inc

Cond Description:
Trial burn, maximum heat duty, maximum ash and chlorine feed

Content:
PM, HCl/Cl2, CO, HC, Metals, Hexavalent Chromium, SVOC, VOC


Cond Description:
Trial burn, maximum heat duty, reduced ash and chlorine feed


Report Name/Date:
Stationary Source Sampling Report, Reference No. 12521, Merck Sharp and Dohme Quimica, Barceloneta, Puerto Rico, April 1996

Cond Description:
Trial burn, min temp, solid and liquid waste


Cond Description:
Trial burn, max temp, solid and liquid waste


Report Name/Date:
Annual Stack Emission Test Report, December 2000


Cond Description:
Trial burn, max feedrate and max comb temp


Cond Description:
Trial burn, min comb temp (data considered invalid due to VOST analyses after holding time allowance.  Testing rerun in Dec. 1999).


Report Name/Date:
Risk Burn (do not have complete report, all we have is PCDD/PCDF results table)


Report Name/Date:
VA-5 Incinerator Trial Burn/Risk Burn Report, February 2000


Report Name/Date:
RCRA Trial Burn Test Report, January 1999


Cl SE Rating Comments:
Run 1 (219.9) is high outlier and not included in cond avg


Report Name/Date:
Trial Burn Report, Oxy Vinyls, LP Houston Chemical Complex, Deer Park - VCM Site Organic Chloride Incinerators HCIN2 & HCIN3 Haz Waste Permit App., May 1999


Cond Description:
Trial burn - worst-case PM/HCl/metals; As/Cr spiked

Content:
PM, HCl/Cl2, metals (As/Cr), Cr6, CO & waste feed ash/Cl/metals


Cond Description:
Risk burn (Slightly higher than annual median waste feedrate)

Content:
Metals, D/Fs, CO, Cr6, PSD, V/SV PICs, feed metals/ash/Cl


Report Name/Date:
PIC Risk Burn Report, Lone Star Industries, February, 2001


Report Name/Date:
Final Recertification of Compliance Test Report, Lone Star Industries, January 2001


Report Name/Date:
Lafarge Corp Paulding Plant Compliance Test, Certification Package, prepared by Radian, August 1992

Cond Description:
CoC, MAX COMB TEMP, MIN ESP POWER, MAX PROD


Report Name/Date:
Lafarge Corp Paulding, Ohio, August 1998 Trial Burn Report, August 1998

Cond Description:
CoC; high temperature, max metals, prod rate, waste feed


Content:
PM/PSD, metals, D/F, organics, HCl/Cl2, CO


Report Name/Date:
Lafarge Corp Paulding Ohio, Certification of Compliance, Alternative Carbon Monoxide Standard, prepared by Radian, September 1994


Report Name/Date:
Lafarge Corp Paulding Ohio Plant, Recertification of Compliance, prepared by Radian, submitted August 1995


Report Name/Date:
PCDD/PCDF Testing Data from Lafarge Paulding, Radian Testing during Summer 1994, CRKC Docket No. 733, contained in letter from CKRC to EPA OSW


Report Name/Date:
Filterable, Condensible, and Total Particulate, Dioxins and Furans, Multi-Metals, Hydrogen Chloroide, and Chlorine Emissions Evaluation Conducted March 12-16, 2001, Report Date July 2001

Report Prepared:
Air Control Techniques, P.C.,  En-Tellect Environmental Services Inc.


Report Name/Date:
Certification of Compliance and Comprehensive Performance Test Report. Ash Grove Cement Co., Chanute, Kansas, Notification of Compliance and Comp Perf Test Report, June 12, 2002


Cond Description:
Comp Perf Test, raw mill off, PCDD/PCDF retest


Report Name/Date:
Air Pollution Emission Assessment No. 42-EK-1463-97 -- Trial Burn and Health Risk Assessment Emissions Test for APE 1236 DFS - McAlester Army Ammunition Plant, McAlester, OK, February 12 - March 14, 1997


Cond Description:
M43A1/M1911 Mixed munitions, metal powder


Report Name/Date:
No. 5133E/5307B, Eli Lilly and Company, Clinton, Indiana, RCRA Hazardous Waste Incineration Testing, Condition 6 and Normal Waste Feed, TO3 Incinerator Stack, June 19 and September 30, 1986


Cond Description:
Trial burn, normal operations; permit test cond OPL for PM


Report Name/Date:
Trial Burn and Risk Burn Report and Revised Certification of Compliance, Transfer of Interim Status. October 2000


Report Name/Date:
Comliance Recertification for Bostik's Struthers-Wells Burner Unit Pursuant to the BIF Regulations. February 16, 2000


Report Name/Date:
Stationary Source Sampling Report, Ref No. 6363-B, Burroghs Wellcome Co. Greenville, NC,  Hazardous Waste Incineration Testing, NAO Incinerator Stack, July 19, 20, 21, 1989

Cond Description:
Trial Burn, incinerator temperature of  1850 °F


Cond Description:
Trial Burn, incinerator temperature of  1950 °F


Report Name/Date:
Stationary Source Sampling Report, Reference No. 6189, Burroghs Wellcome Company, Greenville, North Carolina, Prenco Incinerator Stack, February and March, 1989


Cond Description:
Trial burn, 1800F, chlorobenzene, chloroform, toluene


Cond Description:
Trial burn, 1700F, chlorobenzene, chloroform, toluene


Report Name/Date:
Certification of Compliance Stack Emission Test Program at Lonestar Industries, Inc., Cape Girardeau, Missouri, April and June 1992, BIF CoC Test Report, Revised January 1993, APCC Project 92007

Report Prepared:
Air Pollution Characterization and Control

Testing Firm:
Air Pollution Characterization and Control

Cl SE Rating Comments:
Not evaluated: not burning hazardous waste

Hg SE Rating Comments:
Not evaluated: not burning hazardous waste

SVM SE Rating Comments:
Not evaluated: not burning hazardous waste

SVM SRE Rating Comments:
Not evaluated: not burning hazardous waste

LVM SE Rating Comments:
Not evaluated: not burning hazardous waste

LVM SRE Rating Comments:
Not evaluated: not burning hazardous waste

LVM TE Rating Comments:
Not evaluated: not burning hazardous waste


Cond Description:
CoC, HIGH COMB TEMP, IN-LINE RAW MILL OFF


Report Name/Date:
Report on Diagnostic Testing, Conducted at Lone Star Industries Stack, Cape Giradrdeau, CAE Project No. 6764, Octoeber 21, 1993

Cond Description:
COAL AND HWF COMBINATION, IN-LINE RAW MILL ON


Report Name/Date:
Emission Measurements for the Burning of Tires at Lone Star Industries, Cape Girardeau, Misssouri, APCC Project 92003, September 1992

Testing Firm:
Air Pollution Characterization and Control, LTD


Report Name/Date:
Trial Burn Report, Lone Star Industries, Cape Girardeau, MO, prepared by Gossman Consulting, December 1995; Report on Trial Burn Testing, conducted at Lone Star Industries, Main Stack, Cape Girardeau, Missouri, CAE Project No. 7576, December 27, 1995

Cond Description:
Trial burn, HIGH COMB TEMP, IN-LINE RAW MILL OFF


Report Name/Date:
Final Trial Burn Report for Light Weight Aggregate Kiln Process Utilizing Low Grade Fuels, Norlite Corporation, Cohoes, New York, Prepared by ENSR, Document Number 9514-016-500, December 1992


Report Name/Date:
RCRA Trial Burn Report for Light-Weight Aggregate Kilns 1 and 2, Aug 1999

Cond Description:
Trial Burn, Minimum operating temperature


Cond Description:
Trial Burn, elevated operating temperature, metals spiking

Content:
PM, HCl/Cl2, CO, HC, SVOC, VOC, D/F, Metals

D/F SE Rating Comments:
Copper spiked to maximize potential for D/F formation.  Is there a Cu feedrate limit?


Report Name/Date:
Risk Burn Final Report for Light-Weight Aggregate Kilns 1 and 2, Aug 2000

Cond Description:
Risk Burn, elevated waste feed rates, maximum temperature, minimum scrubber pH

D/F SE Rating Comments:
Not evaluated: report indicated metals spiking interferred with combustion efficiency


Report Name/Date:
Risk Burn-Phase 2 Final Report for Light-Weight Aggregate Kilns 1 and 2, Sept 2001

Cond Description:
Risk Burn, metal feeds equiv. to Jan '97 permit


Cond Description:
Risk Burn, metal feeds equiv. to June '01 permit


LVM SE Rating Comments:
Run 2 Cr emission outlier (739), not used in cond avg


Cond Description:
CoC, LOW COMB TEMP, HIGH HALOGEN FEED, HIGH SHW FEED


Cond Description:
CoC, HIGH COMB TEMP, HIGH HALOGEN FEED, HIGH SHW FEED


Report Name/Date:
Emission Test Report for No. 4 Aggregate Kiln Solite Corporation, Leaksville Plant, Cascade, Virginia, Prepared by IEA, August 8, 1992


Report Name/Date:
RCRA Testing, Kilns 1,2,3,4, Certification of Compliance, August 1999


Report Name/Date:
Trial Burn Report, Solite Corp, Virginia Solite Div., March 2000

Cond Description:
Trial Burn, organics DRE, HCl/Cl2 emissions limits


Report Name/Date:
Trial Burn Report, Kiln 1 DRE Retest, Kilns 1-4 D/F. Solite Corp, Virginia Solite Div., July 2000

D/F SE Rating Comments:
NE- Research testing, D/F retest at lower FF temperature


Report Name/Date:
Emission Test Report for No. 4 Aggregate Kiln Solite Corporation, Leaksville Plant, Cascade, Virginia, Prepared by IEA August 8, 1992


Report Name/Date:
Stationary Source Sampling Report, Reference # 13967, Virginia Solite Company, Leaksville Plant, Cascade, Virginia, May 1995


Report Name/Date:
Emmision Test Results for No. 7 and No. 8 Aggregate Kilns, Solite Corporation, Arvonia, Virginia, Prepared by IEA, Project # 1381-003, August 8, 1992; COC Forms attached, August 21, 1992


Report Name/Date:
Trial Burn Report, Solite Corporation, A. F. Old Facility, Arvonia, Virginia, March 2000; Entropy Stationary Sampling Report, Reference No. 1702, Solite Corp Arvonia, VA, November and December 1999


Report Name/Date:
Recertification of Compliance for Kilns 7 and 8, Solite Corp, Arvonia, VA, July 27, 1999; Entropy Stationary Sampling Report, Reference No. 17091, Solite Corp Arvonia, VA, May 1999;


Cond Description:
CoC testing, metals and chlorine SRE demo


Report Name/Date:
PCDD/PCDF Emissions Testing Kiln 8, Solite Corporation, Arvonia, Virginia, EPA ID # VAD042755082, January 1997


Report Name/Date:
COC Forms AF Old Kiln No. 8, Solite Corporation, Arvonia, Virginia, March 18, 1996

SVM SE Rating Comments:
Unusually high SVM level in HW, likely due to unreported spike contribution?

LVM SE Rating Comments:
High LVM level in HW, likely from unreported spike contribution


Report Name/Date:
Texas Industries, Midlothian Cement Plant, Second Revision, Certification of Compliance, submitted to EPA Region VI and Texas Waste Commission of May 24, 1993, Revised October 10, 1992, prepared by Entellect

Cond Description:
CoC, DRE Mode 1, MAX HW FEED, POHC SPIKING, NO QUENCH

PM SE Rating Comments:
Data from 473 represents this kilns current emissions


SVM SE Rating Comments:
Data from source 473 represents current emissions from this kiln

SVM SRE Rating Comments:
Data from source 473 represents current performance of this kiln

LVM SE Rating Comments:
No Cr emissions.  Also data from source 473 currently represents this kiln

LVM SRE Rating Comments:
Data from source 473 currently represents this kiln

LVM TE Rating Comments:
Data from source 473 currently represents this kiln


Report Name/Date:
Report on Polychlorinated Dibenzo-p-Dioxins and Polychlorinated Dibenzofurans Testing, Conducted at Continental Cement, CAE Project No. 6922, February 25, 1994


Report Name/Date:
Report on Diagnostic Testing, Performed for Continental Cement Company Stack, Hannibal, Missouri, CAE Project No. 6677-1, August 23, 1993


Report Name/Date:
Report on Diagnostic Testing, Conducted at Continental Cement, Hannibal Missouri, CAE Project No. 6394, December 15, 1992


Report Name/Date:
Summary Report on PM Diagnostic Testing Conducted at Continental Cement, Hannibal, Missouri, CAE Project No. 6173/1, May 22, 1992

PM SE Rating Comments:
Not evaluated: failed run 4 (>0.08 gr/dscf)


Report Name/Date:
Air Source Technologies Report Prepared for Continental Cement, Project No. 411241, January 14, 1992


Report Name/Date:
Trial Burn and Certification of Compliance Test Report, Continental Cement Company, Hannibal, Missouri, July 1992


Report Name/Date:
Emissions Testing of a Wet Cement Kiln at Hannival, Missouri, for U.S. EPA OSW, prepared by MRI, December 1990


Report Name/Date:
Emissions Testing of a Wet Cement Kiln at Hannibal, Missouri, for U.S. EPA OSW, prepared by MRI, December 1990


Report Name/Date:
Report on Air Emissions Demonstration Testing, performed for Continental Cement Company, Kiln Stack, Back Housing, Cooler Stack, and ID Fan Outlet, Hannibal Missouri, CAE Project No. 6967, June 1, 1994


Report Name/Date:
Emission Test Report, Emissions Testing for PCDD/PCDF, PCBs, Volatiles, Semivolatiles, BIF Metals, and Particulates, Continental Cement, Hannibal, Missouri, DEECO Report 95-1192, February 16, 1995


Report Name/Date:
Trial Burn Report, Continental Cement Company, prepared by Gossman Consulting, September 1996

Cond Description:
TB, MAXIMUM TEMPERATURE CONDITIONS, metals testing


Cond Description:
TB, DRE, MINIMUM BURNING ZONE CONDITIONS


Report Name/Date:
Lafarge Corporation, Fredonia, Kansas Plant, November 1995 Recertification of Compliance, prepared by Radian, November 1995


Report Name/Date:
Lafarge Corporation Fredonia Plant Compliance Test Certification Package, prepared by Radian, August 1992

Cond Description:
CoC, MAX PROD,MAX HW FEED,MAX COMB TEMP,MAX ESP TEMP


Report Name/Date:
PCDD/PCDF Emission Testing Report - Fredonia Kansas Cement Plant, report from Gary Elliott (Lafarge) to Frank Behan (OSW), sent January 5, 1995; Fredonia PCDD/PCDF Report, Hans Schrama, dated November 1994


Report Name/Date:
Lafarge Fredonia Kansas, Certification of Compliance Revised Operating Conditions, Radian, September 1994

Cond Description:
CoC, MAX RAW MIX FEED RATE AND ESP INLET TEMP, MIN ESP POWER


Report Name/Date:
Emission Test Report, Measurements for PCDD/PCDDFs and HCl/Cl2 from a Wet Process Cement Kiln, Lafarge Corp, Fredonia, Kansas, DEECO Inc., August 9, 1993


Cond Description:
CoC, MAXIMUM OPERATING CONDITIONS FOR PRODUCTION OF CLINKER


Cond Description:
CoC, MINIMUM COMBUSTION ZONE, DRE DEMONSTRATION


Report Name/Date:
Pilot Combustion Minimization and Public Involvement Enhancement Program (PCMPIE) Test Report, prepared by Radian, June 1996

Cond Description:
LOW CHLORINE, HIGH ESP INLET TEMPERATURE


Cond Description:
HIGH CHLORINE, LOW ESP INLET TEMPERATURE


Cond Description:
CoC, OPERATING CONDITIONS AT MINIMUM TEMPERATURE


Cond Description:
CoC, OP COND AT MIN TEMP WHILE FEEDING AIR CONVEYED CANISTERS


Report Name/Date:
Lafarge Corp Fredonia Plant Compliance Test, Certification Package, prepared by Radian, August 1992


Report Name/Date:
Lafarge Corp, Fredonia, Kansas, Certification of Compliance, Revised Operating Conditions, prepared by Radian, September 1994


Cond Description:
HIGH CHLORINE, HIGH ESP INLET TEMPERATURE


Report Name/Date:
Trial Burn Report for the Aptus Rotary Kiln Incinerator in Aragonite, Utah, Alliance Project No. 5-008-999, August 1992

Cond Description:
Trial burn, MAX LIQUID AND DIRECT BURN FEED RATES

LVM SE Rating Comments:
Carbon injection system not used, old APCS

LVM SRE Rating Comments:
Carbon injection system not used, old APCS


Cond Description:
Trial burn, to set oper limits on all constituents


Report Name/Date:
Evaluation of Polychlorinated Dibenzo-p-dioxins and Polychlorinated dibenzo-furan Formation in the Hazardous Waste Incinerator Operated by Aptus, Inc. at Aragonite, Utah, NAWC Report EM 94-31, October 1994

Cond Description:
Evaluation testing, HIGH, LOW APCD TEMP/NO SULFUR ADDITIVE


Cond Description:
Research test, HIGH, LOW APCD TEMP/SULFUR ADDITIVE


Report Name/Date:
Emission Test Report, Hazardous Waste Incinerator, Ross Incineration Services, Grafton, OHio, prpeared by International Technology Corp, JTN 332282, March 1993


Report Name/Date:
Performance Test Report, October 18-19, 2000; Performance Test Emission Results, Final Report, ENSR International, Jan 2001, Project No. 5763-003-300

Cond Description:
Low temperature, DRE, high solids, APCD detuned

Content:
PM, HCl, POHC DRE, Cr, Pb, Hg, Be (metals taken for evaluation purposes, no specific limits), D/F (also taken for evaluation purposes)

SVM SE Rating Comments:
NE - metals tested for evaluation purposes only

SVM SRE Rating Comments:
NE - metals tested for evaluation purposes only

LVM SE Rating Comments:
NE- assumed metals tested for evaluation purposes only

LVM SRE Rating Comments:
NE- assumed metals tested for evaluation purposes only


Report Name/Date:
Trial Burn Test Report, Ross Incineration Services, Inc., Grafton, Ohio, OHD # 048 415 665, log # 157-257, May 1992


Report Name/Date:
Trial Burn Test Report, Ross Incineration Services, Inc., Grafton, Ohio, Prepared by PEI Associates, PN # 8431-9-3, April 1989


Report Name/Date:
Test Report for the RCRA Trial Burn on the TWI Unit 4 Incinerator, Trade Waste Incineration, Sauget, Illinois (ILD 098642424), Prepared by MRI, Project # 9730-M02, September 18, 1992


Report Name/Date:
Stationary Source Sampling Report, Reference No. 12327, Virginia Solite Cascade, Virginia, Kiln No. 1 Stack, March 24, 1994

Cond Description:
DRE / dioxin testing, MAX CL FEED, HIGH COMB TEMP


Cond Description:
DRE / dioxin testing, MAX CL FEED, low COMB TEMP


Report Name/Date:
Stationary Source Sampling Report, Reference No. 13967, Virginia Solite, Leaksville Plant, Cascade VA, Kiln Nos. 1 and 4 Stack, May 1995


Report Name/Date:
Particulate Matter, Sulfur Dioxide, NOx, Lead, CO, and PM-10 Emission Measurements at Virginia Solite Cascade, Oldover Corp., June 25, 1991


Report Name/Date:
BIF CoC forms prepared by Calvin Gover, Dick Carnes, and James Peters


Report Name/Date:
E. I. Dupont Company Trial Burn Test Program Emission Test Results, Orange, Texas, Prepared by Alliance Technologies, Project # 5-954999, August 1990

Cond Description:
Trial burn, MEDIUM TEMP/TYPICAL OP PARAMETERS


Report Name/Date:
Source Emission Survey of Dupont SRW Incinerator Stack Trial Burn, Orange, TX, July 2000

Content:
PM, HCl/Cl2, metals, Cr6, D/Fs, VOCs/SVOCs, PSD, SO2 (No CO)

D/F SE Rating Comments:
Assumed normal because of low temp DRE condition


Cond Description:
Trial burn, MAX TEMP/MAX WASTE,CL,ASH FEED


Report Name/Date:
Final Trial Burn Report for the Fluidized Bed Incinerator, Miles, Inc., New Martinsville, WV, ENSR Document No. 4690-009-400, September 1992

Cond Description:
Trial burn, MAX LIQUID FEED AND ASH INPUT


Report Name/Date:
Investigation of PCDD/PCDF Emissions from the Fluidized Bed Incinerator with and without Carbon Injection, December 1998


Report Name/Date:
As reported in Investigation of PCDD/PCDF Emissions from the Fluidized Bed Incinerator with and without Carbon Injection, December 1998 (as reported in) possibly also same as above 1992 trial burn


Report Name/Date:
Incinerator Trial Burn Report, Glaxo Inc., RTP NC, October 1993; Entropy Stationary Source Sampling Report, Reference No. 10983, August 1993


Cond Description:
Trial burn, high temp for liq mode oper.

Hg SRE Rating Comments:
Hg not controlled, SREs set to 0, normal


Cond Description:
Trial burn, low temp for liq mode oper. Max feedrate


Cond Description:
Trial burn, high temp for solid mode oper. Max batch size


Cond Description:
Trial burn, low temp for solid mode oper. Max feedrate


Report Name/Date:
Hazardous Waste Trial Burn Performed for the Upjohn Company, Kalamazoo, MI, December 4-6, 1990, report dated March 3, 1992

Cond Description:
Trial burn, PART./METALS TESTING, HIGH SOLID FEED


Cond Description:
Trial burn, POHC TESTING, HIGH LIQUID HW FEED


Report Name/Date:
Results of the RCRA Trial Burn with VX Feed for the Liquid Incinerator at the Johnston Atoll Chemical Agent Disposal System, Jun 23, 1992, prepared by Southern Research Institute, SRI-APC-92-384-7530.11.1-I-R3


Report Name/Date:
JACADS Liquid Incinerator - Trial Burn Report, August 29, 1997

Content:
PM, HCl/HF, metals, PCDD/PCDF, VOC/SVOC (Runs 2-5)


Report Name/Date:
Results of the RCRA Trial Burn with GB Feed fo the Liquid Incinerator at the Johnston Atoll Chemical Agent Disposal System, June 17, 1991, SRI-APC-91-190-6967-006-F-R4


Report Name/Date:
Results of the Demonstration Test Burn for Thermal Destruction of Agent HD in the Johnston Atoll Chemical Agent Disposal System Liquid Incinerator, prepared by United Engineers and Constructors, Feburary, 1993


Report Name/Date:
Results of the RCRA Trial Burn and TSCA Demonstration Burn of the Deactivation Furnace System with M55 VX Rockets at the Johnston Atoll Chemical Agent Disposal System, June 23, 1992, SRI-APC-92-385-7530.5.1-I-R3


Report Name/Date:
JACADS- GB Trial Burn Report of the DFS Incinerator, July, 1998

Content:
PM, HCl/Cl2/HF, metals, PCDD/PCDF, DRE, VOC/SVOC (Runs 3-6)


Report Name/Date:
Tooele Chemical Agent Disposal Facility (TOCDF), RCRA Agents GB Trial Burn Report for the Deactivation Furnace System (DFS), Prepared by EG & G Defense Materials, Inc., April 9, 1997


Report Name/Date:
DFS GB ATB2 Report - Rev 1, July 7, 1999 (only have copy of select tables received in NODA comments, missing full report)


Report Name/Date:
Preliminary Trial Burn of the Occidental Chemical Corporation Liquid Waste Incinerator Facility, Niagara Falls, New York, Test Report, MRI Project No. 3539-M(02), February 10, 1994

Cond Description:
Preliminary trial burn, NOMINAL CONDITIONS

Cl SE Rating Comments:
NE-Preliminary test; assumed OPLs were not established

PM SE Rating Comments:
Preliminary Test-assumed OPLs were not established

LVM SE Rating Comments:
Preliminary test; OPLs were not established

LVM SRE Rating Comments:
Preliminary test; OPLs were not established


Report Name/Date:
Trial Burn Report, Occidental Chemical Corporation, Niagara Plant Liquid Waste Incinerator Burning Organic and Aqueous Wastes, January 1998

Cond Description:
Trial Burn, Maximum Combined waste and fuel oil feed, minimum temperature, max stack gas flow, max Cl feed


Report Name/Date:
Trial Burn of the Occidental Chemical Corporation Liquid Waste Incinerator Facility, Niagara Falls, New York, Test Report, MRI Project No. 3539-M(03), March 16, 1995

Cond Description:
Trial burn, LOW COMB TEMP/HIGH WASTE FEED


Cond Description:
Trial burn, HIGH COMB TEMP/HIGH WASTE FEED


Report Name/Date:
Trial Burn Report for Emission Source Test of Waste Propellant Incinerator 6A at Radford Army Ammunition Plant, Radford, Virginia, Prepared by DRE Environmental Services, June 1993


Report Name/Date:
830 Incinerator Trial Burn Report, ID # MID 000 724, Summary of Results and Program Description, Dow Chemical Company, March 1992

Cond Description:
Trial burn, NORMAL KILN TEMP, HIGH CL AND METAL FEED, metals results considered invalid shice lab failed to analyze the EPA audit sample


Cond Description:
Trial burn, LOW KILN TEMP, HIGH CL AND SOLIDS FEED


Cond Description:
Trial burn, LOW KILN TEMP,MAX ASH&CONTAINER BTU FEED


Cond Description:
Trial burn, NORMAL KILN TEMP, MAX CHLOROSILANES FEED


Cond Description:
Trial burn, METALS RE-TEST; HIGH CHLORINE

SVM SE Rating Comments:
Feedrate extrapolation used to set limit

LVM SE Rating Comments:
Feedrate extrapolation used to set limit

LVM SRE Rating Comments:
Feedrate extrapolation used to set limit


Report Name/Date:
RCRA Trial Burn Report for a Dual Purpose RCRA/TSCA Incinerator at the U.S. Department of Energy's K-25 Facility in Oak Ridge, Tennessee, August 31, 1989

Cond Description:
Trial burn, MAX WASTE, CL, ASH FEED; MINIMUM TEMP


Report Name/Date:
Final Report, Trial Burn of the TSCA Incinerator, U.S. Department of Energy, Oak Ridge East Tennessee Technology Park, Oak Ridge Tennessee, September 7, 2001, TRC Project No. 02261 - 0020 - 00000


Cond Description:
PCDD/PCDF data from 1995 testing provided to EPA by DOE


Report Name/Date:
Trial Burn Report, M&T Chemicals Inc., the Carrollton Plant, April 21, 1989


Report Name/Date:
Atochem North America, Metals Trial Burn Report Results, June 1990


Report Name/Date:
Ash Grove Cement Company, Foreman Arkansas, Waste Derived Fuel Facility, RCRA Trial Burn Report and Certification of Compliance for Kiln No. 1 - July 1992, October 1992


Cond Description:
Trial burn: Max comb temp, max metals, chlorine, raw material feedrate, 4 runs


Cond Description:
Trial burn: D/F test at max APCD temp and max CO, 3 runs


Cond Description:
CoC, LOW COMB TEMP, HIGH CL FEED, HIGH HW FEED


Report Name/Date:
Ash Grove Cement, Foreman Arkansas, Report of RCRA Trial Burn for Kiln Nos. 1 and 2, November 1994, dated June 1995

Cond Description:
CoC, HIGH COMB TEMP, HIGH CL FEED, HIGH HW FEED


Report Name/Date:
Emissions Testing of Ash Grove Cement Company, Foreman, Arkansas, Waste Derived Fuel Facility Cement Kiln No. 3, prepared for U.S. EPA OSW by EER under EPA Contract No. 68-D2-0164, Work Ass 2-07, May 19, 1995


Report Name/Date:
Ash Grove Cement, Foreman Arkansas, RCRA Trial Burn Report and Certification of Compliance for Kiln No. 3 - July 1992, dated November 1992


Cond Description:
Trial burn: Max comb temp, max metals, chlorine, raw material feedrate, max APCD temp, min ESP power


Report Name/Date:
Ash Grove Cement, Foreman Arkansas, Report of RCRA Trial Burn for Kiln No. 3, January 1995, dated June 1995

Cond Description:
CoC, MAX FEED & CHLORINE, MIN. COMB. TEMP.

PM SE Rating Comments:
Not evaluated: failed Run 2 (<0.08 gr/dscf)


Cond Description:
CoC, MAX FEED, PRODUCTION, CHLORINE, & COMB. TEMP. MIN ESP POWER


Cond Description:
LOW KILN EXIT TEMP, LOW PARTICULATE MATTER LOADING


Cond Description:
EER/EPA sponsored research testing with copper and water quench


Report Name/Date:
FMC Hazardous Waste Incinerator Trial Burn Test Report, prepared for FMC Agricultural Chemical Group, Baltimore, Maryland, prepared by Scott Environmental Services, August 1986, SET 1619-03-0886


Report Name/Date:
Baltimore Plant Hazardous Waste Trial Burn Report, Dec 27,2000

Cond Description:
Trial burn, high temperature operation, spiking of ash and metals, (Metals spiked in wastewater)

Content:
PM, HCl/Cl2, CO, HC, NOx, POHC DREs, Metals, PCDD/F


Report Name/Date:
POHC Trial Burn Stack Emission Test Series John Zink Thermal Oxidizer, Akzo Chemie, America, Morris, Illinois, Prepared by ARI Environmental, Project # 432-01, September  18-20, 1984


Report Name/Date:
Trial Burn Sampling and Analysis Results for the Mobay Incinerator, Kansas City, MO, Final Report, MRI, November 1984


Cond Description:
Trial burn, worst case, max temp, max feedrate


Report Name/Date:
EPA OSW Sponsored Evaluation Testing, November 1988


Report Name/Date:
Stationary Source Sampling Report, Reference No. 6036, Allied Fibers, Hopewell, Virginia, October 12-14, 1988


Report Name/Date:
PCDD/PCDF data only as reported in Inc reported in Inc Conf"Application of an Ultra Clean Technique for the Measurement of Trace Dioxin and Furan Levels in Source Emissions," Bruce Maisel, L. Davis, and M. Wood, 1997 Incineration Conference, May 12-16, 1997, Oakland California, pp. 355-360

Cond Description:
PCDD/PCDF data only as reported in Inc Conf


Report Name/Date:
Final Report on RCRA Trial Burn Test Results to SmithKline Chemicals from Batelle Columbus Labratories, November 12, 1984


Report Name/Date:
RCRA Trial Burn Report for HD - Mustard Ton Containers - Metals Parts Furnace at the Johnston Atoll Chemical Agent Disposal System, December 16, 1992


Report Name/Date:
JACADS Metal Parts Furnace Halogenated Waste Performance Test, March 2001

Cond Description:
Halogenated waste trial burn, no metals spiking nor DRE

Content:
PM, HCl/Cl2/HF, metals, PCDD/PCDF, VOC/SVOC, PCB, total organics, limited feed analysis


Report Name/Date:
JACADS Metal Parts Furnace 4.2-Inch Agent HD Mortar Projectiles Trial Burn Report, August 1999

Content:
PM, metals, HCl, Cl2, HF, D/F, CO, DRE, SVOC, VOC, no metals spiking


Report Name/Date:
GB Trial Burn Report, Trial Burn of the MPF Incinerator, Johnston Atoll Chemical Agent Dispoal System, Johnston Island, July 1998


Report Name/Date:
Re-certification of Compliance, Texas Industries Resource Recovery Program, May 8, 1995, prepared by Entellect


Report Name/Date:
Stationary Source Sampling Report Reference No. 11583, Virginia Solite Corporation, Cascade, Virginia, Prepared by Entropy, June 1993; COC Forms attached, dated August 23, 1993


Report Name/Date:
Stationary Source Sampling Report Reference No. 11438, Solite Corporation, Arvonia, Virginia, Prepared by Entropy, February 1993; COC Forms attached, dated January 28, 1994


Cond Description:
CoC, high temperature metals and chlorine testing


Report Name/Date:
Test Report for Trial Burns on the Prowl Incinerator at the American Cyanamid Facility, Hannibal, Missouri, Prepared by MRI, Project # 9353-L(02), August 9, 1989

Cond Description:
ORGANICS SPIKED INTO LIQUID AND AQUEOUS WASTES


Report Name/Date:
Re-Test Report for Trial Burns on the Prowl Incinerator at the American Cyanamid Facility, Hannibal, Missouri, Prepared by MRI, Project # 9353-L(02), November 6, 1989

Cond Description:
LOW CO LEVELS, AQUEOUS (FIREWATER) SPIKED WITH MCB


Cond Description:
HIGH CO LEVELS, AQUEOUS (ACTUAL PLANT WASTE) SPIKED WITH MCB


Report Name/Date:
Dioxin/Furan Emission Test Results for Incinerators Final Report, For American Cyanid Company, Prepared by MRI, Project # 4435, August 13, 1996

Cond Description:
DIOXIN/FURAN EMISSIONS TESTING - AQUEOUS/ORGANIC WASTE


Cond Description:
DIOXIN/FURAN EMISSIONS TEST - AQUEOUS/ORGANIC WASTE


Report Name/Date:
Test Report for the RCRA Trial Burn, February 2, 1998


PM SE Rating Comments:
NE - miniburn - unknown if OPLs established as result of test

PM SRE Rating Comments:
NE - miniburn - unknown if OPLs established as result of test


Report Name/Date:
Test Report for VOST Retest, October 1998


Report Name/Date:
Supplemental Low Grade Fuel Trial Burn, Kiln No. 2, Norlite Corporation, Cohoes, New York, June 1990, Prepared by APCC

SVM SE Rating Comments:
Data from source 307 represents this kiln

LVM SE Rating Comments:
Data from source 307 represents this kiln, no Be data


SVM SE Rating Comments:
Not evaluated: not burning hazardous waste during test; data in lieu kiln

LVM SE Rating Comments:
Not evaluated: not burning hazardous waste during test


Report Name/Date:
Source Emissions Survey of Ciba-Geigy Corporation, Multi Purpose Incinerator Stack, St. Gabriel, Louisiana, Prepared by METCO Environmental, File # 93-265, December 1993


Report Name/Date:
Trial Burn Report for Arkansas Eastman Company No. 2 Incinerator, Batesville, Arkansas, July 1987

Cond Description:
Trial burn, DEMONSTRATE DRE FOR AQUEOUS WASTE


Cond Description:
Trial burn, DEMONSTRATE PM REMOVAL FOR WASTES W/DISSOLVED SALTS


Cond Description:
Trial burn, DEMONSTRATE DRE AND HCL REMOVAL FOR HIGHLY CHLORINATED WASTE


Report Name/Date:
MWP-2000 Trial burn Report, for Trial Burn conducted January 7, 1992 at El Dorado Arkansas, ENSCO, Little Rock Arkansas, dated April 10, 1992


Report Name/Date:
Environmental Systems Company Fixed Base Incinerator Trial Burn Report, El Dorado, Arkansas, prepared by METCO, April 14, 1992

Cond Description:
Trial burn, SURR. SOLID TO #1,2; MAX SOLIDS TO #1; LIQ. FEED TO TOU/WFB


Cond Description:
Trial burn, SURR. SOLID TO #1,2; MAX SOLIDS TO #2; LIQ TO TOU; NG OT WFB


Cond Description:
Trial burn, NG TO #1,2; MAX LIQ TO TOU; NG TO WFB


Report Name/Date:
Rollins Environmental Services (TX) Inc. Trial Burn Program Incinerator Train I Emission Test Results, Deer Park, Texas, Prepared by Alliance Technologies Corporation, ID # - 5-919-999, September 1989


Report Name/Date:
Res(TX) Trial Burn Program Rotary Reactor / Incinerator Train II, Emission Test Results, Final Report, Prepared for Rollins Environmental, Deer Park TX, prepared by Alliance Technologies, Project No. 5-950-999, October 1989


Report Name/Date:
Hazardous Waste Incinerator No. 2, Trial Burn Report, Ciba-Geigy Corp, McIntosh, Alabama, Volume I of V, June 1994

Cond Description:
Trial burn, HIGH KILN EXIT TEMPERATURE, METALS SPIKING


Report Name/Date:
Hazardous Waste Incinerator No. 2, Trial Burn Report of Results, Ciba Specialty Chemicals Corporation, McIntosh, Alabama, July 2000

Cond Description:
Trial burn, POHC DRE, low temp, max feed and gas velocity


Cond Description:
Trial burn, worst case for metals, PM, chlorine (max temp, max feedrates)


Cond Description:
Reasonable worst case, low temp PIC risk burn


Cond Description:
Trial burn, LOW KILN EXIT TEMPERATURE, DRE


Report Name/Date:
1995 Recertification at Essroc Materials, Inc, Logansport, Indiana, APCC Project No. 95001, August 1995

Cond Description:
CoC, MAX COMB TEMP, MAX METALS/CL FEED, MAX APCD TEMP

Cl SE Rating Comments:
Data for source 300 currently represents this kiln

PM SE Rating Comments:
Data for source 300 represents current emissions

Hg SE Rating Comments:
Data from source 300 represents current emissions from this kiln

SVM SE Rating Comments:
Data from source 300 currently represents this kiln

SVM SRE Rating Comments:
Data from source 300 currently represents current performance of this kiln

LVM SE Rating Comments:
Data from source 300 represents this kiln

LVM SRE Rating Comments:
Data from source 300 represents this kiln

LVM TE Rating Comments:
Data from source 300 represents this kiln


Cond Description:
CoC, MIN COMB TEMP, MAX CL FEED, MAX PROD RATE


Report Name/Date:
Texas Eastman Company Trial Burn Program Emission Test Results, Alliance Project No. 5-986-999, April 5, 1991


Report Name/Date:
Trial Burn Report, Fluid Bed Incinerator, Jan 1999

Content:
PM, HCl/Cl2, DRE, D/Fs, V/SV PICs, CO, PSD, aldehydes/ketones


Content:
PM, HCl/Cl2, metals, Cr6, & waste feed ash/Cl/metals


Report Name/Date:
Tooele Chemical Agent Disposal Facility (TOCDF), RCRA Agent Trial Burn Report for the Liquid Incinerator System No. 1, EG&G Defense Materials, Inc., July 7, 1997


Report Name/Date:
TOCDF, Agent GB Mini-Burn Report for the Liquid Incinerator System #1, EG&G Defense Materials Inc., January 20, 1999

Cond Description:
Trial burn to set arsenic operating limits (waste with higher than average arsenic used), and gather risk burn data for other constituents


Report Name/Date:
Tooele Chemical Agent Disposal Facility (TOCDF), RCRA Agent Trial Burn Report for the Metal Parts Furnace, EG&G Defense Materials, Inc, August 15, 1997


Report Name/Date:
PCDD/PCDF data reported in "Results from the Metals Parts Furnace Performance Standard Demonstration Burn Using Ton Containers with Agent GB Heels," Timothy Booth, Michel Foster, T. Bumann, and C. McBride, 1997 Incineration Conference, Oakland CA, May 12-16, 1997, pp. 677-681


Report Name/Date:
Stationary Source Sampling Report, Reference No. 5471, PPG Industries, Circleville, OH, January 11 - 15 1988

Cond Description:
Trial Burn, Slagging Kiln With Maximum Solids Loading

SVM SRE Rating Comments:
Assumed normal for lead/no Cd emission data


Report Name/Date:
Final Trial Burn Report for the Energy Recovery Unit/March, 1998

Content:
PM, HCl/Cl2, PCDD/PCDF, DRE (PERC, MCB), SVOCs, VOCs,CO,NOx,SO2


Cond Description:
Trial Burn, High Temperature, Metals Spike (Pb,Cr,As)

Content:
PM, HCl/Cl2, metals, Cr+6, PCDD/PCDF, SVOCs, VOCs


Cond Description:
Trial Burn, Non-Slagging Kiln With Maximum Solid Loading


Report Name/Date:
Trial Burn Report for Explosive Waste Incinerator at Lake City Army Ammunition Plant, Independence, Missouri, March 1993


Report Name/Date:
3rd Trial Burn Program, Lake City Army Ammunition Plant, Explosive Waste Incinerator, Olin Corporation, Independence, Missouri, TRC Projection No. 17791, January 1996

Cond Description:
Trial burn, 5.56mm M855 SAWS feed, max metal feed

Hg SE Rating Comments:
All tests considered to be the same campaign; recent test added new mode of operation


Cond Description:
Trial burn, 20mm M56 HEI feed, max metal feed


Report Name/Date:
APE 1236 Explosive Waste Incinerator Risk Burn Report

Cl SE Rating Comments:
Assumed risk burn conducted at normal conditions

PM SE Rating Comments:
Assumed risk burn conducted at normal conditions


Report Name/Date:
Air Pollution  Emission Assessment # 42-21-0475-91, Trial Burn for Deactivation Furnace Building 97, Lake City Army Ammunition plant, Independence, Missouri, February 19- March 6, 1991


Cond Description:
Trial burn, HI SKOR 700X Propellant Feed


PM SE Rating Comments:
PM emissions exceeded current RCRA standard


Report Name/Date:
EPA Trial Burn Emission Testing of BASF Incinerator Unit # IN-701, BASF Corporation, Freeport, Texas, Prepared by NUS Corporation, Project # 4963, November 1986


Report Name/Date:
Rotary Kiln Application Trial Burn Results, RCRA Permit HW-50161-001, Dow Chemical Company, Freeport, Texas

Cond Description:
Trial burn, Avg. Temp to meet 99.99% DRE


Cond Description:
Trial burn, MAX. heat duty, MIN. INCINERATOR RES. TIME


Report Name/Date:
Rotary Kiln Supplemental Trial Burn Results, RCRA Permit HW-50161-001, December 14, 1995; Compliance Test Report, Texas Rotary Kiln, Dow Freeport TX, Sampling Date: July 11-13, 1995

SVM SE Rating Comments:
Assumed OPLs were established as result of test


Report Name/Date:
Trial Burn Report, Chemical Waste Management Incinerator Facility, Port Arthur, Texas, prepared by Radian, May 25, 1990

Cond Description:
Trial Burn, DRE On Non-Energetic And Energetic Sludge Fed To Kiln


Cond Description:
Trial Burn, Dre On  Energetic Liquid And Sludge


Report Name/Date:
Trial Burn Report, Bi-Annual Stack Test on the Hazardous Waste Incinerator System, prepared by Radian for Chemical Waste Management, Port Arthur, TX, October 19, 1994

Cond Description:
Bi-Annual Stack Test At "Normal" Operating Conditions


Report Name/Date:
Supplemental Trial Burn, Chemical Waste Management Incinerator Facility Port Arthur Texas, prepared by Radian for Chemical Waste Management, October 10, 1990

Cond Description:
Trial Burn, Min Kiln Temp (1200F), Min Heat Input


Cond Description:
Trial Burn, Min Kiln Temp (1300F), Min Heat Input


Report Name/Date:
Toxic Substances Control Act Trial Burn Report, Chemical Waste Management Incinerator Facility, Port Arthur, Texas, prepared by Radian, June 30, 1990


Report Name/Date:
2000 Bi-Annual Stack Test/Trial Burn - Chemical Waste Mgmt, Inc. Port Arthur, TX, June 2000

Cond Description:
RCRA / TSCA Biannual Trial burn, normal metal feeds

Content:
PM, HCl/Cl2, metals, DRE, PCDD/F,VOC/SVOC, HC, NOx, SO2


Report Name/Date:
Report, 1998 Bi-Annual Stack Test / Risk Assessment Test / Trial Burn,  Chemical Waste Management Inc., Port Arthur, Texas Incinerator, prepared by Radian Int., Nov 13, 1998

Cond Description:
Bi-annual testing trial burn, max temp, max metals feeds


Cond Description:
Bi-annual testing, typical operations (metals at historic feedrates)


Report Name/Date:
Bi-Annual Stack Test on the Hazardous Waste Incinerator System, Port Arthur, Texas, prepared by Radian, September 21,1992, DCN # 263-091-05-00, Prepared for, Chemical Waste Management Inc.

Cond Description:
Bi-Annual Stack Test At "Normal" Operating Condition


Cond Description:
Demonstrate Operating Conditions Outside Current Permit


Cond Description:
Demonstrate Operating Conditions Outside Permit


Cond Description:
Trial Burn, Pohc Dre On Energetic Sludge & Liquid And Aqueous Liquid Fed


Cond Description:
Trial Burn, Dre On Non-Energetic Sludge & Liquid And Energetic Solid Fed


Cond Description:
Trial Burn, DRE On Non-Energetic Solids Fed To Kiln

SVM SRE Rating Comments:
OPLs not likely set during testing, normal


Cond Description:
Trial Burn, DRE On Energetic Liquid Fed To SCC


Report Name/Date:
Test Report for the Trial Burn on the Aniline Incinerator at BASF Corp. in Geismar, LA , Final Report, December 1992.

Content:
PM, metals, DRE, NOx/CO/THC, VOC/PICs, metal feeds


Report Name/Date:
REX(TX) Stack Test Results, Incinerator Trains I/II Tri-Annual RCRA Requirements and TSCA (PCB) Testing, prepared for Rollins Environmental Services, Deer Park TX, prepared by TRC Environmental, April 1995

Cond Description:
TRAIN I: IS A RCRA AND TSCA PERMITTED INCINERATOR


Report Name/Date:
Trial Burn/ Risk Burn Report Conditions 1,2 and 4, August 1998

Cond Description:
Risk burn organics, max RR feed, low temp-Condition 1


Cond Description:
Risk burn metals, high temp, max RR feed, moderate metals spike - Condition 2


Report Name/Date:
Trial Burn/ Risk Burn Report Conditions 3I and 3II, October 1998

Cond Description:
Trial burn, min temp, max feedrate, DRE train I - Condition 3i


Cond Description:
Trial burn, min temp, max feedrate, DRE train II - Condition 3ii


Cond Description:
Trial burn, max temp, max metals spike - Condition 4


Report Name/Date:
PM, HCl, and HCl Removal Efficiency Compliance Emissions Sampling of Incinerator NCIN-1, Shell Chemical Co, NORCO, LA, December 1991, SwL Project No. 54-9112-065

Report Prepared:
Southwestern Laboratories, Environmental Analytical Services Div.

Testing Firm:
Southwestern Laboratories, Environmental Analytical Services Div.


Report Name/Date:
Source of Emissions Survey of Shell Chemical Company NCIN 1 Stack, February 1998.

Cond Description:
Trial burn, low temp, no water injection, low waste feed


Cond Description:
Trial burn, upper oper temp, max waste, max water injection


Cond Description:
Risk burn, reasonable upper bound on normal operation


Report Name/Date:
Air Emissions Compliance Sampling for Consolidated Air Permit No. 2252, NCIN-2 Incinerator and Biosolids Incinerator, Shell Chemical Co., NORCO West Site, NORCO, LA, July 1994, SwL Project No. 5354-9406-003

Report Prepared:
Huntingdon/Southwestern Lab, Air Emissions Services Division

Testing Firm:
Huntingdon/Southwestern Lab, Air Emissions Services Division


Report Name/Date:
Source of Emissions Survey of Shell Chemical Company NCIN 2 Stack, February 1998.


Report Name/Date:
Test Report for the RCRA Trial Burn on the Unit 3 Incinerator, Trade Waste Incineration, Sauget, Illinois, ILD 098642424, Prepared by MRI, Project # 4341-02, January 21, 1997

Cond Description:
Trial burn, Worst case operating conditions


Report Name/Date:
Environmental Assesment of the Texas Eastman Hazardous Waste Incinerator, February, 1985, Prepared by Acurex, Project # 6699, Purchase Order # 144-0078-B-P, Longview, Texas


Report Name/Date:
Trial Burn Report, Rotary Kiln Incinerator, Texas Eastman Division Eastman Chemical Company, Longview, Texas, January 4, 1999

Cond Description:
Trial burn, high temp metals and chlorine determination


Cond Description:
Trial burn, low temp DRE and risk burn, max ash

Content:
PM, HCl/Cl2, HF, HBr, D/F, SVOC, VOC, PAH, aldehyde/ketones, CO


Report Name/Date:
Test Report on Exhaust Emissions from VCM Incinerator CC-IN-1 (550) at the Oxymar VCM Production Facility, Gregory Texas, prepared by Cubix Corporation, Job # 2924, November, 1994


Report Name/Date:
Metals and HCl/Cl2 Source Emission Test on No. 3 Kiln Baghouse Exhaust, Giant Cement Co., Harleyville, SC, prepared by Davis and Floyd

Cl SE Rating Comments:
Data for source 200 currently represents this kiln

PM SE Rating Comments:
Data for source 200 represents this kilns current emissions

Hg SE Rating Comments:
Data from source 200 represents current emissions from this kiln

SVM SE Rating Comments:
Data from source 200 currently represents this kiln

LVM SE Rating Comments:
Data from source 200 currently represents this kiln


Report Name/Date:
Metals and HCl/Cl2 Source Emission Test on No. 2 Kiln Baghouse Exhaust, Giant Cement Co., Harleyville, SC, prepared by Davis and Floyd

Cond Description:
State of South Carolina emissions testing requirements


Report Name/Date:
Stationary Source Sampling Report, Reference No. 10181A, Giant Cement, Harleyville, SC, June 5, 1991

Cond Description:
State of South Carolina emissions testing requirements, pre-BIF


Report Name/Date:
Test Report for the RCRA Trial Burn on the Du Pont Experimental Station Hazardous Waste Incinerator, Wilmington, Delaware, Prepared by MRI, Projecct # 6495-M(04), August 13, 1992


Report Name/Date:
Stationary Source Sampling Report, Reference No. 6181, Eli Lilly and Company, Clinton, Indiana, C-10 Incinerator Stack, February 21-24, 1989


Report Name/Date:
Ciba Giegy St. Gabriel, Louisiana Trial Burn on Hazardous Waste Liquid Incinerator, # LAD053783445 July 15, 1988


SVM SRE Rating Comments:
Assumed normal for Cd, No Pb emission data


Report Name/Date:
Dupont Central Scubbed Incinerator(CSI) Trial Burn Report, DCN 89-274-015-02, Prepared by Radian Corp., La Porte, Texas, January 5, 1989


Cond Description:
Trial burn, max temp, max feedrate, worst oper cond


Report Name/Date:
Stationary Source Sampling Report, Reference No. 10786, Burroughs Wellcome Company, Greenville, NC, NcGill No 2 Incinerator, November 18-20, 1992

Cond Description:
Triak burn, minimum temperature, maximum feed rate


Cond Description:
Trial burn, minimum temperature, maximum feed rate


Cond Description:
Trial burn, minimum temperature, maximum feed rate.


Report Name/Date:
Stationary Source Sampling Report, prepared for Nepera, Incorporated, prepared by ENTROPY Environmentalists, Emissions Testing, Incinerator Stack R238 VENT, February 1993, Harriman, New York, Reference # 11546

SVM SRE Rating Comments:
SVM not controlled, SRE set to 0, normal


Cl SRE Rating Comments:
Chlorine not controlled, no APCD, SRE set to 0


Report Name/Date:
Stationary Source Sampling Report, prepared for Nepera, Incorporated, prepared by ENTROPY Environmentalists, Emissions Testing, Incinerator Stack R238 VENT, September 1992, Harriman, New York, Reference # 11179


Report Name/Date:
Incinerator Trial Burn Test Results Olin Corporation (now Lyondell), Lake Charles Louisiana, Prepared by Radian Corporation, January 27, 1989

Cond Description:
Trial burn, MAX CHLORINE,T-101, AND STACK FLOW RATE


Report Name/Date:
Trial Burn Report Olin - Lake Charles Plant

Cond Description:
Minimum operating temperature w/TDI residue


Cond Description:
Trial burn, MIN COMB TEMP/MAX TDI RESIDUE


Cond Description:
Trial burn, MAX TDI RESIDUE & MAX T-101 WASTE LIQUID


Report Name/Date:
Recertification of Compliance for Tennessee Eastman Division Boilers 23 and 24; dated September 1, 1998

Cl SE Rating Comments:
R1 not reported; sample train leak check failure


Content:
Total organics, CO, volatile organics, PCDD/PCDFs, SV organics, aldehydes/ketones, PM size distribution; metals, chlorine in feedstreams


Report Name/Date:
Certification of Compliance, Boiler 4 Celanese Ltd/October 1998

Report Prepared:
TRC Environmental Corporation, Houston, TX

Content:
Stack PM; Feed analysis of organics and ash.


Report Name/Date:
Compliance Test Report, Boiler 4, Celanese Ltd/October 1998


Report Name/Date:
Trial Burn/Risk Bum Report, Boiler 4, Celanese Ltd/November 1998

Content:
VOC, Total Organics, SVOCs, PCDDs/PCDFs, Particle Size Distribution, aldehydes, and ketones.


Report Name/Date:
Recertification of Compliance (ReCOC) for Merichem; report provided begins at section 2.0 (no date)

Testing Firm:
Focus Environmental, Inc (Ramcon Environmental Corporation)

Cond Description:
CoC; min combustion temp; Wet Scrubber not used


Cond Description:
CoC; max waste feed (spiked ash, chlorine, metals), Wet Scrubber not used

Content:
PM, HCl/Cl2, metals, CO;  ash, metals, chlorine in feeds

Cl SE Rating Comments:
Chlorine spiked for chlorine feed limit for setting Tier III metals limits


Report Name/Date:
Stationary Source Sampling Report, prepared for ICI Americas Inc., prepared by Entropy Environmentalists, Hazordous Waste Incineration Testing, LV-3 Incinerator Stack, June 19-21, 1990, Bayonne, New Jersey, Reference # 6743


Report Name/Date:
Stationary Source Sampling Report, Reference No. 11112, ICI Americas, Inc., Bayonne, New Jersey, LV-3 Incinerator, August 26-27, 1992


Report Name/Date:
Stationary Source Sampling Report, prepared for Eli Lilly and Company, prepared by Entropy Environmentalists, Hazordous Waste Incineration Testing, Brule Incinerator Stack, November 18, 1987, Mayaguez, Puerto Rico, Reference # 5720


Report Name/Date:
Compliance Recertification for Boiler A Pursuant to the BIF Regulations, August 1998


Report Name/Date:
Compliance Recertification for BIF Units R-1and R-3 Pursuant to the BIF Regulations, March 1999


Report Name/Date:
BIF Compliance Certification and Results of the Trial Burn for BIF Units U-304 and U-305; August 1992


Report Name/Date:
Revised Certification of Compliance Test Report for Boilers 70K, 30K, and 28K, August 21, 1996

Testing Firm:
Spectrum Compliance Resources, Inc., METCO Environmental, B3 Systems, Inc


Report Name/Date:
Trial Burn Report for Boiler 70K, February 3, 2000

Testing Firm:
METCO Environmental (Stack sampling), B3 Systems, Inc (Feed spiking)

Content:
PM, CO, HCl/Cl2, PCDD/PCDF emissions; metals/chlorine in feedstreams


Report Name/Date:
Mini Burn Test Report for Boiler 70K, July 10, 2000


Report Name/Date:
Trial Burn Retest Report for Boiler 70K, July 10, 2000

Cond Description:
Trial burn retest, min comb cham temp, min prod rate


Report Name/Date:
Trial Burn Report for Boiler 30K, February 3, 2000

Cond Description:
Trial burn, high feed rate, max steam prod


Cond Description:
Trial burn, min comb temp, min steam prod rate


Report Name/Date:
Trial Burn Retest Report for Boiler 30K, July 10, 2000

Cond Description:
Trial burn retest, min comb temp, min steam prod rate


Report Name/Date:
1998 BIF Compliance Recertification, December 1998


Cond Description:
CoC, acryloid coatings waste blend, max ash feed (ash spiking)


Report Name/Date:
Source Emission Survey of Rohm & Haas Texas, Inc. HT-1 Thermal Oxidizer Stack (EPN HT-3), BIF Certification Test, No. 99-196A, July 1999

Content:
PM, CO emissions; metals, chlorine, and ash in feeds


Report Name/Date:
Certification of Compliance Boiler No. 100, Nov. 19, 1999

Cond Description:
CoC; max waste feed rate, ash spiking (TiO2)

Content:
PM, CO in stack gas; metals, chlorine and ash in feedstreams


Report Name/Date:
Source Emissions Survey for Schenectady International B-503, File # 96-99; no date reported

Content:
PM, CO; metals and chlorine in feedstreams


Report Name/Date:
Sterling Chemicals, Inc. BIF Recertification of Compliance Test Waste Oxidation Boiler A; Sept/97

Content:
PM, CO; metals, chlorine, and ash in feeds


Report Name/Date:
Trial Burn Report, Boiler 31, Union Carbide Corporation, June 1998

Cond Description:
Risk burn -- normal operating conditions


Content:
PM only (no DRE), CO, ash (titanium oxide) spiked


Report Name/Date:
Revised Certification of Compliance, January 29, 1999

Content:
PM, CO emissions; metals, ash, Cl feed analysis


Report Name/Date:
Source Emissions Survey of DSM Copolymer Boiler Number 3 Risk Burn, April and May 1997; also Risk Burn Summary - Final Report, DSM Copolymer, January 1998


Report Name/Date:
Recertification of Compliance, DSM Copolymer Plant, July 22, 1996

Content:
PM, CO, HCl/Cl2; metals, chlorine in feedstreams


Report Name/Date:
Source Emissions Survey of E.I. Dupont De Nemours & Company, Inc. Sabine River Works

Cond Description:
CoC; max comb temp, haz waste feed and steam prod rate


Report Name/Date:
Source Emissions Survey of E.I. Dupont De Nemours & Company, Inc. Sabine River Works , Risk Burn, 98-183D, July 1998


Report Name/Date:
Source Emissions Survey of E.I. Dupont De Nemours & Company, Inc. Sabine River Works, DRE Burn, Dec. 1998, No. 98-305A


Report Name/Date:
Source Emissions Survey of E.I. Dupont De Nemours & Company, Inc. Sabine River Works, DRE Burn, 98-183C, July 1998


Cond Description:
CoC; max temp, haz waste feed and prod rate


PM SRE Rating Comments:
PM not controlled, SRE set to 0; data in lieu


Report Name/Date:
Source Emissions Survey for DuPont ADN South Boiler Stack, DRE Burn, 98-305B, 1998


Report Name/Date:
Source Emissions Survey for DuPont ADN South Boiler Stack, Risk Burn, 98-305, 1998


Report Name/Date:
RCRA Boiler and Industrial Furnace Recertification of Compliance Report Boiler No. 4, November 1999

Content:
PM, CO, HCl/Cl2 in stack gas; metals, ash, Cl in feed


Report Name/Date:
Revised Recertification of Compliance of BIF Boilers H530A and H530B at GE Plastics, February 1998


Report Name/Date:
Revised Recertification of Compliance of BIF Boilers H530A and H530B, GE Plastics Mt. Vernon Facility, February 1998


Report Name/Date:
Recertification of Compliance Boilers H530A and H530B, GE Plastics Mt. Vernon Facility, September 2001

Content:
PM and CO emissions; waste feed ash, chlorine, metals


Report Name/Date:
Boiler and Industrial Furnace Compliance Test Report and Certification of Compliance - General Electric Plastics Plant, August 1998

Content:
PM, CO emissions; ash, metals, and chlorine anaysis of feedstreams


Report Name/Date:
Test Report for Recertification of Compliance of BIF Boilers B-101, B-102, B-103, B-104, & B-105, July 1995, Test Report II for ReCoC, Nov. 1995

Report Prepared:
The Goodyear Tire and Rubber Co. and Radian Corp.

Cond Description:
CoC; max waste feedrate and steam prod rate


Cond Description:
CoC; less aggressive max waste feed and max prod rate


Cond Description:
CoC; similar to C1 but higher prod rate, lower chamber temp


Report Name/Date:
Trial Burn Report for BIF Boilers B101-B105, July 1999


Cond Description:
Trial burn, max waste feed, max steam prod


Report Name/Date:
Risk Burn Report for BIF Boilers B101-B105, Revision 1, July 1999

Cond Description:
Risk burn, worst case cond, max waste feed and max prod


Report Name/Date:
Trial Burn Report Addendum U-3 Boiler, December 1997

Cond Description:
Trial burn; max comb temp, max prod rate, max benzene


Cond Description:
Trial burn; min comb temp and min prod rate, max moisture/methanol feed


Report Name/Date:
Certification of Compliance for Boilers A/B & C; May 23, 1997


Report Name/Date:
Certification of Compliance Forms, November 1998

Cond Description:
CoC; max feeds for T-303 bottoms and IPOH

Content:
PM, Cl2, CO emissions; metals and chlorine in feedstreams


Report Name/Date:
BIF Recerification of Compliance Test Report - Boilers 1 and 2; dated August 20, 1997

Content:
PM, CO, HCl/Cl2, Cr emissions; metals, ash, Cl feed analysis


Report Name/Date:
BIF Recertification of Compliance Test Report - Boilers 1 and 2; dated August 20, 1997

Content:
PM, CO, HCl/Cl2, Cr emissions; metals/ash/Cl feed analysis


Report Name/Date:
Recertification of Compliance Test Report for Boiler No. 1, 8/27/98; Compliance Emission Test Report - Boiler No. 1, 8/21/98.

Content:
PM, CO, Cr/Cr+6 emissions; ash, Cl, and metals feeds


Testing Firm:
METCO Environmental (Source Emissions Survey of Borden Chem., April 1998, File No. 98-118)


Cond Description:
CoC; Lower scrubber recirculation rate, low scrubber pH


Report Name/Date:
R-30 Trial Burn and Risk Report, November 1998

Cond Description:
Trial burn, max waste feed and prod rate, max comb temp, min APCS


Cond Description:
Trial burn; DRE, min comb temp, max comb gas flow


Content:
Stack gas metals, PCDD/F, other organics, PSD


Report Name/Date:
B-824 Trial Burn Report and Risk Burn Report, March 13, 1998


Cond Description:
Trial burn, DRE, min comb temp and max stack gas flow


Cond Description:
Risk burn, max liq waste feed rate, normal comb temp


Report Name/Date:
Test Report for Trial Burns on the Thimet/ Counter Incinerators at the American Cyanamid Facility in Hannibal, Missouri, Prepared by MRI, Project No. 9353-L(02), August 9, 1989

Cond Description:
Trial burn, ORGANICS SPIKED INTO SOLID/LIQUID WASTE


Report Name/Date:
Retest Trial Burn on the Thimet/Counter (Trane/Brule) Incinerators at the American Cyanamid Facility in Hannibal, Missouri, MRI Project No. 9353-L-03, September 20, 1989

Cond Description:
Trial burn retest, ORGANICS SPIKED INTO SOLID/LIQUID WASTE


Report Name/Date:
Dioxin/Furan Emission Test Results for Incinerators C, B, and D, MRI Project No. 4435, August 13, 1996


Report Name/Date:
Report of RCRA Trial Burn Results for a Fluidized Bed Incinerator, Prepared for Amoco Oil Company, Whiting, Indiana, Prepared by Scott Environmental Technology Inc. June 1989

Cond Description:
Trial burn, HIGH WASTE FEED/HIGH COMB TEMP


Cond Description:
Trial burn, LOW WASTE FEED/LOW COMB TEMP


Report Name/Date:
Dow Chemical Trial Burn Report for Rotary Kiln, Prepared by Dow Chemical, Plaquemine, Louisiana, February 10, 1998


Report Name/Date:
Metals Trial Burn, Tennessee Eastman's No. 1 Rotary Kiln, Tennessee Eastman Company, August 30, 1991


Report Name/Date:
Mini-Trial Burn Report for Rotary Kiln Incinerator No. 1, March 2002

Cond Description:
Trial burn, max metals, ash, chlorine, min temp


Cond Description:
Trial burn, organics testing, min combustion temp, SCC not operated


Report Name/Date:
Trial Burn Report for Tennessee Eastman Company B-248 Incineration Facility, Tennessee Eastman Company, Eastman Road, P.O. Box 511, Kingsport TN 37662, Submitted to Tennessee Division of Solid Waste Management, April 1989

Cond Description:
Trial burn, max feedrates, all permit conditions set during testing


Cond Description:
General trash feed, no permit limits set


Report Name/Date:
Metals Trial Burn, Tennessee Eastman's No. 1 Liquid Chemical Destructor, Tennessee Eastman Company, August 30, 1991


Report Name/Date:
Performance Test Report for Liquid Chemical Destructor. August 2000


Cond Description:
Trial burn, max operating conditions, permit limit setting test cond


Report Name/Date:
Source Emission Survey, Fina Oil, Laporte, TX, File No. 98-203, December 1998

Content:
PM, HCl/Cl2, CO; metals, chlorine, and ash in feeds


Report Name/Date:
Risk Assessment Trial Burn Report, Dec. 29, 1997


Report Prepared:
Westvaco Chemical Division, Deridder, LA facility

Content:
Non D/F organics (no PM, chlorine, metals, volatiles, semi-vol, TOC)


Report Name/Date:
Recertification of Compliance Test Report


Report Name/Date:
Certification of Compliance Boiler 3 Institute Plant, August 1998

Content:
PM, CO, HCl/Cl2, Tier lll metals (As, Cr)

LVM SE Rating Comments:
As, Be measurement only in stack gas; data in lieu


Report Name/Date:
Source Emissions Survey of Exxon Plastics C Boiler Stack, Baton Rouge, LA, July 1997, File 97-103


Report Name/Date:
Trial Burn Test Report, Pennwalt Corporation, Isotron 142b Incinerator, Thorofare, New Jersey, June 1989, Volume 1 of 2, prepared by PEI Associates, Inc.


Report Name/Date:
GE PCB Trial Burn Report, General Electric Company Silicone Products Division Rotary Kiln Incinerator, Waterford, New York, Prepared by GE, March 18, 1994


Report Name/Date:
Trial Burn Testing Results at Rotary Kiln Incinerator under maximum heat duty, v.1, Oct 1991

Cond Description:
Trial burn, maximum heat duty, maximum flow, minimum temperature, maximum ash, chlorine and metals feed.

Content:
PM, HCl/Cl2, CO, HC, Metals, Hexavalent Chromium, SVOC, VOC, D/F


Report Name/Date:
Report on Supplemental Trial Burn Testing, March 1996

Cond Description:
Supplemental trial burn to verify certain aspects of performance compliance.

Content:
PM, HCl/Cl2, CO, HC, Metals, Hexavalent Chromium


Report Name/Date:
Risk Burn Report, No. 7 Boiler, March 1998

Content:
Stack testing: D/F, PM, PM PSD, HCl/Cl2, CO, VOC/SVOC;  No stack testing for metals (has Tier IA limits and metals feeds) or DRE


Report Name/Date:
Source Emission Survey BASF Corp. NOEL Boiler Stack (EPN 5-5-08) Trial Burn, no date listed (Risk Burn also included)

Cond Description:
Trial burn; Wastewater and HDO Heavies Waste Feeds

Content:
Monochlorobenzene DRE; PM/CO/Chlorine Stack Emissions; Ash/Metals/Chlorine Feed Analysis


Content:
PM/CO/Chlorine Stack Emissions; Ash/Metals/Chlorine Feed Analysis


Content:
Metals, aldehydes/ketones, dioxins/furans, SVOCs, total organics, VOCs as stack emissions


Report Name/Date:
BASF Corp. DRE Trial Burn Report, March 1998, Rev. 2

Content:
DRE, PM, HCl/Cl2, CO; metals, chlorine, ash feeds


Report Name/Date:
Risk Burn Report Amines Boiler, Number 6 Utility Boiler, March 1998

Cond Description:
Risk burn, worst case op cond (max temp, feedrates, prod rates)

Content:
PM, chlorine, D/F, organics (metals in feedstream only)


Cond Description:
Risk burn; worst case (max temp., feedrates, production rates)


Report Name/Date:
Periodic Recertification of Compliance Boiler No. 4 Monsanto Company Port Plastics Plant, December 1994

Cond Description:
CoC; max feed Bldg. 30 spent monomer and resimene distillate


Cond Description:
CoC; max feed Bldg. 9 spent monomer and resimene distillate


Report Name/Date:
Compliance Recertification for Bayer's Boiler No. 4 Pursuant to the BIF Regulations; November 1997 Doc No 4690-047-400


Report Name/Date:
FTB-400 Trial Burn and Risk Burn Report, August 11 and 12, 1998

Cond Description:
Trial burn, max prod rate, min APCS, thermal capacity, max waste feed rate


Report Name/Date:
B-902 Trial Burn and Risk Burn Report, October 9 and 12, 1998

Cond Description:
Trial burn, max waste feed rate, max comb gas velocity


Cond Description:
Risk burn, slightly above normal operating conditions

SVM SRE Rating Comments:
SVM not controlled; SRE set to 0, normal


Report Name/Date:
F-2AB Trial Burn Report and Risk Burn Report, September 2, 1998

Cond Description:
Trial burn, min comb temp and max velocity


Cond Description:
Risk burn, slightly above normal liq waste feed rate, normal comb temp


Report Name/Date:
F-2A/B Certificate of Compliance Burn, April 1997


Report Name/Date:
F-210 Trial Burn and Risk Burn Report, July 13 and 15, 1998

Cond Description:
Trial burn, max waste feed rate, max ash and Cr

SVM SE Rating Comments:
No Cd stack gas measurements, spiked Pb but not Tier III


Cond Description:
Trial burn, DRE min comb temp, max stack gas flow rate


Cond Description:
Risk burn, above normal feed of liq waste, normal comb temp


Report Name/Date:
F-11 Trial Burn and Risk Burn Reports, September 25, 1998

Cond Description:
Trial burn, max waste feed rate and comb temp, min APCS


Cond Description:
Trial burn, DRE, min comb temp and max comb gas velocity


Cond Description:
Risk burn, above normal liq waste feed rate, normal comb temp


Report Name/Date:
F-820AB Trial Burn Report, September 2, 1998

Cond Description:
Trial burn, max feed rate, max comb temp and max comb gas flow, min APCS


Report Name/Date:
F-820AB Second Trial Burn Report and Risk Burn Report, December 9, 1998

Cond Description:
Trial burn, high capacity, max prod, max feed

Content:
PM, HCl/Cl2, Cr+6, CO (testing only on F 820B)


Cond Description:
Risk burn, slightly above normal conditions


Report Name/Date:
Trail Burn Report For The Dow Chemical Company Manufacturing Services Halogen Acid Furnace; Volume 1 of 5, January 2000


Content:
PM, HCl/Cl2, metals, Cr+6, organics, PCDD/F

Cl TE Rating Comments:
Keep as normal? even out normal, still has very very high chlorine, likely very accurate, feed


Report Name/Date:
Source Emissions Survey of DuPont Dow Elastomers, HCl Recovery Unit Stack Risk Burn, April 1997, File Number 97-17A


Report Name/Date:
Source Emissions Survey of DuPont Dow Elastomers, HCl Recovery Unit Stack Permit Burn, April 1997, File Number 97-17

Content:
DRE, PM, Cr (HCl/Cl2 testing performed, but results later considered invalid due to analytical difficulties)


Report Name/Date:
Source Emissions Survey of DuPont Dow Elastomers Halogen Acid Furnace Stack, September 1997, File Number 97-240A


Report Name/Date:
Trial Burn Report for Texas Eastman Hydrochloric Acid Recovery Unit, October 22, 1998

Cond Description:
Trial burn, worst case for organics destruction

Content:
PM, CO, HCl/Cl2, POHC DRE, PCDD/PCDF, other organics


Report Name/Date:
BIF Certification of Compliance for Eastman Chemical Co, Texas Eastman Division, September, 1996

Cl SE Rating Comments:
NE; only considering most recent compliance test campaign

PM SE Rating Comments:
NE; only considering most recent compliance test campaign


Report Name/Date:
Georgia Gulf, Industrial Furnace DRE Trial Burn Report Volume I, June 1998, EMI Proj No. 98-8045


Report Name/Date:
Compliance Test Report, Georgia Gulf, April 25-26 and July 10, 1995

Report Prepared:
Environmental Science and Engineering, Inc.


Report Name/Date:
Confirmation of Trial Burn Test Report for Georgia Gulf Industrial Acid Furnace, March 12-14, 1990

Cond Description:
Trial burn -- Heavy liquid and wet/dry vent streams

Content:
PM, HCl/Cl2, DRE, CO, complete waste feed analysis


Report Name/Date:
Biennial RCRA Trial Burn and BIF Certification of Compliance Test Report Regeneration Unit Number 4, January 1997

Cond Description:
Trial burn/CoC; max haz waste feed rate, Cl, metal, max comb temp

Content:
PM, CO, HCl/Cl2, Tier lll metals, PCDD/F, DRE for POHC (CCl4)


Cond Description:
Trial burn/CoC; max POHC spiking, min comb temp and O2

Content:
PM, CO, HCl/Cl2, PCDD/F , DRE for POHCs (MCB, CCl4, TCB)


Report Name/Date:
BIF Revised Certification of Compliance for Hazardous Waste Boiler Operation, April 1996

Cond Description:
CoC, max feed, flow, and prod rate, max temp


Cond Description:
CoC, max feed and flowrate, min pressure drop


Report Name/Date:
Source Emissions Survey of First Chemical Corp. Hazardous Waste Incinerator Stack, Trial Burn Report, MSD 033417031, Pascagoula, Mississippi July 1991, Metco File Number 90-199


Report Name/Date:
Trial Burn Report of First Chemical Corporation, Noxidizer Incinerator Stack, Pascagoula, Mississippi, Volume I Prepared by METCO Environmental, April 1, 1995


Report Name/Date:
Velsicol Trial Burn Report, Metals Emissions, Velsicol Chemical Corp, Memphis, Tennessee, DCN 90-274-018-04, prepared by Radian, February 20, 1990

SVM SRE Rating Comments:
assumed normal for Cd, no lead emission data


Report Name/Date:
Certification of Compliance Boilers #15 and #25, August 1998

SVM SE Rating Comments:
Pb Tier I, not in stack gas, Cd only in stack gas


Report Name/Date:
Certification of Compliance Boilers 4 and 5, July 1999; Boiler 5 Trial Burn Report, Volume I of VII, August 1999

Cond Description:
CoC/trial burn, max liquid waste feed, max prod rate

Content:
PM, HCl, Cl2, and Cr+6, DRE (toluene and chlorobenzene)


Content:
PCDD/F, other organics, particle size distribution


Report Name/Date:
Revised Certification of Compliance, November 1996


SVM SRE Rating Comments:
SVM not controlled; SRE set to 0; normal


Content:
CO, D/F, PCB, PAH, VOC/SVOC, Aldehydes/ketones


Report Name/Date:
Revised Certification of Compliance, January 1999


# LVM SRE

LVM SRE Comments:
Data from source 403 currently represents this kilns emissions


LVM SRE Comments:
Assumed metals not spiked and operating limits not established


LVM SRE Comments:
Not evaluated: pre-BIF Rule data; SRE based on As and Cr only


LVM SRE Comments:
Not evaluated: not burning hazardous waste


LVM SRE Comments:
Data from source 473 currently represents this kiln


LVM SRE Comments:
Carbon injection system not used, old APCS


LVM SRE Comments:
NE- assumed metals tested for evaluation purposes only


LVM SRE Comments:
Preliminary test; OPLs were not established


LVM SRE Comments:
Feedrate extrapolation used to set limit


LVM SRE Comments:
Not evaluated: data from source 300 represents this kiln


# Old Condition Description

Report Name/Date:
Supplemental Fuel Trial Burn, Coplay Cement, Logansport Indiana, May 1987, prepared by TRC, TRC project No. 3919-E71, September 1987


Cl Rating Comments:
Not evaluated: pre-BIF Rule data; HCl emissions only

LVM Rating Comments:
Not evaluated: pre-BIF Rule data; no Be emissions data


Cond Description:
Trial burn, high waste feedrate, min temp oper


Cond Description:
Trial burn, high wet solids feed rate, low temp oper


Cond Description:
Trial burn, high viscous liquid feed rate, low temp oper


Cond Description:
Trial burn, high nonviscous liquid feed rate, max comb temp


Report Name/Date:
Clean Harbors Technology Corp 1995 Annual Performance Test Report, January 15, 1996


Report Name/Date:
Clean Harbors Technology Corporation 1996 Annual Performance Test Report, December 3, 1996


Report Name/Date:
Annual Performance Test Program on Fluidized Bed Incinerator, Prepared by TRC Environmental Corporation, Report No. EM 97-14, December 3, 1997


Report Name/Date:
Compliance Test Report for Clean Harbors Env. Services, IN., Kimball, Nebraska Facility, Test Dates: November 16-19, 1999


Report Name/Date:
Source Emissions Testing Report for Clean Harbors Environmental Services, Kimball, NE Incinerator Facility, Comprehensive Performance Test, November 2000, Project No. CLH0387


Report Name/Date:
Recertification of Compliance Test Report for Boiler No. 2, 12/4/97; Compliance Emission Test Report - Boiler No. 2, 11/5/97

Content:
PM, CO, Cr and Cr+6 emissions; ash, Cl, and metals feeds


Report Name/Date:
Certification of Compliance for Boilers A/B & C; 5/23/97

Content:
PM, CO emissions; ash, chlorides, metals in feeds


Content:
PM, CO emissions; ash/chlorides/metals in feeds


Report Name/Date:
Recertification of Compliance for F-65630 Hot Oil Heater and Utility Boilers; 8/07/97


Report Name/Date:
Recertification of Compliance for F-65630 Hot Oil Heater and Utility Boilers; 8/31/98

Content:
PM, CO emissions only; feed analysis for ash, metals, chlorides


Report Name/Date:
Recertification of Compliance for F-57180 Hot Oil Heater; 9/06/96

Content:
PM, CO emissions, feed analysis for ash, metals, chlorides

PM Rating Comments:
NE; only consider most recent compliance test campaign


Report Name/Date:
Test Report for Recertification of Compliance for F-57180 Hot Oil Heater; 3/09/99


Report Name/Date:
Re-Certification of Compliance for F-65630 Hot Oil Heater and Utility Boilers;8/6/97


Report Name/Date:
Re-Certification of Compliance for F-65630 Hot Oil Heater and Utility Boilers; 8/31/98


Report Name/Date:
Test Report on Re-Certification of Compliance of Boiler No. 1 & Annual Performance Test on 2 CEMS installed on Blrs 1 & 2; 10/95

Content:
PM, HCl/Cl2, CO emissions; metals, ash, chlorides in feeds


Report Name/Date:
BIF Certification of Compliance Units H-K2-001 and H-K2-002, Dec. 1996


Report Name/Date:
Re-Certification of Compliance of Boiler - PO/MTBE Steam Generators; 11/97


Report Name/Date:
Recertification of Compliance Test Report - Huntsman Polymers C Boiler; Jan, 1999

Content:
PM, HCl/Cl2, CO emissions; metals, chlorine, and ash in feeds


Report Name/Date:
Compliance Test Report - BIF Recertification of Compliance - Beaumont, Texas Facility; Aug, 1998

Cond Description:
CoC; max feedrate, production rate, comb temp

Content:
PM, HCl/Cl2, metals, CO emissions; metals, chlorine, and ash in feeds (As, Be, Cd, Cr, ash spiked)


Report Name/Date:
Boiler Trial Burn Report - Eastman Chemicals Company, Arkansas Eastman Div.; dated October 6, 1999


Cond Description:
Trial burn, risk burn; max conditions for feedrates and other parameters

Content:
PM, CO/HC, HCl/Cl2, metals, PCDD/PCDF, SVOCs/PAHs, DRE; POHCs, ash, metals, Cl feed analysis

D/F Rating Comments:
Many factors affect D/F emissions for coal fired boilers; Conducted under max desired ESP oper temp

SVM Rating Comments:
Spiked Pb; made Pb and Cd stack gas; Tier I for Pb and Cd


Report Name/Date:
Biennial RCRA Trial Burn Test Report - Rhone-Poulenc, Inc., Regeneration Unit No. 2; dated December 1996

Cond Description:
Trial burn; max cond for feedrates, comb temperature


Cond Description:
Trial burn; max cond for feedrates; min comb temp and O2

Content:
PM, CO, HCl/Cl2, DRE; POHC, ash, Cl feed analysis


Report Name/Date:
Recertification of Compliance for Tennessee Eastman Division Boilers 18, 19, and 20; dated March 24, 1998

Content:
PM, metals, CO, HCl/Cl2; feed analysis for metals, ash, HCl/Cl2


Report Name/Date:
Recertification of Compliance for Tennessee Eastman Division Boilers 21 and 22; dated August 11, 1997

Content:
PM, metals, CO, HCl/Cl2; feed analysis for metals, ash, chlorides

Cl Rating Comments:
no reported chlorine spiking, but Tier III

PM Rating Comments:
Run 2 had outlier PM level of > 0.10; not used


Report Name/Date:
Recertification of Compliance (ReCOC) for Celanese Boilers 9 & 10; No date, Report provided begins at Section 2.0

Content:
PM, CO, Cr emissions; feed analysis for metals, ash, chlorides


Content:
PM, Cr, CO emissions; feeds for metals, ash, chlorides


Report Name/Date:
Periodic Recertification of Compliance Hot Oil Heater No. 1 Down Draft Duct (EPN-12) Georgia Gulf Corporation, July 1998

Content:
PM, CO;  feedstream analysis metals, ash, chlorine


Report Name/Date:
Source Emissions Survey BASF Corp. WOD K541 Stack Risk Burn; No report date

Content:
Stack PM, HCl, Cl2, D/F, SVOC, Total Organics, CO, and O2;
Metals, D/F, Chlorine, VOCs characterization of waste feed steams.


Report Name/Date:
Source Emission Survey - Aristech Chemical Corp. - F-8 Boiler Stack (EPN 84); File No. 95-165B, September 1995

Content:
PM, HCl/Cl2, & CO emissions; metals, ash, & chlorine in waste feedstreams

Cl Rating Comments:
NE; only consider most recent compliance test campaign

Hg Rating Comments:
NE; only considering most recent compliance test campaign

LVM Rating Comments:
NE; only considering most recent compliance test campaign

SVM Rating Comments:
NE; only considering most recent compliance test campaign


Cond Description:
CoC; max feed waste liq 2EH and combined PA residue


Report Name/Date:
Source Emission Survey - Aristech Chemical Corp. - F-8 Boiler Stack (EPN 84); 2000

Content:
HCl/Cl2, CO, D/Fs, VOC/SVOC, total organics, aldehydes/ketones, & particle size emissions; metals, ash, & chlorine in waste feedstreams


Report Name/Date:
Boiler 16 Recertificatioin of Compliance, Oct 1996

Cond Description:
Compliance Test. Maximum combustion temperature condition

Content:
Feed analysis: 10 BIF metals (not chromium only), chlorides, and ash. 
PM, CO, and hexavalent and total Cr emissions.


Cond Description:
Risk burn at max. liquid waste feedrates + min. natural gas flowrate

Content:
VOC, Total Organics, SVOCs, PCDDs/PCDFs, Particle Size Distribution, aldehides, and ketones.


Report Name/Date:
Ticona, Boiler 16 baseline test for Chrome, May 2002


Report Name/Date:
Nebraska Boiler Trial  Burn Report, December 1997

Cond Description:
Trial burn, max waste feed, min comb temp

Content:
PM, HCl/Cl2, DRE for acetophenone, cumene, phenol


Content:
CO, DRE for acetophenone, cumene, phenol


Cond Description:
Trial burn, Cr+6 burn, max waste, ash, Cl, comb temp

PM Rating Comments:
PM Emissions exceeded current RCRA standard


Report Name/Date:
Trial Burn Report, Vinyl II Plant, Industrial Boiler F-410, Dow Chem., Louisiana Operations, Volume 1: Report, December 19, 1997

Cond Description:
Trial burn; not used for permit setting (max oper cond)


PM Rating Comments:
Used to establish operating limits?  Assume N


Cond Description:
Trial burn; max waste feedrates (Cr, ash spiking)


Report Name/Date:
Trial Burn Report, Glycol I Plant, Industrial Boiler R-4, Dow Chem., Louisiana Operations, Volume 1: Report, December 12, 1997

Cond Description:
Trial burn; min comb chamber temperature


Cond Description:
Trial burn; max waste feedrates (Cr, ash spiking), steam prod rate, min L/G


Report Name/Date:
Trial Burn Report, Chlorinated Methanes, Industrial Boiler R-750, Dow Chem., Louisiana Operations, Volume 1: Report, December 22, 1997


Cond Description:
Trial burn; min combustion chamber temperature


Report Name/Date:
Stationary Source Sampling Report Ref No. 6582A, Vulcan Materials Co Chem Div, T-11 Stack, February 19-26, 1990

Cond Description:
Trial burn -- max hex feed to burner No. 1 only


Cond Description:
Trial burn -- max D-40 groundwater phase feed to burner No. 2 only


Cond Description:
Trial burn -- similar to cond 1 but at lower feedrate


Cond Description:
Trial burn -- operation with both feeds and both burners


Report Name/Date:
Results of the Feb. 1999 Compliance Certification Testing of Energy Recovery Boiler No. 1, March 3, 1999

Content:
PM, CO in stack gas (metals, chlorine in feedstreams)


Cond Description:
CoC; max firing rate, high Btu, high ash


Report Name/Date:
Recertification of Compliance for the COEN Waste Fuel Boiler, November 6, 1998

Content:
CO in stack gas; metals/chlorine/ash in feeds


Report Name/Date:
1999 Revised BIF Compliance Certification, September 1999


Report Name/Date:
Certification of Compliance, Giant Cement Co., Boiler and Industrial Furnace Regulations, August 21, 1992; Source Test Report BIF Compliance Program, Giant Resource Recovery Company, Harleyville, SC, August 13, 1992, TRC Project No. 12667-E13

Cond Description:
CoC, MAX HW FEED, SPIKED METAL, SPIKED CHLORINE


Report Name/Date:
Giant Cement Company, BIF Recertification of Compliance, Cement Kin Nos. 2, 3, 4, and 5, November 1998

Cond Description:
CoC, Max operating mode waste feed, temp, prod rate

Content:
CO, HC, HCl/Cl2, metals (no Hg stack gas), PM


Report Name/Date:
Source Emission Test on Hazardous Waste Fuels No. 4 Kiln Baghouse Exhaust Giant Cement Company, Harleyville, South Carolina, May 1989, Davis and Floyd Job No. 6781.01


Report Name/Date:
Stationary Source Sampling Report, Reference No. 10181F, Giant Cement, Harleyville, South Carolina, Unit No. 4 Baghouse Outlet, July 9 adn 10, 1991


Report Name/Date:
Giant Cement Company Boiler and Industrial Furnace Compliance Recertification Report, prepared by Roy F. Weston, WO #06633-033-001, August 1995

Cond Description:
CoC, MAX HW FIRING, MAX TIER III METALS SPIKING, MAX SLURRY FEED


Report Name/Date:
Source Emssions Survey of E.I. Du Pont De Nemours & Company, Inc. Boiler Number 7 Stack, May 1999


Report Name/Date:
Source Emission Survey of E.I. Du Pont De Nemours & Company, Inc. Boiler 3 and 4 Stack, June 1995


Report Name/Date:
Dupont DRE Burn, Boiler No. 3 Stack, Victoria, TX, Feb. 1999


Report Name/Date:
Dupont Risk Burn, Boiler No. 3 Stack, Victoria, TX, Feb. 1999


Report Name/Date:
Dupont DRE Burn, Boiler No. 1 Stack, Victoria, TX, Feb. 1999


Report Name/Date:
Dupont Risk Burn, Boiler No. 1 Stack, Victoria, TX, Feb. 1999


Report Name/Date:
FTB-401 Trial Burn Report and Risk Report, May 26, 1998

Cond Description:
Trial burn, max prod rate, min APCS, max waste feed rate


Cond Description:
Trial burn, DRE, min comb temp, max stack gas flow rate


Content:
PCDD/F, stack gas metals, PSD, other organics


Report Name/Date:
FTB-603 Trial Burn Report and Risk Burn Report, June 30, 1998

Cond Description:
Trial burn, min comb temp, max stack gas flow rate


Report Name/Date:
FTB-603 Certificate of Compliance Burn, January 1997

Cond Description:
COC burn, max waste feed and production rate, max comb temp, min APCS


Report Name/Date:
Stationary Source Sampling Report, Reference No. 10000, Giant Cement, Harleyville, SC, Kiln No. 5 Dust Collector Outlet, January 30, 1991

Cond Description:
DRE TEST, also PM, metals, HCl; pre BIF rule


Report Name/Date:
Particulate Emission Evaluation No. 5 Kiln Exhaust Duct, Giant Cement Co, Harleyville, SC, Davis and Floyd, June 1989


Cond Description:
Trial burn, max waste feed, max op temp and prod rate, min APCS dP

Content:
PM, HCl/Cl2, Cr+6 (run 3 reported as run 5), CO (report only run 1, 2, and 5)


Cond Description:
Trial burn, min comb temp and max comb gas flow.


Report Name/Date:
Risk Rurn Report for Dow Facility ID No. F-2820, June 16, 2000

Cond Description:
Risk burn, normal operating cond of liq feed and comb temp


Report Name/Date:
Trial Burn Report for Boiler 53, July 2000

Cond Description:
Trial burn, max comb Temp, max steam prod rate, max feedrate, soot blow


Report Name/Date:
Trial Burn Report for Incinerator Unit 1 and 2 and Number 3 HAF Unit, October 2001


Report Name/Date:
Risk Burn Report for Incinerator Unit 1 and 2 and Number 3 HAF Unit, October 2001

Cond Description:
Risk burn, normal op cond, PCB containing material


Report Name/Date:
BIF Certification of Compliance Report, Holnam Artesia, Mississippi, prepared by SciTech, August 19, 1993


Report Name/Date:
Trial Burn and Recertification of Compliance Test Report, Sept 2000

Cond Description:
CoC: Max comb temp, max metal and chlorine feed rate, max prod rate, min ESP power

Content:
PM, HCl, metals (Cl2 not measured by accident)

LVM Rating Comments:
Run 3 not used in cond avg since ESP went off-line

SVM Rating Comments:
Run 3 not used in cond avg since ESP went off line


Cond Description:
CoC: Min comb temp. max feed rate, max ESP temp


Report Name/Date:
Annual Stack Test Report, Holnam Artesia, Mississippi; Stack Sampling Report, Holnam Inc., Artesia Mississippi, July 1994

Cond Description:
State of MS testing, ANNUAL STACK SAMPLING WITH SF6 SPIKE

Cl Rating Comments:
HCl measurement only, chlorine gas not measured


Report Name/Date:
BIF Certification of Compliance Report, Holnam, Artesia MS, August 19, 1993


Report Name/Date:
Annual Stack Test Report, Holnam Artesia, Mississippi; Stack Sampling Report, Holnam Inc., Artesia Mississippi

Cond Description:
State of Mississippi required annual testing, DRE TEST USING SF6

LVM Rating Comments:
Not evaluated: No arsenic emissions data


Report Name/Date:
Recertification of Compliance Test Report, Holnam Artesia MS, August 16, 1996

Cond Description:
CoC, MAX COMB ZONE TEMP, MAX METALS/CHLORINE FEED RATES


Report Name/Date:
Trial Burn and Recertification of Compliance Report, prepared for Holnam Clarksville Missouri, prepared by Schreiber, Grana, and Yonley, September 10, 1996

Cond Description:
CoC, DRE, MIN COMB ZONE TEMP, MAX HWDF FEED RATE


Cond Description:
CoC, MAX COMB ZONE TEMP, MAX SLURRY/METALS FEED, MIN ESP POWER


Report Name/Date:
Particulate Matter Emissions Testing and Continuous Emission Rate Monitoring System Certification, Holnam, Clarksville, Missouri, Fugro Midwest Report 0895-2230, November 6, 1995

Cond Description:
PM EMISSIONS TESTING AND CEM CERTIFICATION


Report Name/Date:
Trial Burn and Certification of Compliance Test Report, Holnam, Safety Kleen, Clarksville, Missouri, Prepared by Gossman Consulting, July 1992

Testing Firm:
Team Environmental, Air Compliance Technologies


Cond Description:
BASELINE, no hazardous waste firing, MAX COMB TEMP

D/F Rating Comments:
Not evaluated: not burning hazardous waste


Report Name/Date:
Engineering Evaluation Test Report, Testing During Four Test Conditions for Dioxin/Furan Emissions, HCl, SO2, and Kiln Dust from Kiln Discharge Stack and Dust Collector, DEECO Report No. 94-1124A and B, July 18, 1994


Report Name/Date:
Engineering Evaluation Test Report, Testing During Four Test Conditions for Dioxin/Furan Emissions, HCl, SO2, and Kiln Dust from Kiln Discharge Stack and Dust Collector, DEECO Report No. 94-1124B, July 18, 1994


Cond Description:
CoC, MAX GAS FLOW RATE, MAX CHLORINE FEED, MAX APCD TEMP


Report Name/Date:
Trial Burn and Certification of Compliance Test Report, Holnam, Holly Hill, SC, August, 1992

Report Prepared:
Gossman Consulting and Team Environmental


Report Name/Date:
Trial Burn and Recertification of Compliance Test Report, Kiln No. 1, July 31, 2000

Cond Description:
Max comb temp, max metals, max chlorine, max prod rate

Content:
CO, HC, HCl/Cl2, metals, PM; arsenic, lead and nickel were spiked


Cond Description:
Max APCD temp, max CO, max feed, min comb temp


Report Name/Date:
Recertification of Compliance Test Report, Kiln No. 1, Holnam Holly Hill, SC, September 15, 1995

Report Prepared:
Safety Kleen, DEECO, B3 Systems, Gossman Consulting

Cond Description:
ReCoC, HIGH COMB TEMP, HIGH METALS FEED, HIGH CHLORINE


Report Name/Date:
Memo from Charles Kellet to H. Rigo, "Holnam Holly Hill Kiln 1 Normal Data," August 17, 1995


Report Name/Date:
Air Emissions Survey Emission Test Results for Kiln No. 1 and Kiln No. 2, Holnam Holly Hill South Carolina Facility, May 15-18, 1995, DEECO Report No. 080995-1190


Report Name/Date:
Trial Burn and Recertification of Compliance Test Report, Kiln No. 2, April 14, 2000

Cond Description:
Max comb temp, max metals, max chlorine, max prod rate, max waste


Cond Description:
Max APCD temp, max CO, min DRE, min comb temp


Report Name/Date:
Recertification of Compliance Test Report, Kiln No. 2, Holnam Holly Hill, SC, August 8, 1995

Cond Description:
CoC, MAX  COMB TEMPS AND MAX METALS/CHLORINE FEED RATES


Cond Description:
CoC, DEMONSTRATE POHC DRE WITH MIN COMB TEMP AND MAX CO


Cond Description:
NORMAL WASTE DERIVED FUEL FIRING, LOW APCD TEMPERATURE


Cond Description:
BASELINE, NO WASTE DERIVED FUEL, NORMAL APCD INLET TEMP

PM Rating Comments:
Not evaluated: not burning hazardous waste


Report Name/Date:
BIF Compliance Certification, Cement Kiln Number One, Keystone Cement, Bath PA, August 1992,  Amendments submitted January 1993

Cond Description:
CoC, MAX PROD, MAX TIER III SPIKE, MAX SLURRY FEED


Report Name/Date:
BIF Recertification of Compliance, Number 1 Kiln, Keystone Cement Company, Bath, Pennsylvania, November 6, 1998

Cond Description:
CoC; max metals, chlorine, waste, slurry, min ESP power


Report Name/Date:
RCRA Trial Burn Test Report, Keystone Cement Company, Kilns No. 1 and No. 2, Bath, PA, Test Dates: 7-10 December 1999, April 2000

Cond Description:
Trial burn; Low temp POHC DRE, PCDD/PCDF


Report Name/Date:
BIF Recertification of Compliance, Cement Kiln No. 1, W. O. No. 02329.030.001, October 4, 2000


Cond Description:
CoC, MAX PROD, >25% TIER III SPIKE, MAX SLURRY FEED


Report Name/Date:
Keystone Cement Company, Bath, Pennsylvania, Source Emissions Compliance Test Report, Test Dates October 28 - November 1, 1996, January 1997, Work Order No. 0239-019-001


Report Name/Date:
BIF Compliance Certification, Cement Kiln Number Two, Keystone Cement, Bath PA, August 1992,  Amendments submitted January 1993


Report Name/Date:
BIF Recertification of Compliance, Number 2 Kiln, Keystone Cement Company, Bath, Pennsylvania, November 6, 1998


Content:
POHC DRE, PM, HCl/Cl2, HC, metals (no spiking)


Report Name/Date:
Stationary Source Sampling Report, Reference No. 10816, LWD Inc., Calvert City, KY, Unit No. 3, January 1993


Report Name/Date:
Stationary Source Sampling Report, Reference No. 12563, LWD, Calvert City, KY, Unit No. 3, January 1994


Report Name/Date:
Stationary Source Sampling Report, Reference # 11658, LWD, Inc., Hazardous Waste Incineration Testing, Unit No. 1, Calvert City, Kentucky, Prepared by Entropy, March 1993


Report Name/Date:
Stationary Source Sampling Report, Reference # 11606, LWD, Inc., Hazardous Waste Incineration Testing, Unit No. 2, Calvert City, Kentucky, Prepared by Entropy, March 1993


Report Name/Date:
RES(TX) Trial Burn Program Incinerator Train II Emission Test Results, Rollins Environmental Services, Deer Park, Texas, Prepared by Alliance Technologies, Project # 5-888-999, August 1998


Report Name/Date:
April 1994 Quarterly Test Emission Results for Lead and Particulate Matter, Waste Technologies Industries, E. Liverpool, Ohio, Prepared by ENSR Consulting and Engineering, Project # 7136-014-400, January 1995

Cond Description:
QUARTERLY EMISSION TEST FOR PB AND PM, CARBON INJECTION


Report Name/Date:
Quarterly Test Emission Results for Lead and Particulate Matter, Waste Technologies Industries, E. Liverpool, Ohio, Prepared by ENSR Consulting and Engineering, Project # 7136-015-400, March 1995


Report Name/Date:
1995 Annual Performance Test Emission Results, Waste Technologies Industries, E. Liverpool, Ohio, Prepared by ENSR Consulting and Engineering, Project # 7136-017-400, November 1995

Cond Description:
ANNUAL PERFORMANCE TEST, NORM WASTE FEED, CARBON INJECTION


Report Name/Date:
Quarterly Test Emission Results, Waste Technologies Industries, E. Liverpool, Ohio, Prepared by ENSR Consulting and Engineering, August 1994

Cond Description:
QUARTERLY COMPLIANCE, NORMAL CONDITIONS, CARBON  INJECTION


Report Name/Date:
Quarterly Test Emission Results, Waste Technologies Industries, E. Liverpool, Ohio, Prepared by ENSR Consulting and Engineering, December 1994

Cond Description:
QUARTERLY COMPLIANCE, NORMAL CONDITIONS, CARBON INJECTION


Report Name/Date:
Mercury Removal Efficiency Stack Testing Report, WTI Facility, East Liverpool, Ohio, December 2, 1993

Cond Description:
HG STACK TESTING W/ENHANCED CARBON INJECTION SYSTEM


Report Name/Date:
Final Trial Burn Report for the Rotary Kiln Incinerator, Waste Technologies Industries, East Liverpool, Ohio, Prepared by ENSR, Document Number 7136-001-800, May 1993

Cond Description:
MAX FEED METALS,CL2,SCC TEMP,KILN AQEOUS, NO CARBON INJ

Cl Rating Comments:
NE - system was later modified to add carbon inj

LVM Rating Comments:
NE - carbon injection system not used, old APCS


Report Name/Date:
1997 Annual Performance Test Emission Results


Report Name/Date:
1998 Annual Performance Test Emission Results


Report Name/Date:
1999 Annual Performance Test Emission Results


Report Name/Date:
CY 2000 Annual Performance Test Emission Results


Cond Description:
MAX FEED SLUDGE,SCC AQ.LIQ, NO CARBON INJECTION


Cond Description:
MAX FEED SOLIDS, MIN SCC TEMP., NO CARBON INJECTION


Report Name/Date:
Preliminary Testing Results for the Enhanced Carbon Injection System, July 30, 1993


Report Name/Date:
Demonstration of Carbon Injection Testing System, Provided by Region 5 EPA, February 1994


Report Name/Date:
Final Trial Burn Report for Condition 2, Waste Technologies Industries, East Liverpool, Ohio, Prepared by ENSR, Document Number 7136-071-400, April 1994


Report Name/Date:
April 1994 Quarterly Test Emission Results for PCDDs/PCDFs and Particulate Matter, Waste Technologies Industries, E. Liverpool, Ohio, Prepared by ENSR Consulting and Engineering, Project # 7136-009-400, May 1994


Report Name/Date:
Quarterly Test Emission Results for Lead and Particulate Matter, Waste Technologies Industries, E. Liverpool, Ohio, Prepared by ENSR Consulting and Engineering, Project # 7136-009-400, June 1994

Cond Description:
QUARTERLY EMISSION TEST FOR PM AND PB, CARBON INJECTION


Report Name/Date:
Quarterly Test Emission Results for Lead and Particulate Matter, Waste Technologies Industries, E. Liverpool, Ohio, Prepared by ENSR Consulting and Engineering, Project # 7136-012-400, September 1994


Report Name/Date:
Ash Grove Foreman Arkansas, RCRA Trial Burn Report and Certification of Compliance for Kiln No. 2, May 1992

Cond Description:
CoC, APCD TEMP > 450, MAX HW FEED, MAX PROD


Report Name/Date:
RCRA Cement Kiln Test Burn Report Kiln 3, April 1998

Cl Rating Comments:
Source 403 currently represents this kiln for metals/chlorine

PM Rating Comments:
Not evaluated: failed Run 1 (> 0.08 gr/dscf)


Cond Description:
D/F test at max APCD temp and max CO, APCD worst case


LVM Rating Comments:
Data from source 403 currently represents this kilns emissions

SVM Rating Comments:
Data from source 403 represents current emissions from this kiln for metals


Report Name/Date:
Ash Grove Foreman Arkansas, Report on Destruction and Removal Efficiency Determined at Minimum Combustion Chamber Temperature, Kiln No 2, submitted July 1993


Report Name/Date:
Data contained in letter from Steven Bales (Ash Grove) to Warren Owens (REI), dated November 18, 1993

Cond Description:
TO STUDY THE FORMATION OF DIOXINS/FURANS


Report Name/Date:
Source Emission Survey of Ash Grove Foreman Cement, Kiln No 2 North and Sorth Stacks, Foreman Arkansas, October 1988, METCO File Number 88-170


Report Name/Date:
Trial Burn Report, Acrylonitrile Boiler Solutia Chocolate Bayou Plant

Testing Firm:
ENSR of Acton, Mass. & Maxim Corp. of Houston TX

Cond Description:
Trial burn; low temp "worst-case" organic destruction

Content:
DRE for HCN; PM, HCl/Cl2, CO, PCDD/PCDF, PICs emissions; metals, ash, chlorine, HCN in feedstreams


Cond Description:
Trial burn; max waste feed, max prod rate

Content:
DRE for HCN; PM, HCl/Cl2, CO, metals, PCDD/PCDF, PICs emissions; metals, ash, chlorine, HCN in feedstreams


Content:
DRE for HCN; CO emissions; metals, ash, chlorine, HCN in feedstreams


Cond Description:
TB, One kiln operating, max metals feed, Worst case for spiked metals (As, Be, Cr), max temp


Cond Description:
TB, Two kilns operating, worst case for PM and HCl, min temp, no spiking


Report Name/Date:
Trial Burn Report for Incinerator Unit 1 and 2, October 2001


Cond Description:
Trial burn, higher temp for DRE and metals


Report Name/Date:
Risk Burn Report for Incinerator Unit 1 and 2, October 2001

Cond Description:
Risk burn, normal op cond, non-PCB containing material


Report Name/Date:
Trial Burn Report for Dow Chemical U.S.A. Louisiana Division Solvents Incinerator


Report Name/Date:
RCRA Compliance Test Results - Final Report, October 1993

Cond Description:
Trial burn, mixed agent VX/munitions feed

Hg Rating Comments:
Tests considered to be the same campaign; recent test added new mode of operation

PM Rating Comments:
Tests assumed to be same campaign; 93 test added new mode of operation


Report Name/Date:
RCRA Compliance Test Results - Final Report, April 1992

Cond Description:
Trial burn, mixed agent HD/munitions feed


Report Name/Date:
Results of the Chromium Emissions Report, May 1993


Report Name/Date:
RCRA Compliance Test Results for the Ton Container Heel Tests on the Metals Parts Furnace with Agent VX, Chemical Agent Munitions Disposal System (CAMDS), Tooele, Utah, Final Report, December 1994.

Report Prepared:
Science Applications International Corporation and TRC

Content:
PM, HCl/Cl2, metals, DRE, PCDD/F,VOC/SVOC (Runs 2, 4, 5)

PM Rating Comments:
Tests assumed to be same campaign; 95 test added new mode of operation


Report Name/Date:
Test Burn Report - Metals Parts Furnace Performance Standard Demonstration Burn Using Ton Containers with GB Heels

Content:
PM, HCl/Cl2, metals, DRE, PCDD/F,VOC/SVOC (Runs 4-6)


Cond Description:
Baseline - one run w/nat gas only without agent GB

Content:
PM, HCl/Cl2, metals, DRE, PCDD/F,VOC/SVOC


Report Name/Date:
Tooele Chemical Agent Disposal Facility (TOCDF), RCRA Agent Trial Burn Report for the Liquid Incinerator System #2, Revision 1, June 19, 1998

LVM Rating Comments:
Assumed metals not spiked and operating limits not established


Report Name/Date:
LIC Metals Demonstration Test Report, September 28, 2001

PM Rating Comments:
Tests assumed to be same campaign; 00 test added new mode of operation


Cond Description:
Worst case mini-burn to demo compliance with HWC MACT stnds

PM Rating Comments:
NE - unclear if mini-burn was used to establish operating limits


Report Name/Date:
Cytec Industries, Willow Island, West Virginia, Preliminary Compliance Determination for the Fluidized Bed Incinerator Pursuant to HWC MACT Regulations, ENSR, February 29, 2000, Project No. 0270-047-400

Cond Description:
Normal wastes, APCD operation, low comb temp


Cond Description:
Normal wastes, APCD operation, high comb temp


Report Name/Date:
Cytec Industries, Willow Island, West Virginia, Phase II, Preliminary Compliance Determination for the Fluidized Bed Incinerator Pursuant to HWC MACT Regulations, ENSR, September 7, 2000, Project No. 0270-047-900


Report Name/Date:
TEAD-N Incinerator Trial Burn Report, 6 December 1993, Air Pollution Emission Assessment No. 42-21-M665-93, RCRA Trial Burn for Deactivation Furnace, Tooele, Utah, 9-31 Autust 1993, Prepared by the U.S. Army Environmental Hygiene Agency


Cond Description:
Trial burn, 0.5 caliber M17 tracer/ Cr powder. Max oper cond.


LVM Rating Comments:
Assumed no spiking and that risk burn reflected normal ops even though emissions were higher than previous compliance test

PM Rating Comments:
Both 00 and 01 tests assumed to be same campaign; 00 test added new mode of operation


Report Name/Date:
Results of the February 25, 1986, Performance Evaluation Test on the Incinerator Scrubber at the Waste Research and Reclamation Plant in Eau Claire, Wisconsin, March 7, 1986


Report Name/Date:
Results of the July 1-3, 1986, Performance Tests on the Hazardous Waste Solvent Incinerator at the WR&R Plant in Eau Claire, Wisconsin, August 18, 1986

SVM Rating Comments:
NE - failed PM test, negative SVM SRE?, no Cd emission data


SVM Rating Comments:
NE - failed PM test, no Cd emission data


Report Name/Date:
Results of the July 24, 1986, Diagnostic Test on the Incinerator Scrubber at the WR&R Plant in Eau Claire, Wisconsin, July 31, 1986, Report Number 6-2250


Report Name/Date:
Results of the February 19, 1987, Particulate and Carbon Monoxide Emission Compliance Test on the Hazardous Waste Incinerator Wet Scrubber Stack at the WR&R Plant in Eau Claire, Wisconsin, February 23, 1987, Report Number 7-2336

SVM Rating Comments:
NE - no Cd emission data, negative SVM SRE?


Report Name/Date:
B.I.F. Certification of Compliance, C.O.C. Report & Attachments, Stack Test Report and Appendix, Submitted August 20, 1992

Testing Firm:
Air Pollution Characterization and Control, Ltd.

PM Rating Comments:
Not evaluated: failed run 1 (> 0.08 gr/dscf)


Report Name/Date:
RCRA Trial Burn for the Burning of Waste-Derived Fuels for Energy Recovery at Essroc Cement Corp., Logansport, Indiana, APCC Project 98062, March 1999

Report Prepared:
Air Pollution Characterization and Control, LTD

Cond Description:
CoC; Min temp, max CO, POHC DRE, min ESP power

Content:
PM, HCl/Cl2, CO, HC, D/F, SVOC, VOC, TOE


Cond Description:
CoC; Max operating temp, max temp, feedrates


Content:
PM/PSD, D/F, organics (SVOC, VOC), HCl/Cl2, CO, HC


Report Name/Date:
Particulate Emissions, ESP Collection Efficiency, and Dioxin/Furan (PCDD/PCDF) Emission Testing at Essroc Materials Inc., Logansport, Indiana, prepared by Air Pollution Characterization and Control, Ltd., September 1993, APCC Project No. 93023

Report Prepared:
Air Pollution Characterization and Control, Ltd.


Report Name/Date:
Test Report for Trial Burn, Vol. 1, February 1996

Cond Description:
Trial burn, max pressure wave, max feedrate


Cond Description:
Trial burn, max clorine feed, max heat content


Report Name/Date:
Trial Burn for Explosive Waste Incinerator, July 1995

Report Prepared:
U.S. Army Center for Health Promotion and Preventive Medicine

SVM Rating Comments:
NE - Did not pass RCRA limits for Pb, Cd


Report Name/Date:
Trial Burn Retest for Explosive Waste Incinerator, January 1996

PM Rating Comments:
Tests assumed to be same campaign; more recent test added new mode of operation


Report Name/Date:
Compliance Evaluation, Liquid Waste Incinerator, Catalyst Resources, Inc., Elyria, Ohio, Jan 18, 1984

Cond Description:
Compliance evaluation with skim tank material


Report Name/Date:
MHI Emission Test Results, February 1995


Cond Description:
Trial burn, max feedrate, max #3 hearth temp


Report Name/Date:
Trial Burn Test Report for the Eastman Kodak B-95 Multiple Hearth Incinerator, March 2002

Cond Description:
Trial Burn, min secondary comb chamber (SCC) operating temp

Content:
PM, HCl/Cl2, CO, HC, VOC/SVOC, POHC DRE, D/F


Cond Description:
Trial Burn, max waste feed, max SCC operating temp


Report Name/Date:
Trial Burn Report, M&T Chemicals Inc., the Carrollton Plant, April 21, 1989


Report Name/Date:
Atochem North America, Metals Trial Burn Report Results, June 1990


Report Name/Date:
Ash Grove Cement Company, Foreman Arkansas, Waste Derived Fuel Facility, RCRA Trial Burn Report and Certification of Compliance for Kiln No. 1 - July 1992, October 1992


Report Name/Date:
RCRA Cement Kiln Test Burn Report Kiln 1 and 2, April 1998

Cond Description:
Trial burn: Max comb temp, max metals, chlorine, raw material feedrate, 4 runs


Cond Description:
Trial burn: D/F test at max APCD temp and max CO, 3 runs


Cond Description:
CoC, LOW COMB TEMP, HIGH CL FEED, HIGH HW FEED


Report Name/Date:
Ash Grove Cement, Foreman Arkansas, Report of RCRA Trial Burn for Kiln Nos. 1 and 2, November 1994, dated June 1995

Cond Description:
CoC, HIGH COMB TEMP, HIGH CL FEED, HIGH HW FEED


Report Name/Date:
Emissions Testing of Ash Grove Cement Company, Foreman, Arkansas, Waste Derived Fuel Facility Cement Kiln No. 3, prepared for U.S. EPA OSW by EER under EPA Contract No. 68-D2-0164, Work Ass 2-07, May 19, 1995


Report Name/Date:
Third and Fourth Mini Burn Report. October 1995

Cond Description:
Mini-burn, max feedrate, max temp at 1685 °F


Cond Description:
Mini-burn, max feedrate, max temp at 1615 °F


Cond Description:
Mini-burn, max feedrate, max temp at 1600 °F


Cond Description:
Mini-burn, max feedrate, max temp at 1505 °F


Cond Description:
Mini-burn, max feedrate, max #3 hearth temp


Report Name/Date:
Final Trial Burn Report for Caloric 1 Incinerator. November 1998


Report Name/Date:
Final Trial Burn Report for Caloric 2 Incinerator. November 1998


Report Name/Date:
Trial Burn Report for No.2 Fixed Box Incinerator, Vol-1, July 9, 1992

Report Prepared:
Industrial and Environmental Analysts(IEA), Inc

Cond Description:
Trial burn, maximum heat duty, maximum ash and chlorine feed

Content:
PM, HCl/Cl2, CO, HC, Metals, Hexavalent Chromium, SVOC, VOC


Cond Description:
Trial burn, maximum heat duty, reduced ash and chlorine feed


Report Name/Date:
Stationary Source Sampling Report, Reference No. 12521, Merck Sharp and Dohme Quimica, Barceloneta, Puerto Rico, April 1996

Cond Description:
Trial burn, min temp, solid and liquid waste


Cond Description:
Trial burn, max temp, solid and liquid waste


Report Name/Date:
Annual Stack Emission Test Report, December 2000


Cond Description:
Trial burn, max feedrate and max comb temp


Cond Description:
Trial burn, min comb temp (data considered invalid due to VOST analyses after holding time allowance.  Testing rerun in Dec. 1999).


Report Name/Date:
Risk Burn (do not have complete report, all we have is PCDD/PCDF results table)


Report Name/Date:
VA-5 Incinerator Trial Burn/Risk Burn Report, February 2000


Report Name/Date:
RCRA Trial Burn Test Report, January 1999


Cl Rating Comments:
Run 1 is high outlier and not included in cond avg


Report Name/Date:
Trial Burn Report, Oxy Vinyls, LP Houston Chemical Complex, Deer Park - VCM Site Organic Chloride Incinerators HCIN2 & HCIN3 Haz Waste Permit App., May 1999


Cond Description:
Trial burn - worst-case PM/HCl/metals; As/Cr spiked

Content:
PM, HCl/Cl2, metals (As/Cr), Cr6, CO & waste feed ash/Cl/metals


Cond Description:
Risk burn (Slightly higher than annual median waste feedrate)

Content:
Metals, D/Fs, CO, Cr6, PSD, V/SV PICs, feed metals/ash/Cl


Report Name/Date:
PIC Risk Burn Report, Lone Star Industries, February, 2001


Report Name/Date:
Final Recertification of Compliance Test Report, Lone Star Industries, January 2001


Report Name/Date:
Lafarge Corp Paulding Plant Compliance Test, Certification Package, prepared by Radian, August 1992

Cond Description:
CoC, MAX COMB TEMP, MIN ESP POWER, MAX PROD


Report Name/Date:
Lafarge Corp Paulding, Ohio, August 1998 Trial Burn Report, August 1998

Cond Description:
CoC; high temperature, max metals, prod rate, waste feed


Content:
PM/PSD, metals, D/F, organics, HCl/Cl2, CO


Report Name/Date:
Lafarge Corp Paulding Ohio, Certification of Compliance, Alternative Carbon Monoxide Standard, prepared by Radian, September 1994


Report Name/Date:
Lafarge Corp Paulding Ohio Plant, Recertification of Compliance, prepared by Radian, submitted August 1995


Report Name/Date:
PCDD/PCDF Testing Data from Lafarge Paulding, Radian Testing during Summer 1994, CRKC Docket No. 733, contained in letter from CKRC to EPA OSW


Report Name/Date:
Filterable, Condensible, and Total Particulate, Dioxins and Furans, Multi-Metals, Hydrogen Chloroide, and Chlorine Emissions Evaluation Conducted March 12-16, 2001, Report Date July 2001

Report Prepared:
Air Control Techniques, P.C.,  En-Tellect Environmental Services Inc.

D/F Rating Comments:
No temperature profile information available


Report Name/Date:
Certification of Compliance and Comprehensive Performance Test Report. Ash Grove Cement Co., Chanute, Kansas, Notification of Compliance and Comp Perf Test Report, June 12, 2002


Cond Description:
Comp Perf Test, raw mill off, PCDD/PCDF retest


Report Name/Date:
Air Pollution Emission Assessment No. 42-EK-1463-97 -- Trial Burn and Health Risk Assessment Emissions Test for APE 1236 DFS - McAlester Army Ammunition Plant, McAlester, OK, February 12 - March 14, 1997


Cond Description:
M43A1/M1911 Mixed munitions, metal powder


Report Name/Date:
No. 5133E/5307B, Eli Lilly and Company, Clinton, Indiana, RCRA Hazardous Waste Incineration Testing, Condition 6 and Normal Waste Feed, TO3 Incinerator Stack, June 19 and September 30, 1986


Cond Description:
Trial burn, normal operations; permit test cond OPL for PM


Report Name/Date:
Certification of Compliance Stack Emission Test Program at Lonestar Industries, Inc., Cape Girardeau, Missouri, April and June 1992, BIF CoC Test Report, Revised January 1993, APCC Project 92007

Report Prepared:
Air Pollution Characterization and Control

Testing Firm:
Air Pollution Characterization and Control

Cl Rating Comments:
Not evaluated: not burning hazardous waste

Hg Rating Comments:
Not evaluated: not burning hazardous waste

LVM Rating Comments:
Not evaluated: not burning hazardous waste

SVM Rating Comments:
Not evaluated: not burning hazardous waste


Cond Description:
CoC, HIGH COMB TEMP, IN-LINE RAW MILL OFF


Report Name/Date:
Report on Diagnostic Testing, Conducted at Lone Star Industries Stack, Cape Giradrdeau, CAE Project No. 6764, Octoeber 21, 1993

Cond Description:
COAL AND HWF COMBINATION, IN-LINE RAW MILL ON


Report Name/Date:
Emission Measurements for the Burning of Tires at Lone Star Industries, Cape Girardeau, Misssouri, APCC Project 92003, September 1992

Testing Firm:
Air Pollution Characterization and Control, LTD


Report Name/Date:
Trial Burn Report, Lone Star Industries, Cape Girardeau, MO, prepared by Gossman Consulting, December 1995; Report on Trial Burn Testing, conducted at Lone Star Industries, Main Stack, Cape Girardeau, Missouri, CAE Project No. 7576, December 27, 1995

Cond Description:
Trial burn, HIGH COMB TEMP, IN-LINE RAW MILL OFF


Report Name/Date:
Final Trial Burn Report for Light Weight Aggregate Kiln Process Utilizing Low Grade Fuels, Norlite Corporation, Cohoes, New York, Prepared by ENSR, Document Number 9514-016-500, December 1992


Report Name/Date:
RCRA Trial Burn Report for Light-Weight Aggregate Kilns 1 and 2, Aug 1999

Cond Description:
Trial Burn, Minimum operating temperature


Cond Description:
Trial Burn, elevated operating temperature, metals spiking

Content:
PM, HCl/Cl2, CO, HC, SVOC, VOC, D/F, Metals

D/F Rating Comments:
Copper spiked to maximize potential for D/F formation.  Is there a Cu feedrate limit?


Report Name/Date:
Risk Burn Final Report for Light-Weight Aggregate Kilns 1 and 2, Aug 2000

Cond Description:
Risk Burn, elevated waste feed rates, maximum temperature, minimum scrubber pH

D/F Rating Comments:
Not evaluated: report indicated metals spiking interferred with combustion efficiency


Report Name/Date:
Risk Burn-Phase 2 Final Report for Light-Weight Aggregate Kilns 1 and 2, Sept 2001

Cond Description:
Risk Burn, metal feeds equiv. to Jan '97 permit


Cond Description:
Risk Burn, metal feeds equiv. to June '01 permit


LVM Rating Comments:
Run 2 Cr emission outlier, not used in cond avg


Cond Description:
CoC, LOW COMB TEMP, HIGH HALOGEN FEED, HIGH SHW FEED


Cond Description:
CoC, HIGH COMB TEMP, HIGH HALOGEN FEED, HIGH SHW FEED

LVM Rating Comments:
Run 3 Cr emission outlier, not used in cond avg


Report Name/Date:
Emission Test Report for No. 4 Aggregate Kiln Solite Corporation, Leaksville Plant, Cascade, Virginia, Prepared by IEA, August 8, 1992


Report Name/Date:
RCRA Testing, Kilns 1,2,3,4, Certification of Compliance, August 1999


Report Name/Date:
Trial Burn Report, Solite Corp, Virginia Solite Div., March 2000

Cond Description:
Trial Burn, organics DRE, HCl/Cl2 emissions limits


Report Name/Date:
Trial Burn Report, Kiln 1 DRE Retest, Kilns 1-4 D/F. Solite Corp, Virginia Solite Div., July 2000

D/F Rating Comments:
NE- Research testing, D/F retest at lower FF temperature


Report Name/Date:
Emission Test Report for No. 4 Aggregate Kiln Solite Corporation, Leaksville Plant, Cascade, Virginia, Prepared by IEA August 8, 1992


Report Name/Date:
Stationary Source Sampling Report, Reference # 13967, Virginia Solite Company, Leaksville Plant, Cascade, Virginia, May 1995


Report Name/Date:
Emmision Test Results for No. 7 and No. 8 Aggregate Kilns, Solite Corporation, Arvonia, Virginia, Prepared by IEA, Project # 1381-003, August 8, 1992; COC Forms attached, August 21, 1992


Report Name/Date:
Trial Burn Report, Solite Corporation, A. F. Old Facility, Arvonia, Virginia, March 2000; Entropy Stationary Sampling Report, Reference No. 1702, Solite Corp Arvonia, VA, November and December 1999


Report Name/Date:
Recertification of Compliance for Kilns 7 and 8, Solite Corp, Arvonia, VA, July 27, 1999; Entropy Stationary Sampling Report, Reference No. 17091, Solite Corp Arvonia, VA, May 1999;


Cond Description:
CoC testing, metals and chlorine SRE demo


Report Name/Date:
PCDD/PCDF Emissions Testing Kiln 8, Solite Corporation, Arvonia, Virginia, EPA ID # VAD042755082, January 1997


Report Name/Date:
COC Forms AF Old Kiln No. 8, Solite Corporation, Arvonia, Virginia, March 18, 1996

LVM Rating Comments:
High LVM level in HW, likely from unreported spike contribution

SVM Rating Comments:
Unusually high SVM level in HW, likely due to unreported spike contribution?


Report Name/Date:
Texas Industries, Midlothian Cement Plant, Second Revision, Certification of Compliance, submitted to EPA Region VI and Texas Waste Commission of May 24, 1993, Revised October 10, 1992, prepared by Entellect

Cond Description:
CoC, DRE Mode 1, MAX HW FEED, POHC SPIKING, NO QUENCH

PM Rating Comments:
Data from 473 represents this kilns current emissions


LVM Rating Comments:
No Cr emissions.  Also data from source 473 currently represents this kiln

SVM Rating Comments:
Data from source 473 represents current emissions from this kiln


Report Name/Date:
Report on Polychlorinated Dibenzo-p-Dioxins and Polychlorinated Dibenzofurans Testing, Conducted at Continental Cement, CAE Project No. 6922, February 25, 1994


Report Name/Date:
Report on Diagnostic Testing, Performed for Continental Cement Company Stack, Hannibal, Missouri, CAE Project No. 6677-1, August 23, 1993


Cl Rating Comments:
Not evaluated: test condition with only 1 run; HCl emissions only


Cl Rating Comments:
Not evaluated: HCl emissions only, no chlorine gas emissions


Cl Rating Comments:
Not evaluated: not burning hazardous waste; HCl emissions only


Report Name/Date:
Report on Diagnostic Testing, Conducted at Continental Cement, Hannibal Missouri, CAE Project No. 6394, December 15, 1992


Report Name/Date:
Summary Report on PM Diagnostic Testing Conducted at Continental Cement, Hannibal, Missouri, CAE Project No. 6173/1, May 22, 1992

PM Rating Comments:
Not evaluated: failed run 4 (>0.08 gr/dscf)


Report Name/Date:
Air Source Technologies Report Prepared for Continental Cement, Project No. 411241, January 14, 1992


Report Name/Date:
Trial Burn and Certification of Compliance Test Report, Continental Cement Company, Hannibal, Missouri, July 1992


Report Name/Date:
Emissions Testing of a Wet Cement Kiln at Hannival, Missouri, for U.S. EPA OSW, prepared by MRI, December 1990


Report Name/Date:
Emissions Testing of a Wet Cement Kiln at Hannibal, Missouri, for U.S. EPA OSW, prepared by MRI, December 1990


Report Name/Date:
Report on Air Emissions Demonstration Testing, performed for Continental Cement Company, Kiln Stack, Back Housing, Cooler Stack, and ID Fan Outlet, Hannibal Missouri, CAE Project No. 6967, June 1, 1994


Report Name/Date:
Emission Test Report, Emissions Testing for PCDD/PCDF, PCBs, Volatiles, Semivolatiles, BIF Metals, and Particulates, Continental Cement, Hannibal, Missouri, DEECO Report 95-1192, February 16, 1995


Report Name/Date:
Trial Burn Report, Continental Cement Company, prepared by Gossman Consulting, September 1996

Cond Description:
TB, MAXIMUM TEMPERATURE CONDITIONS, metals testing


Cond Description:
TB, DRE, MINIMUM BURNING ZONE CONDITIONS


Report Name/Date:
Lafarge Corporation, Fredonia, Kansas Plant, November 1995 Recertification of Compliance, prepared by Radian, November 1995


Report Name/Date:
Lafarge Corporation Fredonia Plant Compliance Test Certification Package, prepared by Radian, August 1992

Cond Description:
CoC, MAX PROD,MAX HW FEED,MAX COMB TEMP,MAX ESP TEMP


Report Name/Date:
PCDD/PCDF Emission Testing Report - Fredonia Kansas Cement Plant, report from Gary Elliott (Lafarge) to Frank Behan (OSW), sent January 5, 1995; Fredonia PCDD/PCDF Report, Hans Schrama, dated November 1994


Report Name/Date:
Lafarge Fredonia Kansas, Certification of Compliance Revised Operating Conditions, Radian, September 1994

Cond Description:
CoC, MAX RAW MIX FEED RATE AND ESP INLET TEMP, MIN ESP POWER


Report Name/Date:
Emission Test Report, Measurements for PCDD/PCDDFs and HCl/Cl2 from a Wet Process Cement Kiln, Lafarge Corp, Fredonia, Kansas, DEECO Inc., August 9, 1993


Cond Description:
CoC, MAXIMUM OPERATING CONDITIONS FOR PRODUCTION OF CLINKER


Cond Description:
CoC, MINIMUM COMBUSTION ZONE, DRE DEMONSTRATION


Report Name/Date:
Pilot Combustion Minimization and Public Involvement Enhancement Program (PCMPIE) Test Report, prepared by Radian, June 1996

Cond Description:
LOW CHLORINE, HIGH ESP INLET TEMPERATURE


Cond Description:
HIGH CHLORINE, LOW ESP INLET TEMPERATURE


Cond Description:
CoC, OPERATING CONDITIONS AT MINIMUM TEMPERATURE


Cond Description:
CoC, OP COND AT MIN TEMP WHILE FEEDING AIR CONVEYED CANISTERS


Report Name/Date:
Lafarge Corp Fredonia Plant Compliance Test, Certification Package, prepared by Radian, August 1992


Report Name/Date:
Lafarge Corp, Fredonia, Kansas, Certification of Compliance, Revised Operating Conditions, prepared by Radian, September 1994


Cond Description:
HIGH CHLORINE, HIGH ESP INLET TEMPERATURE


Report Name/Date:
Trial Burn Report for the Aptus Rotary Kiln Incinerator in Aragonite, Utah, Alliance Project No. 5-008-999, August 1992

Cond Description:
Trial burn, MAX LIQUID AND DIRECT BURN FEED RATES

LVM Rating Comments:
Carbon injection system not used, old APCS


Cond Description:
Trial burn, to set oper limits on all constituents


Report Name/Date:
Evaluation of Polychlorinated Dibenzo-p-dioxins and Polychlorinated dibenzo-furan Formation in the Hazardous Waste Incinerator Operated by Aptus, Inc. at Aragonite, Utah, NAWC Report EM 94-31, October 1994

Cond Description:
Evaluation testing, HIGH, LOW APCD TEMP/NO SULFUR ADDITIVE


Cond Description:
Research test, HIGH, LOW APCD TEMP/SULFUR ADDITIVE


Report Name/Date:
Emission Test Report, Hazardous Waste Incinerator, Ross Incineration Services, Grafton, OHio, prpeared by International Technology Corp, JTN 332282, March 1993


Report Name/Date:
Performance Test Report, October 18-19, 2000; Performance Test Emission Results, Final Report, ENSR International, Jan 2001, Project No. 5763-003-300

Cond Description:
Low temperature, DRE, high solids, APCD detuned

Content:
PM, HCl, POHC DRE, Cr, Pb, Hg, Be (metals taken for evaluation purposes, no specific limits), D/F (also taken for evaluation purposes)

LVM Rating Comments:
NE- assumed metals tested for evaluation purposes only

SVM Rating Comments:
NE - metals tested for evaluation purposes only


Report Name/Date:
Trial Burn Test Report, Ross Incineration Services, Inc., Grafton, Ohio, OHD # 048 415 665, log # 157-257, May 1992


Report Name/Date:
Trial Burn Test Report, Ross Incineration Services, Inc., Grafton, Ohio, Prepared by PEI Associates, PN # 8431-9-3, April 1989


Report Name/Date:
Test Report for the RCRA Trial Burn on the TWI Unit 4 Incinerator, Trade Waste Incineration, Sauget, Illinois (ILD 098642424), Prepared by MRI, Project # 9730-M02, September 18, 1992


Report Name/Date:
Stationary Source Sampling Report, Reference No. 12327, Virginia Solite Cascade, Virginia, Kiln No. 1 Stack, March 24, 1994

Cond Description:
DRE / dioxin testing, MAX CL FEED, HIGH COMB TEMP


Cond Description:
DRE / dioxin testing, MAX CL FEED, low COMB TEMP


Report Name/Date:
Stationary Source Sampling Report, Reference No. 13967, Virginia Solite, Leaksville Plant, Cascade VA, Kiln Nos. 1 and 4 Stack, May 1995


Report Name/Date:
Particulate Matter, Sulfur Dioxide, NOx, Lead, CO, and PM-10 Emission Measurements at Virginia Solite Cascade, Oldover Corp., June 25, 1991


Report Name/Date:
BIF CoC forms prepared by Calvin Gover, Dick Carnes, and James Peters


Report Name/Date:
E. I. Dupont Company Trial Burn Test Program Emission Test Results, Orange, Texas, Prepared by Alliance Technologies, Project # 5-954999, August 1990

Cond Description:
Trial burn, MEDIUM TEMP/TYPICAL OP PARAMETERS


Report Name/Date:
Source Emission Survey of Dupont SRW Incinerator Stack Trial Burn, Orange, TX, July 2000

Content:
PM, HCl/Cl2, metals, Cr6, D/Fs, VOCs/SVOCs, PSD, SO2 (No CO)

D/F Rating Comments:
Assumed normal because of low temp DRE condition


Cond Description:
Trial burn, MAX TEMP/MAX WASTE,CL,ASH FEED


Report Name/Date:
Final Trial Burn Report for the Fluidized Bed Incinerator, Miles, Inc., New Martinsville, WV, ENSR Document No. 4690-009-400, September 1992

Cond Description:
Trial burn, MAX LIQUID FEED AND ASH INPUT


Report Name/Date:
Investigation of PCDD/PCDF Emissions from the Fluidized Bed Incinerator with and without Carbon Injection, December 1998


Report Name/Date:
As reported in Investigation of PCDD/PCDF Emissions from the Fluidized Bed Incinerator with and without Carbon Injection, December 1998 (as reported in) possibly also same as above 1992 trial burn


Report Name/Date:
Incinerator Trial Burn Report, Glaxo Inc., RTP NC, October 1993; Entropy Stationary Source Sampling Report, Reference No. 10983, August 1993


Cond Description:
Trial burn, high temp for liq mode oper.


Cond Description:
Trial burn, low temp for liq mode oper. Max feedrate


Cond Description:
Trial burn, high temp for solid mode oper. Max batch size


Cond Description:
Trial burn, low temp for solid mode oper. Max feedrate


Report Name/Date:
Hazardous Waste Trial Burn Performed for the Upjohn Company, Kalamazoo, MI, December 4-6, 1990, report dated March 3, 1992

Cond Description:
Trial burn, PART./METALS TESTING, HIGH SOLID FEED


Cond Description:
Trial burn, POHC TESTING, HIGH LIQUID HW FEED


Report Name/Date:
Results of the RCRA Trial Burn with VX Feed for the Liquid Incinerator at the Johnston Atoll Chemical Agent Disposal System, Jun 23, 1992, prepared by Southern Research Institute, SRI-APC-92-384-7530.11.1-I-R3


Report Name/Date:
JACADS Liquid Incinerator - Trial Burn Report, August 29, 1997

Content:
PM, HCl/HF, metals, PCDD/PCDF, VOC/SVOC (Runs 2-5)

Cl Rating Comments:
All considered same campaign; adding different modes of operation


Report Name/Date:
Results of the RCRA Trial Burn with GB Feed fo the Liquid Incinerator at the Johnston Atoll Chemical Agent Disposal System, June 17, 1991, SRI-APC-91-190-6967-006-F-R4


Report Name/Date:
Results of the Demonstration Test Burn for Thermal Destruction of Agent HD in the Johnston Atoll Chemical Agent Disposal System Liquid Incinerator, prepared by United Engineers and Constructors, Feburary, 1993


Report Name/Date:
Results of the RCRA Trial Burn and TSCA Demonstration Burn of the Deactivation Furnace System with M55 VX Rockets at the Johnston Atoll Chemical Agent Disposal System, June 23, 1992, SRI-APC-92-385-7530.5.1-I-R3


Report Name/Date:
JACADS- GB Trial Burn Report of the DFS Incinerator, July, 1998

Content:
PM, HCl/Cl2/HF, metals, PCDD/PCDF, DRE, VOC/SVOC (Runs 3-6)


Report Name/Date:
Tooele Chemical Agent Disposal Facility (TOCDF), RCRA Agents GB Trial Burn Report for the Deactivation Furnace System (DFS), Prepared by EG & G Defense Materials, Inc., April 9, 1997


Report Name/Date:
DFS GB ATB2 Report - Rev 1, July 7, 1999 (only have copy of select tables received in NODA comments, missing full report)


Report Name/Date:
Preliminary Trial Burn of the Occidental Chemical Corporation Liquid Waste Incinerator Facility, Niagara Falls, New York, Test Report, MRI Project No. 3539-M(02), February 10, 1994

Cond Description:
Preliminary trial burn, NOMINAL CONDITIONS

Cl Rating Comments:
NE-Preliminary test; assumed OPLs were not established

LVM Rating Comments:
Preliminary test; OPLs were not established

PM Rating Comments:
Preliminary Test-assumed OPLs were not established


Report Name/Date:
Trial Burn Report, Occidental Chemical Corporation, Niagara Plant Liquid Waste Incinerator Burning Organic and Aqueous Wastes, January 1998

Cond Description:
Trial Burn, Maximum Combined waste and fuel oil feed, minimum temperature, max stack gas flow, max Cl feed


Report Name/Date:
Trial Burn of the Occidental Chemical Corporation Liquid Waste Incinerator Facility, Niagara Falls, New York, Test Report, MRI Project No. 3539-M(03), March 16, 1995

Cond Description:
Trial burn, LOW COMB TEMP/HIGH WASTE FEED


Cond Description:
Trial burn, HIGH COMB TEMP/HIGH WASTE FEED


Report Name/Date:
Trial Burn Report for Emission Source Test of Waste Propellant Incinerator 6A at Radford Army Ammunition Plant, Radford, Virginia, Prepared by DRE Environmental Services, June 1993


Report Name/Date:
830 Incinerator Trial Burn Report, ID # MID 000 724, Summary of Results and Program Description, Dow Chemical Company, March 1992

Cond Description:
Trial burn, NORMAL KILN TEMP, HIGH CL AND METAL FEED, metals results considered invalid shice lab failed to analyze the EPA audit sample


Cond Description:
Trial burn, LOW KILN TEMP, HIGH CL AND SOLIDS FEED


Cond Description:
Trial burn, LOW KILN TEMP,MAX ASH&CONTAINER BTU FEED


Cond Description:
Trial burn, NORMAL KILN TEMP, MAX CHLOROSILANES FEED


Cond Description:
Trial burn, METALS RE-TEST; HIGH CHLORINE

LVM Rating Comments:
Feedrate extrapolation used to set limit

SVM Rating Comments:
Feedrate extrapolation used to set limit


Report Name/Date:
RCRA Trial Burn Report for a Dual Purpose RCRA/TSCA Incinerator at the U.S. Department of Energy's K-25 Facility in Oak Ridge, Tennessee, August 31, 1989

Cond Description:
Trial burn, MAX WASTE, CL, ASH FEED; MINIMUM TEMP


Report Name/Date:
Final Report, Trial Burn of the TSCA Incinerator, U.S. Department of Energy, Oak Ridge East Tennessee Technology Park, Oak Ridge Tennessee, September 7, 2001, TRC Project No. 02261 - 0020 - 00000


Cond Description:
PCDD/PCDF data from 1995 testing provided to EPA by DOE


Report Name/Date:
Ash Grove Cement, Foreman Arkansas, RCRA Trial Burn Report and Certification of Compliance for Kiln No. 3 - July 1992, dated November 1992


Cond Description:
Trial burn: Max comb temp, max metals, chlorine, raw material feedrate, max APCD temp, min ESP power


Report Name/Date:
Ash Grove Cement, Foreman Arkansas, Report of RCRA Trial Burn for Kiln No. 3, January 1995, dated June 1995

Cond Description:
CoC, MAX FEED & CHLORINE, MIN. COMB. TEMP.

PM Rating Comments:
Not evaluated: failed Run 2 (<0.08 gr/dscf)


Cond Description:
CoC, MAX FEED, PRODUCTION, CHLORINE, & COMB. TEMP. MIN ESP POWER


Cond Description:
LOW KILN EXIT TEMP, LOW PARTICULATE MATTER LOADING


Cond Description:
EER/EPA sponsored research testing with copper and water quench


Report Name/Date:
FMC Hazardous Waste Incinerator Trial Burn Test Report, prepared for FMC Agricultural Chemical Group, Baltimore, Maryland, prepared by Scott Environmental Services, August 1986, SET 1619-03-0886


Report Name/Date:
Baltimore Plant Hazardous Waste Trial Burn Report, Dec 27,2000

Cond Description:
Trial burn, high temperature operation, spiking of ash and metals, (Metals spiked in wastewater)

Content:
PM, HCl/Cl2, CO, HC, NOx, POHC DREs, Metals, PCDD/F


Report Name/Date:
POHC Trial Burn Stack Emission Test Series John Zink Thermal Oxidizer, Akzo Chemie, America, Morris, Illinois, Prepared by ARI Environmental, Project # 432-01, September  18-20, 1984


Report Name/Date:
Trial Burn Sampling and Analysis Results for the Mobay Incinerator, Kansas City, MO, Final Report, MRI, November 1984


Cond Description:
Trial burn, worst case, max temp, max feedrate


Report Name/Date:
EPA OSW Sponsored Evaluation Testing, November 1988


Report Name/Date:
Stationary Source Sampling Report, Reference No. 6036, Allied Fibers, Hopewell, Virginia, October 12-14, 1988


Report Name/Date:
PCDD/PCDF data only as reported in Inc reported in Inc Conf"Application of an Ultra Clean Technique for the Measurement of Trace Dioxin and Furan Levels in Source Emissions," Bruce Maisel, L. Davis, and M. Wood, 1997 Incineration Conference, May 12-16, 1997, Oakland California, pp. 355-360

Cond Description:
PCDD/PCDF data only as reported in Inc Conf


Report Name/Date:
Final Report on RCRA Trial Burn Test Results to SmithKline Chemicals from Batelle Columbus Labratories, November 12, 1984


Report Name/Date:
RCRA Trial Burn Report for HD - Mustard Ton Containers - Metals Parts Furnace at the Johnston Atoll Chemical Agent Disposal System, December 16, 1992


Report Name/Date:
JACADS Metal Parts Furnace Halogenated Waste Performance Test, March 2001

Cond Description:
Halogenated waste trial burn, no metals spiking nor DRE

Content:
PM, HCl/Cl2/HF, metals, PCDD/PCDF, VOC/SVOC, PCB, total organics, limited feed analysis

Hg Rating Comments:
All tests considered to be the same campaign; recent test added new mode of operation


Report Name/Date:
JACADS Metal Parts Furnace 4.2-Inch Agent HD Mortar Projectiles Trial Burn Report, August 1999

Content:
PM, metals, HCl, Cl2, HF, D/F, CO, DRE, SVOC, VOC, no metals spiking


Report Name/Date:
GB Trial Burn Report, Trial Burn of the MPF Incinerator, Johnston Atoll Chemical Agent Dispoal System, Johnston Island, July 1998


Report Name/Date:
Re-certification of Compliance, Texas Industries Resource Recovery Program, May 8, 1995, prepared by Entellect


Report Name/Date:
Stationary Source Sampling Report Reference No. 11583, Virginia Solite Corporation, Cascade, Virginia, Prepared by Entropy, June 1993; COC Forms attached, dated August 23, 1993


Report Name/Date:
Stationary Source Sampling Report Reference No. 11438, Solite Corporation, Arvonia, Virginia, Prepared by Entropy, February 1993; COC Forms attached, dated January 28, 1994


Cond Description:
CoC, high temperature metals and chlorine testing


Report Name/Date:
Test Report for Trial Burns on the Prowl Incinerator at the American Cyanamid Facility, Hannibal, Missouri, Prepared by MRI, Project # 9353-L(02), August 9, 1989

Cond Description:
ORGANICS SPIKED INTO LIQUID AND AQUEOUS WASTES


Report Name/Date:
Re-Test Report for Trial Burns on the Prowl Incinerator at the American Cyanamid Facility, Hannibal, Missouri, Prepared by MRI, Project # 9353-L(02), November 6, 1989

Cond Description:
LOW CO LEVELS, AQUEOUS (FIREWATER) SPIKED WITH MCB


Cond Description:
HIGH CO LEVELS, AQUEOUS (ACTUAL PLANT WASTE) SPIKED WITH MCB


Report Name/Date:
Dioxin/Furan Emission Test Results for Incinerators Final Report, For American Cyanid Company, Prepared by MRI, Project # 4435, August 13, 1996

Cond Description:
DIOXIN/FURAN EMISSIONS TESTING - AQUEOUS/ORGANIC WASTE


Cond Description:
DIOXIN/FURAN EMISSIONS TEST - AQUEOUS/ORGANIC WASTE


Report Name/Date:
Test Report for the RCRA Trial Burn, February 2, 1998


PM Rating Comments:
NE - miniburn - unknown if OPLs established as result of test


Report Name/Date:
Test Report for VOST Retest, October 1998


Report Name/Date:
Supplemental Low Grade Fuel Trial Burn, Kiln No. 2, Norlite Corporation, Cohoes, New York, June 1990, Prepared by APCC

Cl Rating Comments:
Not evaluated: no Cl2 emissions data, pre-BIF

LVM Rating Comments:
Data from source 307 represents this kiln, no Be data

SVM Rating Comments:
Data from source 307 represents this kiln


LVM Rating Comments:
Not evaluated: not burning hazardous waste during test

SVM Rating Comments:
Not evaluated: not burning hazardous waste during test


Report Name/Date:
Source Emissions Survey of Ciba-Geigy Corporation, Multi Purpose Incinerator Stack, St. Gabriel, Louisiana, Prepared by METCO Environmental, File # 93-265, December 1993


Report Name/Date:
Trial Burn Report for Arkansas Eastman Company No. 2 Incinerator, Batesville, Arkansas, July 1987

Cond Description:
Trial burn, DEMONSTRATE DRE FOR AQUEOUS WASTE


Cond Description:
Trial burn, DEMONSTRATE PM REMOVAL FOR WASTES W/DISSOLVED SALTS


Cond Description:
Trial burn, DEMONSTRATE DRE AND HCL REMOVAL FOR HIGHLY CHLORINATED WASTE


Report Name/Date:
MWP-2000 Trial burn Report, for Trial Burn conducted January 7, 1992 at El Dorado Arkansas, ENSCO, Little Rock Arkansas, dated April 10, 1992


Report Name/Date:
Environmental Systems Company Fixed Base Incinerator Trial Burn Report, El Dorado, Arkansas, prepared by METCO, April 14, 1992

Cond Description:
Trial burn, SURR. SOLID TO #1,2; MAX SOLIDS TO #1; LIQ. FEED TO TOU/WFB


Cond Description:
Trial burn, SURR. SOLID TO #1,2; MAX SOLIDS TO #2; LIQ TO TOU; NG OT WFB


Cond Description:
Trial burn, NG TO #1,2; MAX LIQ TO TOU; NG TO WFB


Report Name/Date:
Rollins Environmental Services (TX) Inc. Trial Burn Program Incinerator Train I Emission Test Results, Deer Park, Texas, Prepared by Alliance Technologies Corporation, ID # - 5-919-999, September 1989


Report Name/Date:
Res(TX) Trial Burn Program Rotary Reactor / Incinerator Train II, Emission Test Results, Final Report, Prepared for Rollins Environmental, Deer Park TX, prepared by Alliance Technologies, Project No. 5-950-999, October 1989


Report Name/Date:
Hazardous Waste Incinerator No. 2, Trial Burn Report, Ciba-Geigy Corp, McIntosh, Alabama, Volume I of V, June 1994

Cond Description:
Trial burn, HIGH KILN EXIT TEMPERATURE, METALS SPIKING


Report Name/Date:
Hazardous Waste Incinerator No. 2, Trial Burn Report of Results, Ciba Specialty Chemicals Corporation, McIntosh, Alabama, July 2000

Cond Description:
Trial burn, POHC DRE, low temp, max feed and gas velocity


Cond Description:
Trial burn, worst case for metals, PM, chlorine (max temp, max feedrates)


Cond Description:
Reasonable worst case, low temp PIC risk burn


Cond Description:
Trial burn, LOW KILN EXIT TEMPERATURE, DRE


Report Name/Date:
1995 Recertification at Essroc Materials, Inc, Logansport, Indiana, APCC Project No. 95001, August 1995

Cond Description:
CoC, MAX COMB TEMP, MAX METALS/CL FEED, MAX APCD TEMP

Cl Rating Comments:
Data for source 300 currently represents this kiln

Hg Rating Comments:
Data from source 300 represents current emissions from this kiln

LVM Rating Comments:
Not evaluated: data from source 300 represents this kiln

PM Rating Comments:
Data for source 300 represents current emissions

SVM Rating Comments:
Data from source 300 currently represents this kiln


Cond Description:
CoC, MIN COMB TEMP, MAX CL FEED, MAX PROD RATE


Report Name/Date:
Texas Eastman Company Trial Burn Program Emission Test Results, Alliance Project No. 5-986-999, April 5, 1991


Report Name/Date:
Trial Burn Report, Fluid Bed Incinerator, Jan 1999

Content:
PM, Hcl/Cl2, DRE, D/Fs, V/SV PICs, CO, PSD, aldehydes/ketones


Content:
PM, HCl/Cl2, metals, Cr6, & waste feed ash/Cl/metals


Report Name/Date:
Tooele Chemical Agent Disposal Facility (TOCDF), RCRA Agent Trial Burn Report for the Liquid Incinerator System No. 1, EG&G Defense Materials, Inc., July 7, 1997


Report Name/Date:
TOCDF, Agent GB Mini-Burn Report for the Liquid Incinerator System #1, EG&G Defense Materials Inc., January 20, 1999

Cond Description:
Trial burn to set arsenic operating limits (waste with higher than average arsenic used), and gather risk burn data for other constituents


Report Name/Date:
Tooele Chemical Agent Disposal Facility (TOCDF), RCRA Agent Trial Burn Report for the Metal Parts Furnace, EG&G Defense Materials, Inc, August 15, 1997


Report Name/Date:
PCDD/PCDF data reported in "Results from the Metals Parts Furnace Performance Standard Demonstration Burn Using Ton Containers with Agent GB Heels," Timothy Booth, Michel Foster, T. Bumann, and C. McBride, 1997 Incineration Conference, Oakland CA, May 12-16, 1997, pp. 677-681


Report Name/Date:
Stationary Source Sampling Report, Reference No. 5471, PPG Industries, Circleville, OH, January 11 - 15 1988

Cond Description:
Trial Burn, Slagging Kiln With Maximum Solids Loading


Report Name/Date:
Final Trial Burn Report for the Energy Recovery Unit/March, 1998

Content:
PM, HCl/Cl2, PCDD/PCDF, DRE (PERC, MCB), SVOCs, VOCs,CO,NOx,SO2


Cond Description:
Trial Burn, High Temperature, Metals Spike (Pb,Cr,As)

Content:
PM, HCl/Cl2, metals, Cr+6, PCDD/PCDF, SVOCs, VOCs


Cond Description:
Trial Burn, Non-Slagging Kiln With Maximum Solid Loading


Report Name/Date:
Trial Burn Report for Explosive Waste Incinerator at Lake City Army Ammunition Plant, Independence, Missouri, March 1993


Report Name/Date:
3rd Trial Burn Program, Lake City Army Ammunition Plant, Explosive Waste Incinerator, Olin Corporation, Independence, Missouri, TRC Projection No. 17791, January 1996

Cond Description:
Trial burn, 5.56mm M855 SAWS feed, max metal feed


Cond Description:
Trial burn, 20mm M56 HEI feed, max metal feed


Report Name/Date:
APE 1236 Explosive Waste Incinerator Risk Burn Report

Cl Rating Comments:
Assumed risk burn conducted at normal conditions

PM Rating Comments:
Assumed risk burn conducted at normal conditions


Report Name/Date:
Air Pollution  Emission Assessment # 42-21-0475-91, Trial Burn for Deactivation Furnace Building 97, Lake City Army Ammunition plant, Independence, Missouri, February 19- March 6, 1991


Cond Description:
Trial burn, HI SKOR 700X Propellant Feed


PM Rating Comments:
PM emissions exceeded current RCRA standard


Report Name/Date:
EPA Trial Burn Emission Testing of BASF Incinerator Unit # IN-701, BASF Corporation, Freeport, Texas, Prepared by NUS Corporation, Project # 4963, November 1986


Report Name/Date:
Rotary Kiln Application Trial Burn Results, RCRA Permit HW-50161-001, Dow Chemical Company, Freeport, Texas

Cond Description:
Trial burn, Avg. Temp to meet 99.99% DRE


Cond Description:
Trial burn, MAX. heat duty, MIN. INCINERATOR RES. TIME


Report Name/Date:
Rotary Kiln Supplemental Trial Burn Results, RCRA Permit HW-50161-001, December 14, 1995; Compliance Test Report, Texas Rotary Kiln, Dow Freeport TX, Sampling Date: July 11-13, 1995

SVM Rating Comments:
Assumed OPLs were established as result of test


Report Name/Date:
Trial Burn Report, Chemical Waste Management Incinerator Facility, Port Arthur, Texas, prepared by Radian, May 25, 1990

Cond Description:
Trial Burn, DRE On Non-Energetic And Energetic Sludge Fed To Kiln


Cond Description:
Trial Burn, Dre On  Energetic Liquid And Sludge


Report Name/Date:
Trial Burn Report, Bi-Annual Stack Test on the Hazardous Waste Incinerator System, prepared by Radian for Chemical Waste Management, Port Arthur, TX, October 19, 1994

Cond Description:
Bi-Annual Stack Test At "Normal" Operating Conditions


Report Name/Date:
Supplemental Trial Burn, Chemical Waste Management Incinerator Facility Port Arthur Texas, prepared by Radian for Chemical Waste Management, October 10, 1990

Cond Description:
Trial Burn, Min Kiln Temp (1200F), Min Heat Input


Cond Description:
Trial Burn, Min Kiln Temp (1300F), Min Heat Input


Report Name/Date:
Toxic Substances Control Act Trial Burn Report, Chemical Waste Management Incinerator Facility, Port Arthur, Texas, prepared by Radian, June 30, 1990


Report Name/Date:
2000 Bi-Annual Stack Test/Trial Burn - Chemical Waste Mgmt, Inc. Port Arthur, TX, June 2000

Cond Description:
RCRA / TSCA Biannual Trial burn, normal metal feeds

Content:
PM, HCl/Cl2, metals, DRE, PCDD/F,VOC/SVOC, HC, NOx, SO2


Report Name/Date:
Report, 1998 Bi-Annual Stack Test / Risk Assessment Test / Trial Burn,  Chemical Waste Management Inc., Port Arthur, Texas Incinerator, prepared by Radian Int., Nov 13, 1998

Cond Description:
Bi-annual testing trial burn, max temp, max metals feeds


Cond Description:
Bi-annual testing, typical operations (metals at historic feedrates)


Report Name/Date:
Bi-Annual Stack Test on the Hazardous Waste Incinerator System, Port Arthur, Texas, prepared by Radian, September 21,1992, DCN # 263-091-05-00, Prepared for, Chemical Waste Management Inc.

Cond Description:
Bi-Annual Stack Test At "Normal" Operating Condition


Cond Description:
Demonstrate Operating Conditions Outside Current Permit


Cond Description:
Demonstrate Operating Conditions Outside Permit


Cond Description:
Trial Burn, Pohc Dre On Energetic Sludge & Liquid And Aqueous Liquid Fed


Cond Description:
Trial Burn, Dre On Non-Energetic Sludge & Liquid And Energetic Solid Fed


Cond Description:
Trial Burn, DRE On Non-Energetic Solids Fed To Kiln


Cond Description:
Trial Burn, DRE On Energetic Liquid Fed To SCC


Report Name/Date:
Test Report for the Trial Burn on the Aniline Incinerator at BASF Corp. in Geismar, LA , Final Report, December 1992.

Content:
PM, metals, DRE, NOx/CO/THC, VOC/PICs, metal feeds


Report Name/Date:
REX(TX) Stack Test Results, Incinerator Trains I/II Tri-Annual RCRA Requirements and TSCA (PCB) Testing, prepared for Rollins Environmental Services, Deer Park TX, prepared by TRC Environmental, April 1995

Cond Description:
TRAIN I: IS A RCRA AND TSCA PERMITTED INCINERATOR


Report Name/Date:
Trial Burn/ Risk Burn Report Conditions 1,2 and 4, August 1998

Cond Description:
Risk burn organics, max RR feed, low temp-Condition 1


Cond Description:
Risk burn metals, high temp, max RR feed, moderate metals spike - Condition 2


Report Name/Date:
Trial Burn/ Risk Burn Report Conditions 3I and 3II, October 1998

Cond Description:
Trial burn, min temp, max feedrate, DRE train I - Condition 3i


Cond Description:
Trial burn, min temp, max feedrate, DRE train II - Condition 3ii


Cond Description:
Trial burn, max temp, max metals spike - Condition 4


Report Name/Date:
PM, HCl, and HCl Removal Efficiency Compliance Emissions Sampling of Incinerator NCIN-1, Shell Chemical Co, NORCO, LA, December 1991, SwL Project No. 54-9112-065

Report Prepared:
Southwestern Laboratories, Environmental Analytical Services Div.

Testing Firm:
Southwestern Laboratories, Environmental Analytical Services Div.


Report Name/Date:
Source of Emissions Survey of Shell Chemical Company NCIN 1 Stack, February 1998.

Cond Description:
Trial burn, low temp, no water injection, low waste feed


Cond Description:
Trial burn, upper oper temp, max waste, max water injection


Cond Description:
Risk burn, reasonable upper bound on normal operation


Report Name/Date:
Air Emissions Compliance Sampling for Consolidated Air Permit No. 2252, NCIN-2 Incinerator and Biosolids Incinerator, Shell Chemical Co., NORCO West Site, NORCO, LA, July 1994, SwL Project No. 5354-9406-003

Report Prepared:
Huntingdon/Southwestern Lab, Air Emissions Services Division

Testing Firm:
Huntingdon/Southwestern Lab, Air Emissions Services Division


Report Name/Date:
Source of Emissions Survey of Shell Chemical Company NCIN 2 Stack, February 1998.


Report Name/Date:
Test Report for the RCRA Trial Burn on the Unit 3 Incinerator, Trade Waste Incineration, Sauget, Illinois, ILD 098642424, Prepared by MRI, Project # 4341-02, January 21, 1997

Cond Description:
Trial burn, Worst case operating conditions


Report Name/Date:
Environmental Assesment of the Texas Eastman Hazardous Waste Incinerator, February, 1985, Prepared by Acurex, Project # 6699, Purchase Order # 144-0078-B-P, Longview, Texas


Report Name/Date:
Trial Burn Report, Rotary Kiln Incinerator, Texas Eastman Division Eastman Chemical Company, Longview, Texas, January 4, 1999

Cond Description:
Trial burn, high temp metals and chlorine determination


Cond Description:
Trial burn, low temp DRE and risk burn, max ash

Content:
PM, HCl/Cl2, HF, HBr, D/F, SVOC, VOC, PAH, aldehyde/ketones, CO


Report Name/Date:
Test Report on Exhaust Emissions from VCM Incinerator CC-IN-1 (550) at the Oxymar VCM Production Facility, Gregory Texas, prepared by Cubix Corporation, Job # 2924, November, 1994


Report Name/Date:
Metals and HCl/Cl2 Source Emission Test on No. 3 Kiln Baghouse Exhaust, Giant Cement Co., Harleyville, SC, prepared by Davis and Floyd

Cl Rating Comments:
Data for source 200 currently represents this kiln

Hg Rating Comments:
Data from source 200 represents current emissions from this kiln

LVM Rating Comments:
Data from source 200 currently represents this kiln

PM Rating Comments:
Data for source 200 represents this kilns current emissions

SVM Rating Comments:
Data from source 200 currently represents this kiln


Report Name/Date:
Metals and HCl/Cl2 Source Emission Test on No. 2 Kiln Baghouse Exhaust, Giant Cement Co., Harleyville, SC, prepared by Davis and Floyd

Cond Description:
State of South Carolina emissions testing requirements


Report Name/Date:
Stationary Source Sampling Report, Reference No. 10181A, Giant Cement, Harleyville, SC, June 5, 1991

Cond Description:
State of South Carolina emissions testing requirements, pre-BIF


Report Name/Date:
Test Report for the RCRA Trial Burn on the Du Pont Experimental Station Hazardous Waste Incinerator, Wilmington, Delaware, Prepared by MRI, Projecct # 6495-M(04), August 13, 1992


Report Name/Date:
Stationary Source Sampling Report, Reference No. 6181, Eli Lilly and Company, Clinton, Indiana, C-10 Incinerator Stack, February 21-24, 1989


Report Name/Date:
Ciba Giegy St. Gabriel, Louisiana Trial Burn on Hazardous Waste Liquid Incinerator, # LAD053783445 July 15, 1988


Report Name/Date:
Dupont Central Scubbed Incinerator(CSI) Trial Burn Report, DCN 89-274-015-02, Prepared by Radian Corp., La Porte, Texas, January 5, 1989


Cond Description:
Trial burn, max temp, max feedrate, worst oper cond


Report Name/Date:
Stationary Source Sampling Report, Reference No. 10786, Burroughs Wellcome Company, Greenville, NC, NcGill No 2 Incinerator, November 18-20, 1992

Cond Description:
Triak burn, minimum temperature, maximum feed rate


Cond Description:
Trial burn, minimum temperature, maximum feed rate


Cond Description:
Trial burn, minimum temperature, maximum feed rate.


Report Name/Date:
Stationary Source Sampling Report, prepared for Nepera, Incorporated, prepared by ENTROPY Environmentalists, Emissions Testing, Incinerator Stack R238 VENT, February 1993, Harriman, New York, Reference # 11546


Report Name/Date:
Stationary Source Sampling Report, prepared for Nepera, Incorporated, prepared by ENTROPY Environmentalists, Emissions Testing, Incinerator Stack R238 VENT, September 1992, Harriman, New York, Reference # 11179


Report Name/Date:
Incinerator Trial Burn Test Results Olin Corporation (now Lyondell), Lake Charles Louisiana, Prepared by Radian Corporation, January 27, 1989

Cond Description:
Trial burn, MAX CHLORINE,T-101, AND STACK FLOW RATE


Report Name/Date:
Trial Burn Report Olin - Lake Charles Plant

Cond Description:
Minimum operating temperature w/TDI residue


Cond Description:
Trial burn, MIN COMB TEMP/MAX TDI RESIDUE


Cond Description:
Trial burn, MAX TDI RESIDUE & MAX T-101 WASTE LIQUID


Report Name/Date:
Recertification of Compliance for Tennessee Eastman Division Boilers 23 and 24; dated September 1, 1998

Cl Rating Comments:
R1 not reported; sample train leak check failure


Content:
Total organics, CO, volatile organics, PCDD/PCDFs, SV organics, aldehydes/ketones, PM size distribution; metals, chlorine in feedstreams


Report Name/Date:
Certification of Compliance, Boiler 4 Celanese Ltd/October 1998

Report Prepared:
TRC Environmental Corporation, Houston, TX

Content:
Stack PM; Feed analysis of organics and ash.


Report Name/Date:
Compliance Test Report, Boiler 4, Celanese Ltd/October 1998


Report Name/Date:
Trial Burn/Risk Bum Report, Boiler 4, Celanese Ltd/November 1998

Content:
VOC, Total Organics, SVOCs, PCDDs/PCDFs, Particle Size Distribution, aldehydes, and ketones.


Report Name/Date:
Recertification of Compliance (ReCOC) for Merichem; report provided begins at section 2.0 (no date)

Testing Firm:
Focus Environmental, Inc (Ramcon Environmental Corporation)

Cond Description:
CoC; min combustion temp; Wet Scrubber not used


Cond Description:
CoC; max waste feed (spiked ash, chlorine, metals), Wet Scrubber not used

Content:
PM, HCl/Cl2, metals, CO;  ash, metals, chlorine in feeds

Cl Rating Comments:
Chlorine spiked for chlorine feed limit for setting Tier III metals limits


Report Name/Date:
Stationary Source Sampling Report, prepared for ICI Americas Inc., prepared by Entropy Environmentalists, Hazordous Waste Incineration Testing, LV-3 Incinerator Stack, June 19-21, 1990, Bayonne, New Jersey, Reference # 6743


Report Name/Date:
Stationary Source Sampling Report, Reference No. 11112, ICI Americas, Inc., Bayonne, New Jersey, LV-3 Incinerator, August 26-27, 1992


Report Name/Date:
Stationary Source Sampling Report, prepared for Eli Lilly and Company, prepared by Entropy Environmentalists, Hazordous Waste Incineration Testing, Brule Incinerator Stack, November 18, 1987, Mayaguez, Puerto Rico, Reference # 5720


Report Name/Date:
Compliance Recertification for Boiler A Pursuant to the BIF Regulations, August 1998


Report Name/Date:
Compliance Recertification for BIF Units R-1and R-3 Pursuant to the BIF Regulations, March 1999


Report Name/Date:
BIF Compliance Certification and Results of the Trial Burn for BIF Units U-304 and U-305; August 1992


Report Name/Date:
Revised Certification of Compliance Test Report for Boilers 70K, 30K, and 28K, August 21, 1996

Testing Firm:
Spectrum Compliance Resources, Inc., METCO Environmental, B3 Systems, Inc

LVM Rating Comments:
Cr+6 emissions only, Cr/Cr+6 ratio testing


Report Name/Date:
Trial Burn Report for Boiler 70K, February 3, 2000

Testing Firm:
METCO Environmental (Stack sampling), B3 Systems, Inc (Feed spiking)

Content:
PM, CO, HCl/Cl2, PCDD/PCDF emissions; metals/chlorine in feedstreams

LVM Rating Comments:
NE; only consider most recent compliance test campaign


Report Name/Date:
Mini Burn Test Report for Boiler 70K, July 10, 2000


Report Name/Date:
Trial Burn Retest Report for Boiler 70K, July 10, 2000

Cond Description:
Trial burn retest, min comb cham temp, min prod rate


Report Name/Date:
Trial Burn Report for Boiler 30K, February 3, 2000

Cond Description:
Trial burn, high feed rate, max steam prod


Cond Description:
Trial burn, min comb temp, min steam prod rate


Report Name/Date:
Trial Burn Retest Report for Boiler 30K, July 10, 2000

Cond Description:
Trial burn retest, min comb temp, min steam prod rate


Report Name/Date:
1998 BIF Compliance Recertification, December 1998


Cond Description:
CoC, acryloid coatings waste blend, max ash feed (ash spiking)


Report Name/Date:
Source Emission Survey of Rohm & Haas Texas, Inc. HT-1 Thermal Oxidizer Stack (EPN HT-3), BIF Certification Test, No. 99-196A, July 1999

Content:
PM, CO emissions; metals, chlorine, and ash in feeds


Report Name/Date:
Certification of Compliance Boiler No. 100, Nov. 19, 1999

Cond Description:
CoC; max waste feed rate, ash spiking (TiO2)

Content:
PM, CO in stack gas; metals, chlorine and ash in feedstreams


Report Name/Date:
Source Emissions Survey for Schenectady International B-503, File # 96-99; no date reported

Content:
PM, CO; metals and chlorine in feedstreams


Report Name/Date:
Sterling Chemicals, Inc. BIF Recertification of Compliance Test Waste Oxidation Boiler A; Sept/97

Content:
PM, CO; metals, chlorine, and ash in feeds


Report Name/Date:
Trial Burn Report, Boiler 31, Union Carbide Corporation, June 1998

Cond Description:
Risk burn -- normal operating conditions


Content:
PM only (no DRE), CO, ash (titanium oxide) spiked


Report Name/Date:
Revised Certification of Compliance, January 29, 1999

Content:
PM, CO emissions; metals, ash, Cl feed analysis


Report Name/Date:
Source Emissions Survey of DSM Copolymer Boiler Number 3 Risk Burn, April and May 1997; also Risk Burn Summary - Final Report, DSM Copolymer, January 1998


Report Name/Date:
Recertification of Compliance, DSM Copolymer Plant, July 22, 1996

Content:
PM, CO, HCl/Cl2; metals, chlorine in feedstreams


Report Name/Date:
Source Emissions Survey of E.I. Dupont De Nemours & Company, Inc. Sabine River Works

Cond Description:
CoC; max comb temp, haz waste feed and steam prod rate


Report Name/Date:
Source Emissions Survey of E.I. Dupont De Nemours & Company, Inc. Sabine River Works , Risk Burn, 98-183D, July 1998


Report Name/Date:
Source Emissions Survey of E.I. Dupont De Nemours & Company, Inc. Sabine River Works, DRE Burn, Dec. 1998, No. 98-305A


Report Name/Date:
Source Emissions Survey of E.I. Dupont De Nemours & Company, Inc. Sabine River Works, DRE Burn, 98-183C, July 1998


Cond Description:
CoC; max temp, haz waste feed and prod rate


PM Rating Comments:
NE; only consider most recent compliance test campaign; Assume N


Report Name/Date:
Source Emissions Survey for DuPont ADN South Boiler Stack, DRE Burn, 98-305B, 1998


Report Name/Date:
Source Emissions Survey for DuPont ADN South Boiler Stack, Risk Burn, 98-305, 1998


Report Name/Date:
RCRA Boiler and Industrial Furnace Recertification of Compliance Report Boiler No. 4, November 1999

Content:
PM, CO, HCl/Cl2 in stack gas; metals, ash, Cl in feed


Report Name/Date:
Revised Recertification of Compliance of BIF Boilers H530A and H530B at GE Plastics, February 1998

PM Rating Comments:
No ash spiking; NE; only consider most recent compliance test campaign


Report Name/Date:
Revised Recertification of Compliance of BIF Boilers H530A and H530B, GE Plastics Mt. Vernon Facility, February 1998


Report Name/Date:
Recertification of Compliance Boilers H530A and H530B, GE Plastics Mt. Vernon Facility, September 2001

Content:
PM and CO emissions; waste feed ash, chlorine, metals


Report Name/Date:
Boiler and Industrial Furnace Compliance Test Report and Certification of Compliance - General Electric Plastics Plant, August 1998

Content:
PM, CO emissions; ash, metals, and chlorine anaysis of feedstreams


Report Name/Date:
Test Report for Recertification of Compliance of BIF Boilers B-101, B-102, B-103, B-104, & B-105, July 1995, Test Report II for ReCoC, Nov. 1995

Report Prepared:
The Goodyear Tire and Rubber Co. and Radian Corp.

Cond Description:
CoC; max waste feedrate and steam prod rate


Cond Description:
CoC; less aggressive max waste feed and max prod rate


Cond Description:
CoC; similar to C1 but higher prod rate, lower chamber temp


Report Name/Date:
Trial Burn Report for BIF Boilers B101-B105, July 1999


Cond Description:
Trial burn, max waste feed, max steam prod


Report Name/Date:
Risk Burn Report for BIF Boilers B101-B105, Revision 1, July 1999

Cond Description:
Risk burn, worst case cond, max waste feed and max prod


Report Name/Date:
Trial Burn Report Addendum U-3 Boiler, December 1997

Cond Description:
Trial burn; max comb temp, max prod rate, max benzene

Cl Rating Comments:
Chlorine spiked and limit set for complying with metals


Cond Description:
Trial burn; min comb temp and min prod rate, max moisture/methanol feed


Report Name/Date:
Certification of Compliance for Boilers A/B & C; May 23, 1997


Report Name/Date:
Certification of Compliance Forms, November 1998

Cond Description:
CoC; max feeds for T-303 bottoms and IPOH

Content:
PM, Cl2, CO emissions; metals and chlorine in feedstreams


Report Name/Date:
BIF Recerification of Compliance Test Report - Boilers 1 and 2; dated August 20, 1997

Content:
PM, CO, HCl/Cl2, Cr emissions; metals, ash, Cl feed analysis


Report Name/Date:
BIF Recertification of Compliance Test Report - Boilers 1 and 2; dated August 20, 1997

Content:
PM, CO, HCl/Cl2, Cr emissions; metals/ash/Cl feed analysis


Report Name/Date:
Recertification of Compliance Test Report for Boiler No. 1, 8/27/98; Compliance Emission Test Report - Boiler No. 1, 8/21/98.

Content:
PM, CO, Cr/Cr+6 emissions; ash, Cl, and metals feeds


Testing Firm:
METCO Environmental (Source Emissions Survey of Borden Chem., April 1998, File No. 98-118)


Cond Description:
CoC; Lower scrubber recirculation rate, low scrubber pH


Report Name/Date:
R-30 Trial Burn and Risk Report, November 1998

Cond Description:
Trial burn, max waste feed and prod rate, max comb temp, min APCS


Cond Description:
Trial burn; DRE, min comb temp, max comb gas flow


Content:
Stack gas metals, PCDD/F, other organics, PSD


Report Name/Date:
B-824 Trial Burn Report and Risk Burn Report, March 13, 1998


Cond Description:
Trial burn, DRE, min comb temp and max stack gas flow


Cond Description:
Risk burn, max liq waste feed rate, normal comb temp


Report Name/Date:
Test Report for Trial Burns on the Thimet/ Counter Incinerators at the American Cyanamid Facility in Hannibal, Missouri, Prepared by MRI, Project No. 9353-L(02), August 9, 1989

Cond Description:
Trial burn, ORGANICS SPIKED INTO SOLID/LIQUID WASTE


Report Name/Date:
Retest Trial Burn on the Thimet/Counter (Trane/Brule) Incinerators at the American Cyanamid Facility in Hannibal, Missouri, MRI Project No. 9353-L-03, September 20, 1989

Cond Description:
Trial burn retest, ORGANICS SPIKED INTO SOLID/LIQUID WASTE


Report Name/Date:
Dioxin/Furan Emission Test Results for Incinerators C, B, and D, MRI Project No. 4435, August 13, 1996


Report Name/Date:
Report of RCRA Trial Burn Results for a Fluidized Bed Incinerator, Prepared for Amoco Oil Company, Whiting, Indiana, Prepared by Scott Environmental Technology Inc. June 1989

Cond Description:
Trial burn, HIGH WASTE FEED/HIGH COMB TEMP


Cond Description:
Trial burn, LOW WASTE FEED/LOW COMB TEMP


Report Name/Date:
Dow Chemical Trial Burn Report for Rotary Kiln, Prepared by Dow Chemical, Plaquemine, Louisiana, February 10, 1998


Report Name/Date:
Metals Trial Burn, Tennessee Eastman's No. 1 Rotary Kiln, Tennessee Eastman Company, August 30, 1991


Report Name/Date:
Mini-Trial Burn Report for Rotary Kiln Incinerator No. 1, March 2002

Cond Description:
Trial burn, max metals, ash, chlorine, min temp


Cond Description:
Trial burn, organics testing, min combustion temp, SCC not operated


Report Name/Date:
Trial Burn Report for Tennessee Eastman Company B-248 Incineration Facility, Tennessee Eastman Company, Eastman Road, P.O. Box 511, Kingsport TN 37662, Submitted to Tennessee Division of Solid Waste Management, April 1989

Cond Description:
Trial burn, max feedrates, all permit conditions set during testing


Cond Description:
General trash feed, no permit limits set


Report Name/Date:
Metals Trial Burn, Tennessee Eastman's No. 1 Liquid Chemical Destructor, Tennessee Eastman Company, August 30, 1991


Report Name/Date:
Performance Test Report for Liquid Chemical Destructor. August 2000


Cond Description:
Trial burn, max operating conditions, permit limit setting test cond


Report Name/Date:
Source Emission Survey, Fina Oil, Laporte, TX, File No. 98-203, December 1998

Content:
PM, HCl/Cl2, CO; metals, chlorine, and ash in feeds


Report Name/Date:
Risk Assessment Trial Burn Report, Dec. 29, 1997


Report Prepared:
Westvaco Chemical Division, Deridder, LA facility

Content:
Non D/F organics (no PM, chlorine, metals, volatiles, semi-vol, TOC)


D/F Rating Comments:
Assume normal ESP operating temp; older data


Report Name/Date:
Recertification of Compliance Test Report


Report Name/Date:
Certification of Compliance Boiler 3 Institute Plant, August 1998

Content:
PM, CO, HCl/Cl2, Tier lll metals (As, Cr)


Report Name/Date:
Source Emissions Survey of Exxon Plastics C Boiler Stack, Baton Rouge, LA, July 1997, File 97-103


Report Name/Date:
Trial Burn Test Report, Pennwalt Corporation, Isotron 142b Incinerator, Thorofare, New Jersey, June 1989, Volume 1 of 2, prepared by PEI Associates, Inc.


Report Name/Date:
GE PCB Trial Burn Report, General Electric Company Silicone Products Division Rotary Kiln Incinerator, Waterford, New York, Prepared by GE, March 18, 1994


Report Name/Date:
Trial Burn Testing Results at Rotary Kiln Incinerator under maximum heat duty, v.1, Oct 1991

Cond Description:
Trial burn, maximum heat duty, maximum flow, minimum temperature, maximum ash, chlorine and metals feed.

Content:
PM, HCl/Cl2, CO, HC, Metals, Hexavalent Chromium, SVOC, VOC, D/F


Report Name/Date:
Report on Supplemental Trial Burn Testing, March 1996

Cond Description:
Supplemental trial burn to verify certain aspects of performance compliance.

Content:
PM, HCl/Cl2, CO, HC, Metals, Hexavalent Chromium


Report Name/Date:
Risk Burn Report, No. 7 Boiler, March 1998

Content:
Stack testing: D/F, PM, PM PSD, HCl/Cl2, CO, VOC/SVOC;  No stack testing for metals (has Tier IA limits and metals feeds) or DRE


Report Name/Date:
Source Emission Survey BASF Corp. NOEL Boiler Stack (EPN 5-5-08) Trial Burn, no date listed (Risk Burn also included)

Cond Description:
Trial burn; Wastewater and HDO Heavies Waste Feeds

Content:
Monochlorobenzene DRE; PM/CO/Chlorine Stack Emissions; Ash/Metals/Chlorine Feed Analysis


Content:
PM/CO/Chlorine Stack Emissions; Ash/Metals/Chlorine Feed Analysis


Content:
Metals, aldehydes/ketones, dioxins/furans, SVOCs, total organics, VOCs as stack emissions


Report Name/Date:
BASF Corp. DRE Trial Burn Report, March 1998, Rev. 2

Content:
DRE, PM, HCl/Cl2, CO; metals, chlorine, ash feeds


Report Name/Date:
Risk Burn Report Amines Boiler, Number 6 Utility Boiler, March 1998

Cond Description:
Risk burn, worst case op cond (max temp, feedrates, prod rates)

Content:
PM, chlorine, D/F, organics (metals in feedstream only)


Cond Description:
Risk burn; worst case (max temp., feedrates, production rates)


Report Name/Date:
Periodic Recertification of Compliance Boiler No. 4 Monsanto Company Port Plastics Plant, December 1994

Cond Description:
CoC; max feed Bldg. 30 spent monomer and resimene distillate


Cond Description:
CoC; max feed Bldg. 9 spent monomer and resimene distillate


Report Name/Date:
Compliance Recertification for Bayer's Boiler No. 4 Pursuant to the BIF Regulations; November 1997 Doc No 4690-047-400


Report Name/Date:
FTB-400 Trial Burn and Risk Burn Report, August 11 and 12, 1998

Cond Description:
Trial burn, max prod rate, min APCS, thermal capacity, max waste feed rate


Report Name/Date:
B-902 Trial Burn and Risk Burn Report, October 9 and 12, 1998

Cond Description:
Trial burn, max waste feed rate, max comb gas velocity


Cond Description:
Risk burn, slightly above normal operating conditions


Report Name/Date:
F-2AB Trial Burn Report and Risk Burn Report, September 2, 1998

Cond Description:
Trial burn, min comb temp and max velocity


Cond Description:
Risk burn, slightly above normal liq waste feed rate, normal comb temp


Report Name/Date:
F-2A/B Certificate of Compliance Burn, April 1997


Report Name/Date:
F-210 Trial Burn and Risk Burn Report, July 13 and 15, 1998

Cond Description:
Trial burn, max waste feed rate, max ash and Cr


Cond Description:
Trial burn, DRE min comb temp, max stack gas flow rate


Cond Description:
Risk burn, above normal feed of liq waste, normal comb temp


Report Name/Date:
F-11 Trial Burn and Risk Burn Reports, September 25, 1998

Cond Description:
Trial burn, max waste feed rate and comb temp, min APCS


Cond Description:
Trial burn, DRE, min comb temp and max comb gas velocity


Cond Description:
Risk burn, above normal liq waste feed rate, normal comb temp


Report Name/Date:
F-820AB Trial Burn Report, September 2, 1998

Cond Description:
Trial burn, max feed rate, max comb temp and max comb gas flow, min APCS


Report Name/Date:
F-820AB Second Trial Burn Report and Risk Burn Report, December 9, 1998

Cond Description:
Trial burn, high capacity, max prod, max feed

Content:
PM, HCl/Cl2, Cr+6, CO (testing only on F 820B)


Cond Description:
Risk burn, slightly above normal conditions


Report Name/Date:
Trail Burn Report For The Dow Chemical Company Manufacturing Services Halogen Acid Furnace; Volume 1 of 5, January 2000


Content:
PM, HCl/Cl2, metals, Cr+6, organics, PCDD/F


Report Name/Date:
Source Emissions Survey of DuPont Dow Elastomers, HCl Recovery Unit Stack Risk Burn, April 1997, File Number 97-17A


Report Name/Date:
Source Emissions Survey of DuPont Dow Elastomers, HCl Recovery Unit Stack Permit Burn, April 1997, File Number 97-17

Content:
DRE, PM, Cr (HCl/Cl2 testing performed, but results later considered invalid due to analytical difficulties)


Report Name/Date:
Source Emissions Survey of DuPont Dow Elastomers Halogen Acid Furnace Stack, September 1997, File Number 97-240A


Report Name/Date:
Trial Burn Report for Texas Eastman Hydrochloric Acid Recovery Unit, October 22, 1998

Cond Description:
Trial burn, worst case for organics destruction

Content:
PM, CO, HCl/Cl2, POHC DRE, PCDD/PCDF, other organics


Report Name/Date:
BIF Certification of Compliance for Eastman Chemical Co, Texas Eastman Division, September, 1996

Cl Rating Comments:
NE; only considering most recent compliance test campaign

PM Rating Comments:
NE; only considering most recent compliance test campaign


Report Name/Date:
Georgia Gulf, Industrial Furnace DRE Trial Burn Report Volume I, June 1998, EMI Proj No. 98-8045


Report Name/Date:
Compliance Test Report, Georgia Gulf, April 25-26 and July 10, 1995

Report Prepared:
Environmental Science and Engineering, Inc.


Report Name/Date:
Confirmation of Trial Burn Test Report for Georgia Gulf Industrial Acid Furnace, March 12-14, 1990

Cond Description:
Trial burn -- Heavy liquid and wet/dry vent streams

Content:
PM, HCl/Cl2, DRE, CO, complete waste feed analysis


Report Name/Date:
Biennial RCRA Trial Burn and BIF Certification of Compliance Test Report Regeneration Unit Number 4, January 1997

Cond Description:
Trial burn/CoC; max haz waste feed rate, Cl, metal, max comb temp

Content:
PM, CO, HCl/Cl2, Tier lll metals, PCDD/F, DRE for POHC (CCl4)


Cond Description:
Trial burn/CoC; max POHC spiking, min comb temp and O2

Content:
PM, CO, HCl/Cl2, PCDD/F , DRE for POHCs (MCB, CCl4, TCB)


Report Name/Date:
BIF Revised Certification of Compliance for Hazardous Waste Boiler Operation, April 1996

Cond Description:
CoC, max feed, flow, and prod rate, max temp


Cond Description:
CoC, max feed and flowrate, min pressure drop


Report Name/Date:
Source Emissions Survey of First Chemical Corp. Hazardous Waste Incinerator Stack, Trial Burn Report, MSD 033417031, Pascagoula, Mississippi July 1991, Metco File Number 90-199


Report Name/Date:
Trial Burn Report of First Chemical Corporation, Noxidizer Incinerator Stack, Pascagoula, Mississippi, Volume I Prepared by METCO Environmental, April 1, 1995


Report Name/Date:
Velsicol Trial Burn Report, Metals Emissions, Velsicol Chemical Corp, Memphis, Tennessee, DCN 90-274-018-04, prepared by Radian, February 20, 1990


Report Name/Date:
Certification of Compliance Boilers #15 and #25, August 1998

SVM Rating Comments:
Pb Tier I, not in stack gas, Cd only in stack gas


Report Name/Date:
Certification of Compliance Boilers 4 and 5, July 1999; Boiler 5 Trial Burn Report, Volume I of VII, August 1999

Cond Description:
CoC/trial burn, max liquid waste feed, max prod rate

Content:
PM, HCl, Cl2, and Cr+6, DRE (toluene and chlorobenzene)


Content:
PCDD/F, other organics, particle size distribution


Report Name/Date:
Revised Certification of Compliance, November 1996


Content:
CO, D/F, PCB, PAH, VOC/SVOC, Aldehydes/ketones


Report Name/Date:
Revised Certification of Compliance, January 1999


# Old flags

SVM Rating Comments:
Spiked Pb; made Pb and Cd stack gas; Tier I for Pb and Cd

DF Rating Comments:
Many unquantifiable factors affect D/F emissions for coal fired boilers; Conducted under max desired ESP oper temp, data in lieu


PM Rating Comments:
Run 2 had outlier PM level of > 0.10; not used

Cl Rating Comments:
no reported chlorine spiking, but Tier III


PM Rating Comments:
PM Emissions exceeded current RCRA standard


PM Rating Comments:
Used to establish operating limits?  Assume N


LVM SRE Rating Comments:
Assume LVM  not controlled, set SRE to 0


SVM Rating Comments:
Run 3 not used in cond avg since ESP went off line

LVM Rating Comments:
Run 3 not used in cond avg since ESP went off-line


LVM Rating Comments:
Not evaluated: No arsenic emissions data


DF Rating Comments:
Not evaluated: not burning hazardous waste


PM Rating Comments:
Not evaluated: not burning hazardous waste


Cl Rating Comments:
NE - system was later modified to add carbon inj

Cl SRE Rating Comments:
NE - system was later modified to add carbon inj

LVM Rating Comments:
NE - carbon injection system not used, old APCS


PM Rating Comments:
Not evaluated: failed Run 1 (> 0.08 gr/dscf)

Cl Rating Comments:
Source 403 currently represents this kiln for metals/chlorine


SVM Rating Comments:
Data from source 403 represents current emissions from this kiln for metals

SVM SRE Rating Comments:
Data from source 403 represents current performance of this kiln for metals

LVM Rating Comments:
Data from source 403 currently represents this kilns emissions

LVM SRE Rating Comments:
Data from source 403 currently represents this kilns emissions


PM Rating Comments:
Tests assumed to be same campaign; 93 test added new mode of operation

Hg Rating Comments:
Tests considered to be the same campaign; recent test added new mode of operation


PM Rating Comments:
Tests assumed to be same campaign; 95 test added new mode of operation


LVM Rating Comments:
Assumed metals not spiked and operating limits not established

LVM SRE Rating Comments:
Assumed metals not spiked and operating limits not established


PM Rating Comments:
Tests assumed to be same campaign; 00 test added new mode of operation


PM Rating Comments:
NE - unclear if mini-burn was used to establish operating limits


PM Rating Comments:
Both 00 and 01 tests assumed to be same campaign; 00 test added new mode of operation

LVM Rating Comments:
Assumed no spiking and that risk burn reflected normal ops even though emissions were higher than previous compliance test


SVM Rating Comments:
NE - failed PM test, negative SVM SRE?, no Cd emission data


SVM Rating Comments:
NE - failed PM test, no Cd emission data


SVM Rating Comments:
NE - no Cd emission data, negative SVM SRE?


PM Rating Comments:
Not evaluated: failed run 1 (> 0.08 gr/dscf)


LVM Rating Comments:
Not evaluated: pre-BIF Rule data; no Be emissions data


LVM SRE Rating Comments:
Not evaluated: pre-BIF Rule data; SRE based on As and Cr only


SVM Rating Comments:
NE - Did not pass RCRA limits for Pb, Cd

SVM SRE Rating Comments:
NE - Did not pass RCRA limits for Pb, Cd


PM Rating Comments:
Tests assumed to be same campaign; more recent test added new mode of operation


SVM SRE Rating Comments:
assumed normal for Pb, no cd emission data


Cl Rating Comments:
Run 1 is high outlier and not included in cond avg


DF Rating Comments:
No temperature profile information available


Cl Rating Comments:
Not evaluated: not burning hazardous waste

Hg Rating Comments:
Not evaluated: not burning hazardous waste

SVM Rating Comments:
Not evaluated: not burning hazardous waste

SVM SRE Rating Comments:
Not evaluated: not burning hazardous waste

LVM Rating Comments:
Not evaluated: not burning hazardous waste

LVM SRE Rating Comments:
Not evaluated: not burning hazardous waste


DF Rating Comments:
Copper spiked to maximize potential for D/F formation.  Is there a Cu feedrate limit?


DF Rating Comments:
Not evaluated: report indicated metals spiking interferred with combustion efficiency


LVM Rating Comments:
Run 2 Cr emission outlier, not used in cond avg


LVM Rating Comments:
Run 3 Cr emission outlier, not used in cond avg


DF Rating Comments:
NE- Research testing, D/F retest at lower FF temperature


SVM Rating Comments:
Unusually high SVM level in HW, likely due to unreported spike contribution?

LVM Rating Comments:
High LVM level in HW, likely from unreported spike contribution


PM Rating Comments:
Data from 473 represents this kilns current emissions


SVM Rating Comments:
Data from source 473 represents current emissions from this kiln

SVM SRE Rating Comments:
Data from source 473 represents current performance of this kiln

LVM Rating Comments:
No Cr emissions.  Also data from source 473 currently represents this kiln

LVM SRE Rating Comments:
Data from source 473 currently represents this kiln


PM Rating Comments:
Not evaluated: failed run 4 (>0.08 gr/dscf)


LVM Rating Comments:
Carbon injection system not used, old APCS

LVM SRE Rating Comments:
Carbon injection system not used, old APCS


SVM Rating Comments:
NE - metals tested for evaluation purposes only

SVM SRE Rating Comments:
NE - metals tested for evaluation purposes only

LVM Rating Comments:
NE- assumed metals tested for evaluation purposes only

LVM SRE Rating Comments:
NE- assumed metals tested for evaluation purposes only


DF Rating Comments:
Assumed normal because of low temp DRE condition


Cl Rating Comments:
All considered same campaign; adding different modes of operation


PM Rating Comments:
Preliminary Test-assumed OPLs were not established

Cl Rating Comments:
NE-Preliminary test; assumed OPLs were not established

LVM Rating Comments:
Preliminary test; OPLs were not established

LVM SRE Rating Comments:
Preliminary test; OPLs were not established


SVM Rating Comments:
Feedrate extrapolation used to set limit

LVM Rating Comments:
Feedrate extrapolation used to set limit

LVM SRE Rating Comments:
Feedrate extrapolation used to set limit


PM Rating Comments:
Not evaluated: failed Run 2 (<0.08 gr/dscf)


Hg Rating Comments:
All tests considered to be the same campaign; recent test added new mode of operation


PM Rating Comments:
NE - miniburn - unknown if OPLs established as result of test

Ash SRE Rating Comments:
NE - miniburn - unknown if OPLs established as result of test


SVM Rating Comments:
Data from source 307 represents this kiln

LVM Rating Comments:
Data from source 307 represents this kiln, no Be data


SVM Rating Comments:
Not evaluated: not burning hazardous waste during test; data in lieu kiln

LVM Rating Comments:
Not evaluated: not burning hazardous waste during test


PM Rating Comments:
Data for source 300 represents current emissions

Cl Rating Comments:
Data for source 300 currently represents this kiln

Hg Rating Comments:
Data from source 300 represents current emissions from this kiln

SVM Rating Comments:
Data from source 300 currently represents this kiln

SVM SRE Rating Comments:
Data from source 300 currently represents current performance of this kiln

LVM Rating Comments:
Data from source 300 represents this kiln

LVM SRE Rating Comments:
Data from source 300 represents this kiln


SVM SRE Rating Comments:
Assumed normal for lead/no Cd emission data


PM Rating Comments:
Assumed risk burn conducted at normal conditions

Cl Rating Comments:
Assumed risk burn conducted at normal conditions


PM Rating Comments:
PM emissions exceeded current RCRA standard


SVM Rating Comments:
Assumed OPLs were established as result of test


PM Rating Comments:
Data for source 200 represents this kilns current emissions

Cl Rating Comments:
Data for source 200 currently represents this kiln

Hg Rating Comments:
Data from source 200 represents current emissions from this kiln

SVM Rating Comments:
Data from source 200 currently represents this kiln

LVM Rating Comments:
Data from source 200 currently represents this kiln


SVM SRE Rating Comments:
Assumed normal for Cd, No Pb emission data


Cl SRE Rating Comments:
Chlorine not controlled, no APCD, SRE set to 0


Cl Rating Comments:
R1 not reported; sample train leak check failure


Cl Rating Comments:
Chlorine spiked for chlorine feed limit for setting Tier III metals limits


LVM SRE Rating Comments:
Cr measurement only in stack gas, LVM not controlled, SRE set to 0


PM Rating Comments:
NE; only considering most recent compliance test campaign

Cl Rating Comments:
NE; only considering most recent compliance test campaign


SVM SRE Rating Comments:
assumed normal for Cd, no lead emission data


SVM Rating Comments:
Pb Tier I, not in stack gas, Cd only in stack gas


# Source Information

Combustor Characteristics:
Firetube boiler. Refractory lined furnace, firetube multi-pass boiler, 235 psig steam, 40 MMBtu/hr

APCS Characteristics:
(HCl absorber, Cl2 wet scrubber);  Water in HCl absorber, caustic sodium hydroxide in Cl2 scrubber


APCS Characteristics:
Quench, HCl absorber, Cl2 wet scrubber.Water in HCl absorber, caustic sodium hydroxide in Cl2 scrubber

Hazardous Wastes Description:
Liquid/gaseous wastes (propylene dichloride plant wastes, crude PDC)


APCS Characteristics:
Quench, HCl absorber, Cl2 wet scrubber .Water in HCl absorber, caustic sodium hydroxide in Cl2 scrubber

Hazardous Wastes Description:
Chlorinated methanes plant liquid wastes


Facility Name:
Rhodia (formerly Rhone-Poulenc Basic Chemical Co.)


APCS Characteristics:
Waste heat boiler, quench tower, scrubbing tower

Hazardous Wastes Description:
Heavy byproducts of perchloroethylene production

Permitting Status:
Currently permitted as incinerator; permit renewal planned as BIF HAF


Combustor Characteristics:
Cleaver Brooks Model CB 600-800, 800 HP (33.5 MMBtu/hr input, 26.8 MMBtu/hr output), firetube design, steam @ 150 psig, 4 pass furnace tube

Hazardous Wastes Description:
Distillate light end waste byproducts (vinyl acetate, methanol, methyl acetate)


Permitting Status:
Tier I metals, chlorine, low risk waste exemption (no PM compliance)


Combustor Characteristics:
Watertube boiler. Babcock and Wilcox BL-702, front wall fired (6 burners in 2 rows), drum Sterling tube design, steam prod at 156,000 lb/hr @ 260 psig and 527°F

Soot Blowing:
Yes; 4 times per day, 10 min in duration (C1R2 has sootblowing)

Permitting Status:
Tier I metals, chlorine (testing for Cr+6/Cr, Cl2/HCl split)


Facility Name:
Sun Company, Inc. (R & M) Frankford Plant

Soot Blowing:
Yes; 3 times per day, 10 min in duration (C1R2 has sootblowing)


Permitting Status:
Tier I for Hg, Ag, Tl, Sb, and Ba; Tier III for Pb, As, Be, Cd, Cr, Se, Ni


Hazardous Wastes Description:
Liq organic wastes (inc. lube oil, HMD oil, VAMT, ADN/LBW, CMC tails), some with chlorinated organics


Permitting Status:
Tier I for metals, Cl (except Cr+6 Tier III)


Combustor Characteristics:
Firetube boiler, Johnston Boiler Company, horizontal-fired combustion chamber, made by John Zink Company, capacity 42 MMBtu/hr, operated @ 1760C

APCS Characteristics:
(Quench, acid absorber, ejector venturi, chlorine packed scrubber)  Inorganic reducing agent used in chlorine scrubber

Hazardous Wastes Description:
Liquid wastes (Vinyl Heavies, PDC bottoms)

Permitting Status:
Tier l for all metals expect Tier lll for Cr+6 (Pb is Tier I even though stack gas testing measurements were taken)


Permitting Status:
Tier l for metals (expect Tier lll for Cr+6), Tier III for Pb?


Combustor Characteristics:
Firetube boiler made by Johnston Boiler Company, horizontal direct fired comb chamber by John Zink Company, 50.2 MMBtu/hr, operated @ 1700oC

APCS Characteristics:
(Venturi scrubber, quench, HCl absorber, venturi scrubber, chlorine scrubber)  Chlorine scrubber uses inorganic reducing agent to capture chlorine

Permitting Status:
Tier l for all chlorine and all metals except Cr+6 (Tier III)


Combustor Characteristics:
Firetube boiler, Johnston Boiler Company, horizontal fired combustion chamber, T-Thermal, capacity of 40 MMBtu/hr, operated @ 1530C, soot blowing used

APCS Characteristics:
Venturi scrubber, acid scrubber (T-2820) uses caustic

Permitting Status:
Tier l for all metals (except Tier III for Cr+6)


Combustor Characteristics:
Watertube boiler. Combustion Engineering Type V-60. Designed to co-fire gaseous fuels with supplemental firing of liquid residues. Equiped with four liquid burners. Produces 300000 lb/hr superheated steam and 250000 lb/hr fuel gas @ 650, 750oF and 50% liquid firing, 441 MM Btu/hr.

Hazardous Wastes Description:
The various organic residue fuels (Propionic Acid Heads, 2-Ethylhexanoic Acid Heads and Ethanol)


Combustor Characteristics:
Cleaver-Brooks Model D52 watertube boiler, John Zink LoNOx burner LN-HIV-30; 30.3 MMBtu/hr heat input, 25,000 lb/hr steam production @ 125 psig, rotary soot blower

Permitting Status:
Adjusted Tier I for all BIF metals and chlorine/chlorides


Combustor Characteristics:
38.5 MM Btu/hr capacity with 32,000 lb/hr steam @ 125 psig


Combustor Characteristics:
Babcock & Wilcox, 600,000 lbs/hr of 750 psig steam, 6 burners

Hazardous Wastes Description:
Liquid waste byproducts (D001, D018, & "LLF")


Combustor Characteristics:
Hot oil heater, John Zink, 25 MM Btu/hr, steam atomized burners, Ljunstrom air preheater

Soot Blowing:
Yes (during test run #3 of test condition 1)

Hazardous Wastes Description:
BDO from tank 57637, gamma butyrolactone (GBL) lights, T-640 overheads, and R-311 tetrahydofuran reactor purge


Combustor Characteristics:
Hot oil heater, 138 MM Btu/hr with Ljunstrom combustion air preheater


Combustor Characteristics:
Steam Boilers - Babcock & Wilcox units, built in 1943; Rated @ 594 MMBtu/hr with 495,000 lb/hr steam @ 500 psig and 563 F


Unit ID Name:
PO/MTBE steam generator # 1 (H-K2-001) (Propylene oxide/methyl tertiary butyl ether

Combustor Characteristics:
Watertube package boiler. Foster Wheeler AG-5175-XMRW, 225 MMBtu/hr, 175,000 lb/hr steam @ 500 psig and 563 F

Hazardous Wastes Description:
HW liquids (ignitable, D001) fed up to 12,022 lb/hr, steam atomized at 150 psig


Unit ID Name:
PO/MTBE steam generator # 2 (H-K2-002) (Propylene oxide/methyl tertiary butyl ether

Other Sister Sources:
Sister to Unit # 1 (H-K2-001) - identical


Combustor Characteristics:
Henry Vogt Model B-16700 steam boiler, 300 MM Btu/hr at 210,000 lb/hr steam @ 600 psig and 750 F

Hazardous Wastes Description:
Liquid ignitable (D001) and reactive (D003) wastes, plus spent non-halogenated solvents (F003 and D018) and process gas

Permitting Status:
Adjusted Tier I for metals and chlorine/chloride feed limits


Combustor Characteristics:
McKee Furnace, horizontal, cylindrical comb chamber, 50 ft l, 16 ft diam, 130 MMBtu/hr, preheated comb air and oxygen Deltak water tube boiler, 62000 lb/hr steam @ 600 psig and 680F

APCS Characteristics:
Waste heat boiler, quench tower, drying tower, SO3 converter, absorbing tower, SO2 scrubber and high-efficiency mist eliminator)

Permitting Status:
Adjusted Tier I for Sb, Ba, Pb, Hg, Ag, & Tl; Tier III for As, Be, Cd, & Cr and chlorine/chloride emission limits


Facility Name:
Eastman Chemicals Co. - Arkansas Eastman Div

Combustor Characteristics:
Watertube boiler (stoker), stoker setup,

Permitting Status:
BIF Interim Status Tier III for 4 metals (As, Be, Cr, Pb)/HCl/Cl2 and Tier 1A for remaining metals (failed to meet 99.99% DRE, but will retest by end of 1999)


Combustor Characteristics:
Spent acid & sulfur as feedstock; HWs & NG for heat input

APCS Characteristics:
Waste heat boiler (firetube), quench tower, contact cooler, wet ESP, drying tower, SO2/SO3 converter, SO3 absorber, and mist eliminator


Facility Name:
Eastman Chemicals Co. - Tennessee Eastman Div

Combustor Characteristics:
Babcock & Wilcox, coal-fired watertube spreader-stoker, 196 MM Btu/hr, comb chamber dimensions (ft): 18 w, 17 l, 40 h, 600 psig steam

APCS Characteristics:
Research Cottrell, 2 fields; 11,232 ft2 plate area for 135 kacfm @ 450 F, SCA=83 ft2/kacfm

Permitting Status:
BIF Interim Status Tier III for metals and chlorine


Combustor Characteristics:
Babcock & Wilcox, coal-fired spreader stoker watertube boiler, 216 MM Btu/hr, comb chamber dimensions (ft): 24 w, 16 l, 40 h

APCS Characteristics:
Research Cottrell, 2 fields; 11,232 ft2 plate area for 118 kacfm @ 350 F, SCA=95 ft2/kacfm

Permitting Status:
BIF Interim Status Tier III for metals, HCl/Cl2


Other Sister Sources:
None (Phase II ID No. 1014 (boiler No. 10) is identical unit but was tested)

Combustor Characteristics:
Manufactured by Combustion Engineering, Model No. VU-40. Water tube, pulverized coal, corner t-fired, steam generating boiler. 750,000 lbs/hr steam capacity, 740 MMBtu/hr

APCS Characteristics:
Baghouse, Joy Manufacturing Co, Model 77-023-02, 10 compartments w/ teflon finish filters, effective area 198,720 sq ft.

Hazardous Wastes Description:
Organic acids and solvent wastes, e.g., long-chain carboxylic acids, ketones, esters

Permitting Status:
Tier IA for ash, chlorides, and metals, except Tier III for Cr


Other Sister Sources:
None (Boiler No. 9 (Phase II ID No. 1013) is identical but was tested separately)

Combustor Characteristics:
Manufactured by Combustion Engineering, Model No. VU-40. Water tube, pulverized coal, corner t-fired, steam generating boiler. 750,000 lbs/hr capacity

APCS Characteristics:
Baghouse - 10 compartments w/ teflon finnish filters, effective area 198,720 sq ft.

Hazardous Wastes Description:
Organic acids and solvent wastes, include but not limited to long-chain carboxylic acids, ketones, esters

Permitting Status:
Tier III  - Cr; Tier IA - other metals and chlorine


Combustor Type:
Liquid injection, process heater (hot oil heater)


Hazardous Wastes Description:
DCP Waste Feed, WWTB Waste Feed, Caustic Feed, Process Water


Hazardous Wastes Description:
Waste liquid fuels and combined PA residues


Combustor Characteristics:
John Zink co-fired boiler; "D" shape w/ superheater; Rated: 60,000 lb/hr steam. Watertube boiler.

Soot Blowing:
Yes, typically 6 times/day w/ a duration of 0.0486 hrs per event

Hazardous Wastes Description:
Liquid waste w/ FuelSolv FS850 (ash modifier)

Permitting Status:
All metals (exception of Cr) Adjusted Tier I; Cr is managed under Tier III.


APCS Characteristics:
Fabric filter, Fuller, reverse air, graphite impregnated fabric bag cloth, A/C = 4


Combustor Characteristics:
Watertube boiler. Anderson 2000 A-type package boiler, installed 1991, 190 MMBtu/hr, 130,000 lb/hr superheated steam @ 900 psig

Hazardous Wastes Description:
Liquid wastes - Distillation bottom tars from the production of phenol/acetone from cumene (K022)

Permitting Status:
Tier l metals expect Cr+6, Tier lll for Cl, Cr+6


Combustor Characteristics:
John Zink side fired combustor capable of burning liquid hazardous waste, vent gases and auxiliary fuel. Also, designed to provide waste heat recovery as steam and acid recovery.

APCS Characteristics:
Waste heat boiler, 2 stages of scrubber, primary (3 packed beds), secondary

Hazardous Wastes Description:
Light and heavy ends from chlorinated hydrocarbon production

Permitting Status:
Tier IA for all metals (metals stack gas measurements made for information purposes only), Tier III HCl/Cl2


APCS Characteristics:
Minimum power limit to ESP of 119 kW, Western Precipitation ESP, 4 fields in 2 compartments, 220 SCA, 72360 ft2 plate area

Permitting Status:
Tier I for Hg, Ba, Sb, Ag, and Tl;  Tier III for As, Be, Cd, Cr, Pb


APCS Characteristics:
4 ESPs in parallel, 20 fields, SCA = 675


APCS Characteristics:
Walther ESP, 100,0000 ft2 plate area (SAC=350), mechanical rapping, SCA = 570 (design)

Permitting Status:
Tier I for Hg, Ag, Tl, Sb, and Ba; Tier III for Pb, As, Be, Cd, and Cr


APCS Characteristics:
2 4-field ESPs, 100,000 ft2 plate area, SCA = 580


Combustor Characteristics:
Kiln: 12.5' diameter, 24' long.  Afterburner used.

APCS Characteristics:
Spray dryer, fabric filter (teflon coated bags, 45,000 ft2 cloth area, 4.5 A/C), packed tower (Raschig rings, 1800 gpm liquor)


APCS Characteristics:
Spray dryer, fabric filter (Teflon fabric, A/C = 4.5, 15,000 ft2 cloth area), packed tower (Rachig ring packing, 4 ft packing depth, 600 gpm caustic liquor)


APCS Characteristics:
Spray dryer, fabric filter, packed bed scrubber;  Fabric filter: Teflon bags, A/C 4.5, 15,000 ft2 bag area.  PBS: 600 pgm liquid, 1" Raschig ring packing, 4 ft depth.


Other Sister Sources:
Old kiln arrangement, Train I not included in testing

Combustor Characteristics:
Old kiln arrangement, Train I not included in testing.  ID No. 609 is current full system

APCS Characteristics:
Spray saturator, packed bed, venturi scrubber


Combustor Characteristics:
Rotary Kiln, Secondary Combustion Chamber, Waste Heat Boiler.  5 steam atomized liquid waste nozzles on front kiln wall

APCS Characteristics:
Waste Heat Boiler/Spray Dryer/Carbon Injection/3-field dry Electrostatic Precipitator with electric impulse rapping/Quench/2-section Packed Bed Scrubber with venturi and mist eliminators.  ESP: Environmental Elements, 750 mADC seconary current, rigid electrode design, automatic controller for spark rate or secondary volatage limit, sized for a dust loading of 12.2 gr/dscf.  Packed bed scrubber and venturi Ring Jet, dp 28 in H2O. Carbon injection added afer first trial burn.

Hazardous Wastes Description:
High Btu and Organic Lance Fed Wastes (Aqueous, Sludge and Slurry Lance Fed Wastes not burned in this test), Drum Wastes, Crane Fed Bulk Wastes


Hazardous Wastes Description:
Solid haz waste and tires fired in mid-kiln hatch


Other Sister Sources:
Boiler 31H4 (identical) Testing was done on one boiler; unclear which one

Combustor Characteristics:
3 chamber John Zink forced draft furnace, produces 184,000 lb/hr of steam @ 1,250 psig (1.8 trillion Btu/yr)

Hazardous Wastes Description:
By-product hydrogen cyanide (HCN) from Acrylonitrile process


Other Sister Sources:
Sister to Boiler 30H5 (identical) Testing was done on one boiler; unclear which one


APCS Characteristics:
5 compartments, 2 fields/compartment, 54,000 ft2 plate area, Research Cottrell, 360 SCA

Hazardous Wastes Description:
Containerized solids mid kiln for Kiln 1

Permitting Status:
Tier I for Hg, Ag, Tl, Sb, Ba; Tier III for Pb, As, Be, Cd, Cr


Unit ID Name:
Reynolds Potliner thermal treatment process

Combustor Characteristics:
2 rotary kilns with a common afterburner

APCS Characteristics:
Dry scrubber, fabric filter, Afterburner. Afterburner is natural gas fired and operates at 1750 - 1800 °F with a residence time of 2 seconds.

Hazardous Wastes Description:
Potliner mixture - having from spent aluminum potliner; landfill leachate

Permitting Status:
Tier I for all metals except Tier III for arsenic, beryllium, and chromium (test 1), chlorine (test 2)


Unit ID Name:
Unit 1 & 2 (both units have common stack and APCD)

Combustor Characteristics:
Thermal Research horizontally fired incinerator capable of burning liquid hazardous waste, vent gases and auxiliary fuel.

APCS Characteristics:
3 stages of scrubber: rapid quench primary, secondary (alkaline), tertiary


Combustor Class:
Onsite incinerator, DoD government, chem demil

APCS Characteristics:
Quench, venturi scrubber, packed bed, demister, cyclone, afterburner


Facility Name:
TOCDF Desert Army Depot (Tooele Army Depot South)

APCS Characteristics:
Quench tower, venturi scrubber, packed bed scrubber, demister


Facility Name:
Deseret Army Depot TOCDF (Tooele Army Depot South)

APCS Characteristics:
Water quench, venturi scrubber, packed bed scrubber, demister


APCS Characteristics:
Quench, counter-current scrubber, two cross flow scrubbers, three stage ionizing wet scrubber


Hazardous Wastes Description:
Wastewater treatment sludge, organic liquid solvents


Combustor Class:
Onsite incinerator, DoD munitions popping, government

Combustor Characteristics:
Designed to ignite the ammunition items and effectively incinerate reactive components from the metal shells. Equiped with a Hauck 783 proportioning burner located at the discharge end. The burner has a turndown ratio of 4:1. Operated at 800-1100F and slight negative pressure.

APCS Characteristics:
Cyclone has a 90-95% removal efficiency for particles 10 microns or larger. Afterburner is built by Southern Technology Inc, designed to raise the temperature of the exhaust gases from the kiln. High temperature cast ceramic filters bahouse which is built by JT Systems Inc.

Permitting Status:
Tier II for Sb, Ba, Cr  and tier III for Pb


Combustor Characteristics:
2 chamber incinerator, made by Sunbeam Equipment Corp, Model A-50, primary and secondary chambers, looks like controlled air design

APCS Characteristics:
Waste heat boiler, Anderson 2000 variable throat venturi scruber with cyclone separator and mist eliminator

Hazardous Wastes Description:
Liquid waste solvents, resin and paint particles


Facility Name:
Clean Harbors Environmental Services, Inc.

Combustor Characteristics:
Fluidized bed incinerator. Equiped with four wastes feeding. Including primary comb chamber, SRC and a pre-quench chamber.

APCS Characteristics:
Heat exchanger recuperator, spray dryer absorber, activated carbon injected, fabric filter.


Combustor Characteristics:
Designed to incinerate a max processing rate of 2080 lb/hr of obsolete and ammunition and bulk explosives. Single burner assembly.

APCS Characteristics:
Spray dryer (ME-104) and baghouse (ME-105 A,B,C), absorber

Hazardous Wastes Description:
Explosive munitions (M96), M30 propellant, inert materials


Combustor Characteristics:
Rotary kiln. Desgined to destroy small ammunition or explosive end items and bulk explosive or propelling materials. Consist of waste feed monitoring system, afterburner, dual conveyor feed system. Equiped with a variable speed drive ranging from 0.5-4.5 rpm.

APCS Characteristics:
Afterburner, gas coolers, cyclone, fabric filter, bypass damper.  Gas coolers are designated the high and low temp heat exchange. The baghouse are silicone treated, heat set, and flameproofed. Bags are made by Tetratec Corp.

Permitting Status:
Tier I for all metals; Tier III for Cr, Pb, Cd


Combustor Characteristics:
Brand new rotary kiln replacing old unit ID No. 334

APCS Characteristics:
Venturi quench, wet ESP, subcooler, M1 scrubber

Hazardous Wastes Description:
Aqueous non-fuel-grade POHC mixture, POHC mixture liquid.

Permitting Status:
Tier I for all metals except Pb (tier III)


Combustor Characteristics:
A gas-fired heater utilizing a mobile floor for ease of charging the furnace. It is used for treatment and decontamination of large, unsual and packaging materials. Max temp expected 1800oC


Combustor Characteristics:
The MHI is a eighth hearth unit manufactured by Envirotech.The sludge is fed to hearth 1 by a screw conveyor system. Drying of the feed occurs on hearths 1 and 2. Combustion takes place on hearth levels 3-5. Ash cools down on levels 6-7 and is discharged from the bottom of the unit.The residence time for the waste at maximum feed is about one hour. Flue gas leaving the MHI is routed to a Secondary Combustion Chamber (SCC) for organics destruction

APCS Characteristics:
Quench, packed bed scrubber/absorber, variable throat venturi scrubber, wet electrostatic precipitator

Hazardous Wastes Description:
Sludge is obtained from a wastewater purification plant and consists of insoluble solids removed by dedimentation in the primary clarifiers, and excess sludge, produced during the biological treatment stage.


Hazardous Wastes Description:
By-product of the manufacture of synthetic resin. Consisting of "waters of reaction"


Combustor Characteristics:
Vertically-fired liquid injection incinerator. Model No. AVS-1600 installed in 1988

APCS Characteristics:
Quench, venturi scrubber. CHEAF to enhance PM removal. Packed bed tower reduces the HCl emissions by treating the effluent gas with caustic soda solution.

Hazardous Wastes Description:
Water spent solvent generated during the manufacuring process which are not amenable to recovery or re-use.

Permitting Status:
Tier I for all metal except Hg, As, Cr (tier III)


APCS Characteristics:
Newly installed FF; ESP used during older test conditions


Facility Name:
General Electric Company, Silicones Products Division

Combustor Characteristics:
Liquid injection incinerator manufactured by Bigelow Liptak Co. The incinerator chamber is a refractory/insulation system encased by a steel outer shell and has a volume of 3640 cubic feet. The construction is suitable for chamber temperatures of 2300 °F

APCS Characteristics:
Quench Chamber, Packed Column Scrubber, Two-stage Ionizing Wet Scrubber (A cross-tie duct enables some of the flue gas from Incinerator #2 to routed through the APCS of Incinerator #1). Incinerator  #1 was turned off during the trial burn.

Hazardous Wastes Description:
Non Polar Solvents: Primarily toluene 45-65%, HV-14900 Btu/lb, Cl < 0.3%, Si~5.4%.  POHC Mixture:Mixture of NPS Waste, carbon Tetrachloride, and chlorobenzene.  Acid Polor Solvents: Liquid mixture of water, HCl and polar solvents, HV < 100 Btu/lb, Cl~5.8%, Si~1.4%, Spiked with As, Be, Cr.  Waste Slurry:Mixture of chlorinated silanes and silicon powder, HV < 10,000 btu/lb, Cl~30%, Si~25%.  Vent Gases: Gases from process vents and wastewater stripper unit


Hazardous Wastes Description:
Aqueous liquids, solvents, sludges, solids


Combustor Characteristics:
Two chamber natural gas fired incinerator. Burning Li, Na, and Mg. Operating at 1500oF

APCS Characteristics:
Quench, venturi scrubber, fiber bed filter

Hazardous Wastes Description:
Sodium dichromate dihydrate, lead acetate trihydrate and mercuric oxide


Combustor Characteristics:
A liquid injection incinerator, has two chamber, horizontally fired, refractory lined combustion chamber. Model TO-097001 maufactured by the John Zinc Company. Operated in the range of 1015-1150oC.

APCS Characteristics:
Quench, packed bed water scrubber, vertical packed bed caustic scrubber

Hazardous Wastes Description:
Carbonyl Chloride Production and Carbon Tetrachloride Removal processes. L/M PSA organics

Permitting Status:
Tier I for all metals except Cr+6 (tier III)


APCS Characteristics:
Quench pot, air cooled heat exchanger/condenser/demistor, fiberglass filter mist eliminator


Other Sister Sources:
VCM HCIN 2 Incinerator (identical, data in lieu)

Combustor Characteristics:
BIGELOW-LIPTAK custom design, comb chamber w/waste heat fire tube boiler

APCS Characteristics:
Water quench, packed bed, 2 spray columns, knockout pot (WQ/PB are for recovery of 10% HCl)


Other Sister Sources:
Sister unit to VCM HCIN 3 Incinerator (3028)


Combustor Type:
Semi-dry, short, preheater, precalciner, in-line raw mill (ILRM)

APCS Characteristics:
ESP made by Southern, 10 fields; FF membrane filter, with cloth area 22,055 ft2, Combined main / bypass single stack


Combustor Type:
Dry, preheater, precalciner, inline raw mill (ILRM)

APCS Characteristics:
Main fabric filter made by Buell, A/C = 2, 32 compartments, 173,000 ft2 bag area


Other Sister Sources:
4 kilns; only 2 can burn at any one time


Combustor Class:
Onsite Incinerator, DoD munitions popping, government

Combustor Characteristics:
Rotary kiln. Desgined to destroy small ammunition or explosive end items and bulk explosive or propelling materials.


Combustor Characteristics:
Constructed in 1998-1999. Water tube-type boiler manufactured by Foster-Wheeler. The BIF unit is a multi-fuel wall boiler with four front burners. Ther boiler will be rated for a maximum heat release of 400 MMBTU/hr. Maximum liquid rate feedrate is 9,260 lbs/hr. It will produce 308,000 lbs/hr of 650 psi team at 540-580°F.

Hazardous Wastes Description:
Biphenol acetone (BPA) heavy ends, phenol heavy ends (K022)


Combustor Characteristics:
The heater was manufactured by Struthers-Wells (SW) of Warren, PA in 1969 and is designed as Model No. 5C15-4. Vertical fired cold chamber heater. The original economizer  was added in 1980 and was also built by SW. A second economizer (also made by SW) was added in July 1996. . Thermal rating output is 7.5x10^6 Btu/hr. The combustion chamber and primary energy recovery section are of integral design. Thermal recovery is at least 60 percent and at least 75 percent of the recoverd energy is ultilized at the facility

Hazardous Wastes Description:
Polyester or direct solvation distillate (byproduct)


Combustor Characteristics:
Kiln #1 manufactured by Traylor is 175 ft long, Kiln #2 manufactured by Allis Chalmers is 180 ft long. Both kilns have an OD of 11 ft, and consist of steel shell lined with a 6" refractory brick giving an ID of 10 ft. The flame zone extends 30 ft from burner end of the kiln. The flame zone gas temperatures are maintained at 2000-3500°F.

APCS Characteristics:
Heat exchanger, Multiclone, fabric filter, venturi scrubber (fixed throat), mist eliminator

Hazardous Wastes Description:
Liquid low grade fuels (LLGF), Solid low grade fuel (SLGF). SLGF was not fed for Risk burn phase II. The raw material was shale


APCS Characteristics:
BHA, Quench system (air and water).  Baghouse (reverse air cleaning, 580 bags, cloth area = 29,155 ft2, net air to cloth ratio = 2.23:1, design operating temp < 450 °F at inlet), fiberglass cloth material

Hazardous Wastes Description:
The raw material was excavated from the Virginia Solite quarry


APCS Characteristics:
Quench system (air and water).  Baghouse (reverse air cleaning, 580 bags, cloth area = 29,155 ft2, net air to cloth ratio = 2.23:1, design operating temp < 450 °F at inlet), fiberglass bag material


APCS Characteristics:
Water quench lance, Fabric filter, 29,000 ft2 bag area, A/C = 2, fiberglass bag material

Permitting Status:
Tier III for As, Be, Cd, Cr, Pb; Tier I for Hg, Sb, Ba, Ag, Tl


APCS Characteristics:
Water quench, fabric filter, BHA, 29,000 ft2 bag area, fiberglass bags

Hazardous Wastes Description:
The raw material was excavated from the Solite Arvonia quarry


Other Sister Sources:
Kiln Nos. 2, 3, 4 (only 2 kilns can burn at any one time)

APCS Characteristics:
Western Precipitation ESP, 70,000 ft plate area, SCA = 430


APCS Characteristics:
American Air Filter ESP, 4 fields, SCA = 1000, each field has 153,000 ft2 plate area, max power of 75 kVA at 1200 mA, use of shale with high oil content causes opacity problems, ESP about 15 years old, uses automatic power controller to limit sparking and maximize power input


APCS Characteristics:
Plate area = 78,000 ft2, SCA = 400, 3 fields


APCS Characteristics:
78,000 ft2 plate area, 3 fields, SCA = 400


Combustor Characteristics:
Rotary kiln, afterburner. Six different waste feed streams can be fed in, most of the waste streams are fed to the kiln; only aqueous and liquid blend are fed to the afterburner.  Kiln has 14' diameter, 40' long

APCS Characteristics:
Spray dryer, carbon injection, fabric filter, 2 stage wet scrubber, wet ESP.  Procedaire spray dryer / FF, pulse jet, A/C = 3, 42,000 ft2 fabric area, Teflon coated fiberglass bags, Intolox saddle packing; Anderson 2000 packed tower, Tellerette packing; Beltran wet ESP, 9600 ft2 plate area. Carbon injection added around 1994, however, not currently in use.


APCS Characteristics:
Ionizing wet scrubber, 3 stages in parallel, 2 packed towers in series?


Combustor Characteristics:
Rotary kiln, afterburner, made by PYROX, kiln has 8' diameter, 35' long


Other Sister Sources:
Currently a sister kiln of kiln No. 2 (311)

APCS Characteristics:
Quench system (air and water).  Baghouse (reverse air cleaning, 580 bags, cloth area = 29,155 ft2, net air to cloth ratio = 2.23:1, design operating temp < 450 °F at inlet)


Combustor Characteristics:
Rotary kiln, afterburner.  Kiln has 14.5' diameter, 40' length.  Afterburner: 21 ft wide, 24 ft high.


APCS Characteristics:
Carbon added upstream of wet scrubber, downstream of ESP.  2-stage wet scrubber

Hazardous Wastes Description:
Waste H2O sludge, MCB/MEA/polyol liquids


Combustor Characteristics:
Designed by Kennedy Van Saun of Danville, PA. Model no. HR-75. Solid waste ram feeder and a dual fuel liquid injection burner.  Primary chamber is 6.5' x 16.5'.  Secondary combustor is 6.5' x 14'3.5''.  900 lb/hr capacity

APCS Characteristics:
Fabric filter, heat exchanger, dry lime injection/absorption. Interell scrubber.  Pulse jet FF with felted polyacryl bag material, 3875 ft2 bag are, A/C = 3.6.  HEPA and carbon adsorption also used at one time

Hazardous Wastes Description:
Animal bedding, reject pharmaceuticals, labpacks of off-spec or reject chemicals, chemically contaminated lab supplies, HPLC and scintiallation vials that contain solvents and products or lab packed waste.

Permitting Status:
Tier I for all metals except arsenic, cadmium, hexavalent chromium (tier III)


Combustor Characteristics:
Rotary kiln, afterburner.  Kiln: 5.5' diameter, 12' long.  Made by C&H Combustion.

APCS Characteristics:
Waste heat boiler, quench, scrubber, venturi scrubber, demister.  Ceilcote packed tower, 16' height, 2" Tellerette packing


Facility Name:
Johnston Atoll Chemical Agent Disposal System (JACADS)

Combustor Class:
Onsite Incinerator, DoD government, Chem Demil

Combustor Characteristics:
Liquid injection incinerator made by T-Thermal (4' diameter, 12' high), with afterburner, LV-14 Vortex burner

APCS Characteristics:
Water quench, venturi scrubber, packed bed scrubber, demister.  Variable throat venturi scrubber, packed bed with steel ring packing


Combustor Class:
Onsite Incinerator, DoD government, chem demil

Combustor Characteristics:
Deactivation furnace system.  Rotary kiln/heated discharge conveyor/cyclone/afterburner

APCS Characteristics:
Quench tower, venturi scrubber (variable throat), packed bed scrubber, demister vessel

Hazardous Wastes Description:
Explosive components from chemical weapons (fuses, explosives, propellants)


Facility Name:
Deseret Army Depot, TOCDF, DEPARTMENT OF THE ARMY - SOUTH

APCS Characteristics:
Cyclone, quench, variable throat venturi, packed bed scrubber, demister

Hazardous Wastes Description:
Chemical weapon nerve agent decontamination


Combustor Characteristics:
Liquid Injection, Carbon steel shell w/ high temperature refractory lining. 12' 8" OD x 21' tall, Internal Volume=1017 ft3.

APCS Characteristics:
Quench Chamber, Absorber/Condensor, Two Stage Ionizing Wet Scrubber.

Hazardous Wastes Description:
Liquid Organics: Taft NAPL blended w/ 1,2 dichlorobenzene,1,2,4-trichlorobenzene, and tetrachlroethane.  Aqueous Liquid Waste: Durez waste blended w/ phenol


Facility Name:
Alliant Ammunition and Powder Company LLC

Combustor Characteristics:
Barlett Snow Model 7A is designed to incinerate water based slurries of bulk explosives and propellant The kiln shell is a carbon steel cylinder. The shell is refractory line with 6 inc of firebrick, which runs the entire length of the kiln. The inside refractory diameter is 5 ft across. The kiln also consists of a barrel which rotates between two fixed breeching equipped with a North American Burner, Series 6514.  6.5' OD, 12' long

APCS Characteristics:
Gas pre-cooler, fabric filter (Gore-tex bags, Zurn pulsed jet, 2300 ft2 fabric area, A/C = 3), evaporative cooler, packed bed scrubber (3" Interlox PP saddle packing, 3' packing), afterburner

Permitting Status:
Tier I for all metal except Pb and Cr (Tier III)


Combustor Characteristics:
Rotary kiln, afterburner.  Kiln has 14' diameter, 60' long

APCS Characteristics:
Quench, Acid Scrubber, Venturi Scrubber, Demister, Ionizing Wet Scrubber (Ceilcote, 2 stages)


Combustor Class:
Onsite incinerator, government, mixed waste

Combustor Characteristics:
Rotary kiln, afterburner, International Waste Energy Systems, kiln is 6' diameter, 25' long

APCS Characteristics:
Quench, venturi scrubber, packed bed scrubber, ionizing wet scrubber (2 in series)

Hazardous Wastes Description:
Radioactive (mixed) liquid, sludge, solid wastes, PCBs


Combustor Characteristics:
Kiln, afterburner.  Kiln has 7.5' diameter, 20' long.  18 MM Btu/hr.  Progressive Equipment manufacturer.

APCS Characteristics:
Waste heat boiler (firetube design), fabric filter (Mikro-Pulsaire, Goretex cloth, 3000 ft2 bag area, A/C = 4), scrubber (Ceilcote Model STT-241, 183 gpm liquid, NaOH scrubber solution)


APCS Characteristics:
SCA = 230, 4 fields, about 20 years old, rebuilt a few years ago


APCS Characteristics:
SCA = 580, 4 fields, 20 years old, recently rebuilt to meet 0.04 gr/dscf


Facility Name:
FMC Corporation, Agriculture Products Group

Combustor Characteristics:
Incinerator made by Universal Oil Products

APCS Characteristics:
Rapid Quench, Packed Tower Scrubber, Wet ESP (Dresser Industries)

Hazardous Wastes Description:
Liquid organic waste, tar, wastewater, vent gas.  Liquid Organics: Methallyl Chloride (MAC) heels, Methanol solvent, Sulfenttrazone.  Vent Gas: MAC, TMOA, Sulfentrazone


Combustor Characteristics:
A pressurized, down-fired unit, has a single vertical combustion chamber. Designed to burn about 21 gp, of organic and aqueous liq wastes and 7800 scfm natural gas.

APCS Characteristics:
Venturi scrubber, SO2 scrubber, separator, quench, packed bed

Hazardous Wastes Description:
Aqueous and liq organic genearated from onsite processes

Permitting Status:
Tier I for all metals except As, Pb, Cr, Cd (tier III)


Combustor Characteristics:
3 chamber roller hearth unit, afterburner

APCS Characteristics:
Water quench, venturi scrubber (variable throat), packed bed scrubber, demister

Hazardous Wastes Description:
Halogenated plastic wastes (personal protective equipment, neoprene, teflon), 4.2" HD mortar projectiles


Combustor Characteristics:
Counter current rotary kiln manufactured by Vulcan. Aggregate process rate 10 tons/hr. 9' ID Shell x 125' long.  Burner consists of a 3/4 "fuel pipe and a 4" atomizing air pipe. Solids retention time = 1.25 to 2.5 hours. Gas outlet temperature = 850 -1200 °F.

APCS Characteristics:
Quench system (air and water).   Baghouse (reverse air cleaning, 580 bags, cloth area = 29,155 ft2, net air to cloth ratio = 2.23:1, design operating temp < 450 °F at inlet), BHA manuf., fiberglass bags


APCS Characteristics:
Quench, packed tower, venturi scubber (Calvert fixed throat), demister


APCS Characteristics:
Quench, scrubber (Calvert fixed throat dual venturi), demister, water separator


Combustor Characteristics:
Kiln: 12' diameter, 40' long, with afterburner


APCS Characteristics:
Waste heat boiler, quench, venturi scrubber (John Zink variable throat venturi), demister


APCS Characteristics:
Quench, packed tower, entrainment separator


Combustor Characteristics:
Rotary kiln, old kiln / system arragement, does not include testing with Train II

APCS Characteristics:
Spray saturator, packed tower, venturi, demister


Combustor Characteristics:
Old kiln / APCS arrangement.  APCS / kiln Train I not used

APCS Characteristics:
Spray saturator, packed bed, venturi scrubber, demister


APCS Characteristics:
Spray saturator, venturi scrubber, packed bed scrubber, venturi scrubber.  Ring-jet venturi scrubbers, heat exchanger used to sub-cool scrubber solution


Other Sister Sources:
None (other unit # 300 Kiln No. 1 shares a stack)

APCS Characteristics:
Research Cottrell, 54,000 ft2 plate area


Facility Name:
Eastman Chemical Company, Longview Texas

APCS Characteristics:
Heat exchanger, venturi, packed bed, demisters

Hazardous Wastes Description:
Various hi-Btu (10-20 kBtu/lb) low ash (<1%) liquid waste & biological wastewater treatment sludge


Facility Name:
TOCDF, Deseret Army Depot, DEPARTMENT OF THE ARMY - South


Facility Name:
Deseret Army Depot, TOCDF, Department of Army South

Combustor Class:
Onsite incinerator, government, DoD Chem Demil

APCS Characteristics:
Cyclone, quench, venturi scrubber, packed bed scrubber, demister


Combustor Characteristics:
Rotary Kiln/Secondary Combustion Chamber/Waste Heat Boiler

APCS Characteristics:
electrostatic precipitator/induced draft fan,quench tank, packed tower wet scrubber, stack

Hazardous Wastes Description:
clean-up solvents, off-specification products and raw materials from paint and resin manufacture


Combustor Class:
Onsite Incinerator, government, munitions popping

Combustor Characteristics:
Rotary kiln (30 ft long, 30 in ID), afterburner

APCS Characteristics:
High temperature heat exchanger (800F), low temperature heat exchanger (300F), cyclone, fabric filter (2 compartments, 1,414 ft2 / compartment, A/C 4.5:1, Nomex fabric, pulse jet cleaning), after burner.

Hazardous Wastes Description:
Off-specification or obsolete ammunitions and explosive wastes

Permitting Status:
Tier III for Sb, As, Ba, Be, Cd, Cr, Pb, Hg, Ag, Tl


Combustor Characteristics:
Manufactured by MAN-GHH. Model 2MOF29646-G1-RN. Designed to handle numerous waste streams in various combinations.

APCS Characteristics:
Quench, absorber, ionizing wet scrubbers (manufactured by Ceilcote, 4 stages of ionizing wet scrubbers), afterburner, carbon bed absorber (Donau Carbon), waste heat boiler.  IWS and carbon bed added recently (2000 testing)

Hazardous Wastes Description:
Glycol PDC Bottoms (D-460), Allyl PDC Crude (D-450)


Combustor Characteristics:
Rotary kiln with secondary combustion chamber, 14' diameter

APCS Characteristics:
Quench tower, absorber, 4-stage IWS w/cooling tower

Hazardous Wastes Description:
Bulk & containerzied solids; sludge; energetic, organic & aqueous liquids

Permitting Status:
RCRA & TSCA, Tier III metals -- As, Be, Cd, Cr, Pb


Combustor Characteristics:
3 combustion chamber, low-NOx via recycled flue gas burning

APCS Characteristics:
Spray contactor/quench tank, hydrosonics 2-stage venturi scrubber,  mist eliminator

Hazardous Wastes Description:
Aniline and mononitrobenzene (MNB) process liquid wastes


Combustor Characteristics:
Composed of two trains that exhaust to a common stack. Train I is a 3.6-meter diameter rotary kiln and an afterburner which has a gas residence time of 2 seconds or more. Train II has a 4.4-meter diamter rotary kiln and a rotary reactor that feed gases in to an after burner.

APCS Characteristics:
Saturator which provides a rapid quench to less than 200F gas temperature, dual packed tower condensors,and a high energy-impact Calvert venturi scrubber.

Hazardous Wastes Description:
Liq wastes (RCRA BLD T27/28, RCRA BLD V110, direct burn, TOx stream and PCB BLD T131). Solid wastes (RCRA repack, rotary reactor bulk solids and reburn ash)


Facility Name:
Norco Chemical Plant-West Site Shell Oil Company

Combustor Characteristics:
Designed and built by Bieglow-Liptak Corp. Equiped with a mason premix pilot with a Hauck spark ignitor. This burner is also equiped with a natural gas firing system and six liquid waste injection guns NCIN-2 is an induced draft organic choloride incinerator consisting of a combustion chamber, flue gas cooler, and scrubbing train. Induced draft blower is 16000 acfm at 90oF and 20 inc W.C. vacuum. Discharge pressure is 2 inc. W.C. Powered by a 150 hp electric motor

APCS Characteristics:
Waste heat boiler, water quench, acid absorber, caustic scrubber.  The system was designed by Shell Oil Company and manufactured by various suppliers

Hazardous Wastes Description:
Allyl Chloride Heavy Ends (ACHE) which is a waste stream produced on site.


APCS Characteristics:
Spray dryer, fabric filter (Pulseflo, pulse jet, fiberglass bags), lime spray dryer


Facility Name:
Eastman Chemical Company, Longview, Texas

Combustor Characteristics:
Rotary kiln, afterburner, International Inc., 10' diameter, 35' long

APCS Characteristics:
Waste heat boiler, water quench, free jet scrubber (Hydrosonics fixed throat), packed bed scrubber


Combustor Characteristics:
BIGELOW-LIPTAK custom design combustion chamber with a waste heat boiler

APCS Characteristics:
Waste heat boiler, water quench, packed bed, 2 spray columns, knockout pot (WQ/PB are for recovery of 10% HCl)

Hazardous Wastes Description:
VCM heavy ends, VCM light ends, EDC heavy ends


Combustor Characteristics:
Nichols Monohearth, with afterburner, 40 MM Btu/hr

APCS Characteristics:
Spray dryer, cyclone,reverse jet scrubber, venturi scrubber (variable throat, Andersen 2000 model WAV-152), packed bed scrubber (counter current baffle style, 3 stage, disc / donut packing) (Andersen 2000 design)

Hazardous Wastes Description:
Liquid organic Waste, metal spike, Jug A (Fuel oil #2), Jug B (Pb Spike), Newspaper, Wood Chips


Combustor Characteristics:
McGill Americans, Inc., custom designed, horizontal, forced draft incinerator

APCS Characteristics:
Venturi scrubber, packed bed, wet electrostatic precipitator. Calvert Collision Scrubber with a maximum design pressure drop of 90 inches WC, vertical Packed Column Scrubber, followed by a Beltran Model 4x4 wet tubular electrostatic precipitator.

Hazardous Wastes Description:
Aqueous flammable waste (AFW) and special flammable waste (SFW) generated during the manufacturing of pharmaceuticals and other health products.


Hazardous Wastes Description:
T-911, T-105 residue wastes, organic liq wastes

Permitting Status:
Tier I for all metals except Cr (tier III)


Facility Name:
Lyondell Lake Charles Plant Incinerator (formerly Arco/Olin)


Combustor Characteristics:
Combustion Engineering, coal-fired spreader stoker watertube boiler, 501 MMBtu/hr, comb chamber dimensions (ft): 33 w, 19 l, 40 h

APCS Characteristics:
Buell, 2 fields; 24,000 ft2 plate area for 240 kacfm @ 380 F, SCA=100 ft2/kacfm


Facility Name:
Celanese Ltd., Chemical Group Clear Lake Plant


Combustor Characteristics:
Watertube boiler. C-E Type VU-60 rated at 350,000 lb/hr steam @ 650 psig and 750F; Ljungstrum regeneration air preheater; 4 natural gas burners and 4 liquid waste nozzles; one boiler performs as a BIF at any time, other either idled or burning natural gas and process vent gases for steam production as a regular boiler

Hazardous Wastes Description:
V-1041 (Vinyl Acetate Unit's waste organics) and V-683 (combined OXO Units' liquid waste); at times may also carry D018 (benzene) and D035 (methyl ethyl ketone)


Combustor Characteristics:
Nebraska Boiler Company (series WTS), 55,000 lb/hr of 240 psig, 68.5 MMBtu/hr; extended fire-box, single North America low NOx burner.

APCS Characteristics:
Quench, wet scrubber, candlefilter-type mist eliminator (appears wet scrubber not operated during either testing.   5 tray, 2 stage scrubber/adsorber, CECO candlefilter-type mist eliminator

Hazardous Wastes Description:
Liquid chemical wastes, residue, liquid waste, nap fuel

Permitting Status:
Tier III - As, Cr, Pb; Tier IA - Sb, Ba, Be, Cd, Hg, Ag, & chlorine


APCS Characteristics:
Quench tower, packed tower, venturi scrubber


Facility Name:
Dow Chemical U.S.A. Allyn's Point Facility

Combustor Characteristics:
Boiler -- Downtherm process heater. Vertically-fired cold boiler, Dowtherm liquid heat exchanger, capacity of 9.0 MMBtu/hr input (8.0 MMBtu/hr output)

Hazardous Wastes Description:
Liquid and solid wastes (polystyrene, recycle process products), mostly ignitable (D001)


Combustor Characteristics:
Boiler -- Downtherm process heater. 9.0 MM Btu/hr, Dowtherm heater

Hazardous Wastes Description:
Liquid waste -- ignitable (D001) and benzene (D018)

Permitting Status:
Tier I for metals and chlorine, LRWE PM waiver


Combustor Characteristics:
Boiler -- Dowtherm process heater. 9.75 MM Btu/hr, Struthers Wells, 1979, Model No. 7CV 19-6PH, heats Dowtherm A liquid

Permitting Status:
Tier I metals and chlorine; Low Risk Waste Exemption (no PM, DRE for trial burn)


Combustor Characteristics:
Watertube boiler, manufactured by Murray Iron Works Company, Model No. MCF4-64; thermal input capacity of 91.8 MMBtu/hr; steam production rate of 70000 lb/hr @ 300 psig

Hazardous Wastes Description:
Pyridine and pyrindine-derived organic chemical production waste


Combustor Characteristics:
Watertube boiler. Babcock and Wilcox Company; a type FM; max thermal input of 39.3 MMBtu/hr; max operating pressure of 250 psig, a nameplate steam production rate of 30000 lbs/hr.

Soot Blowing:
Yes, 4 times/day, 5 min/event (run 3, cond 3)


Unit ID Name:
Boiler 28K (**unit is now considered a sister unit to 737 (30K)**)

Other Sister Sources:
This unit is now considered a sister unit to 737 (30K)

Combustor Characteristics:
Watertube boiler. Babcock and Wilcox type FM; max thermal input of 36.8 MMBtu/hr; max operating pressure of 250 psig, steam production rate of 28000 lb/hr

Soot Blowing:
Yes, 4 times/day, 5 minutes/event (run 3, cond 1)


Combustor Characteristics:
Watertube boiler. Combustion Engineering Type 30-A-12, package tube water tube boiler (installed 1971), COEN DAF low NOx burners, 110,000 lb/hr superheated steam @ 524 psig and 600°F

Soot Blowing:
Yes -- 3 times per day, 10 minute each time (cond 1, run 2)


Combustor Characteristics:
Furnace with watertube boiler. John Zink watertube boiler; horizontally mounted circular furnace; 235 MMBtu/hr rated at 175,000 lb/hr steam @ 600 psi and 750 F

Hazardous Wastes Description:
HT-2 EA light ends and HT & HT-2 acetic acid, each liquid wastes; propylene wastes; wastes are ignitable (D001) and/or corrositve (D002); also process gas


Combustor Characteristics:
Watertube boiler. ABB Combustion type 35-A-14, 180000 lb/hr of steam @ 400 psig, frontwall burner, economizer, FGR, 248 MMBtu/hr


Combustor Characteristics:
Firetube boiler. Zurn firetube boiler, 180 MMBtu/hr rated at 144,000 lb/hr steam at 600 psig; multiple gun burner with steam atomizers; mfg'd in '76, upgraded to 2-stage combustion in '89


Other Sister Sources:
None (Boiler No. 30 no longer burns hazardous waste)

Combustor Characteristics:
Watertube boiler. Package watertube boiler, 241 MMBtu/hr, 125000 lb/hr steam, air preheater


Other Sister Sources:
H-2002 Boiler (Used only when H-002 is shut down, H-2022 is a larger B&W boiler @ 361 MM Btu/hr, 278,000 lb/hr steam @ 300 psig)

Combustor Characteristics:
Babcock & Wilcox, natural gas fired boiler, 162 MMBtu/hr, 125,000 lb/hr steam @ 300 psig

Hazardous Wastes Description:
Liquid, "light residue" organic byproduct from cyclohexanone distillation from caprolactam manufacturing


Combustor Characteristics:
Watertube boiler. Riley Union Type MWH with Todd Combustion low NOx burner, watertube, 268 MM Btu/hr, 200000 lb/hr steam @ 350 psig

Permitting Status:
Low risk waste exemption; Tier I for metals/chlorine


Permitting Status:
Tier IA for metals (except Cr) and chlorine


Permitting Status:
Adjusted Tier I for metals (except Cr) and chlorine


Permitting Status:
Tier I for all metals (spiked ash and chlorine)


Unit ID Name:
Boiler H530A (Unit 1) and Boiler H530B (Unit 2), identical units

Combustor Characteristics:
Watertube boiler. Babcock and Wilcox Model 103-88 boiler, 70,000 lb/hr steam @ 195 psig

Hazardous Wastes Description:
Liquid waste (phenol distillation tar, benzene byproduct)

Permitting Status:
Tier I Adjusted for all metals, chlorine


Soot Blowing:
Not conducted during testing, however is conducted on this boiler.

Hazardous Wastes Description:
Liquid waste byproducts (monomer bottoms)


Other Sister Sources:
Boilers B-101, B-102, B-104, B-105 (all identical units)

Combustor Characteristics:
Watertube boiler. B&W Model FO-27, installed 1961, refractory-lined carbon steel, 100,000 lb/hr steam @ 50 psig, 100 MMBtu/hr heat input

Hazardous Wastes Description:
Liq. wastes with hexane, benzene, isoprene, toluene, etc.


Other Sister Sources:
Sister unit to Boilers B-103, B-102, B-104, B-105 (all identical units)


Other Sister Sources:
Sister unit to Boilers B-101, B-103, B-104, B-105 (all identical units)


Other Sister Sources:
Sister unit to Boilers B-101, B-102, B-103, B-105 (all identical units)


Other Sister Sources:
Sister unit to Boilers B-101, B-102, B-104, B-103 (all identical units)


Combustor Characteristics:
Watertube boiler. A-type package watertube, 30,000 lb/hr steam @ 250 psig, refractory lined combustion chamber, 50 MMBtu/hr

APCS Characteristics:
Air-to-cloth ratio of 4.06:1, fiberglass bags, reverse pulse jet cleaning

Hazardous Wastes Description:
Liquid organic chemicals -- tars, aromatic hydrocarbon and alcohol liquid wastes (methanol, benzene)


Hazardous Wastes Description:
Liquid organic hazardous waste (propylene tetramer, C5's)


Facility Name:
Equistar Chemicals, LP - Channelview Complex

Combustor Characteristics:
Watertube boiler. 230 MMBtu/hr watertube boiler


Combustor Characteristics:
Firetube boiler. John Zink 2-stage combustion boiler, forced draft, with 3 burner guns; 66 MM Btu/hr, 49,000 lb/hr steam with fire-tube heat recovery boiler; part of cooled boiler exhaust is returned to 2nd stage combustor inlet

Hazardous Wastes Description:
Liquid, primarily ester #1 and methanol, classed as D001 and D002;  42-51% ester #1, 10-17% methanol, 11-18% water, 9-22% acetic acid, and < 1% hydrochloric acid; 8.1 lb/gal and 7,100 Btu/lb

Permitting Status:
Tier IA for all metals, except Cr; Tier III for Cr and chlorine


Combustor Characteristics:
Firetube boiler. John Zink 2-stage combustion firetube boiler, forced draft, with 2 burner guns; 26 MM Btu/hr, 19,500 lb/hr steam with fire-tube heat recovery boiler; part of cooled boiler exhaust is returned to 2nd stage combustor inlet

Hazardous Wastes Description:
Liquid, primarily ester #1 and methanol, classed as D001 and D002;  42-51% ester #1, 10-17% methanol, 11-18% water, 9-22% acetic acid, and <1% hydrochloric acid; 8.1 lb/gal and 7,100 Btu/lb

Permitting Status:
Tier IA for all metals, except Cr; Tier III for Cr/HCL/Cl2


Combustor Characteristics:
Watertube boiler. Cleaver-Brooks Model D34 water-tube boiler, John Zink LoNOx burner LN-HIV-25, 18.6 million Btu/hr heat input, 15,000 lb/hr steam production @ 125 psi, rotary soot blower


APCS Characteristics:
Gas cooler, shell and tube heat exchanger, quench column, 3 absorber towers, HCl stripper, 2-stage caustic scrubber

Hazardous Wastes Description:
Vinyl chloride monomer (VCM) and ethylene dichloride process wastes


Combustor Characteristics:
Horizontal fired combustion chamber manufactured by T-Thermal, capacity of 31 MMBtu/hr, operated @ 1700C

APCS Characteristics:
(Dry quench, HCl absorbers, venturi, chlorine wet scrubber)  Dry quench uses steam and condensate?, T-34 chlorine scrubber uses water/caustic and inorganic reducing agent in scrubber liquor

Hazardous Wastes Description:
Liquid wastes (Vinyl Heavies and DC Heavies from EDC and VCM)

Permitting Status:
Tier I for metals except Cr+6 (Tier III) and Cl (Tier III)


Combustor Characteristics:
Vertical fired, open chamber, manufactured by Dow Chemical Proprietary Design, capacity 88 MMBtu/hr, operated @ 1100-1350C, designed to recover MgCl2

APCS Characteristics:
(Venturi scrubber, separator, demister) J-3 Venturi Scrubber, S-3 Separator, and inorganic reducing agent to capture HCl/Cl2. The gas passes through S-30 demister to remove entrained droplets.

Hazardous Wastes Description:
Liquid wastes (Allyl Crude PDC, Trichlor-B-Recycle)


Combustor Type:
Fixed hearth controlled air, liquid injection

Combustor Characteristics:
Brule multi chamber unit, Trane liquid injection, to common APCS

APCS Characteristics:
Quench, separator, venturi, entrainment separator, packed bed scrubber


Combustor Characteristics:
Dorr Oliver unit, 82 MMbtu/hr, constructed in 1972, 22' diameter, 40' height

Hazardous Wastes Description:
API and oily refinery separator sludge, dissolved air flotation unit sludge (biosolids), caustic solutions


APCS Characteristics:
Quench tower, packed bed scrubber, wet electrostatic precipitator


APCS Characteristics:
Quench for gas cooling, rod scrubber for hydrogen chloride absorption, gas subcooling, and two wet electrostatic precipitators.  New APCS for new most recent data.  Old APCD used with old data.

Permitting Status:
Spiked and measured Pb and Cr to fully represent all SVM and LVM


APCS Characteristics:
Quench for gas cooling, rod scrubber for hydrogen chloride absorption, gas subcooling, and two wet electrostatic precipitators.  New APCS for most recent data.  Older data taken with APCS that has been removed.


APCS Characteristics:
Venturi scrubber, variable pressure drop

Hazardous Wastes Description:
2 liquid ignitable wastes: atactic, meeting Tier IA for metals, ash, Cl; and catalyst residue for Tier III; also process vent gases

Permitting Status:
Adjusted Tier I for atactic waste, Tier III for catalyst residue waste


Combustor Characteristics:
Turbulent burner chamber, closed coupled to a watertube waste heat boiler, 30 MMBtu/hr, installed 1985, 25,000 lb/hr steam @ 215 psig.

Hazardous Wastes Description:
TDI LUWA Bottoms, ODCB flush, waste vacuum pump oil


Combustor Characteristics:
Turbulent burner chamber closed coupled to a water tube waste heat 
boiler and economizer, Steam of 25,000 lb/hr @ 350 psig.

Soot Blowing:
During Run 4 of 813C1 there were 6 minutes of Soot Blowing as reported in Section 3.2 of the Aniline II Compliance Trial Burn Report Submitted on December 29, 1997.

APCS Characteristics:
Fabric filter, collected dust high in Ni catalyst, sold as usable product

Hazardous Wastes Description:
Organic liquid wastes from aniline distillation.  Dry purge residue (K083), wet purge residue (K083), reactor residue (D018, D036), reactor vent gas


Combustor Characteristics:
Process heater/boiler. Primary function to superheat a raw material used in production of Diphenylamine. Only a small portion of the total heat input is utilized for steam production.Turbulent burner chamber, separate tube banks

Hazardous Wastes Description:
Liquid wastes -- tar residue, TDA distillation bottoms, DPA light and heavy impurities, vacuum oil, converter and process gases


Combustor Characteristics:
Turbulent burner chamber, separate tube banks. Process Heater/Boiler; Primary function to superheat a raw material
used in Diphenylamine production. Only a small portion of the total heat input is utilized for steam production

Hazardous Wastes Description:
Liquid waste -- TDA distillation bottoms, DPA light and heavy impurities, converter and process gases


Unit ID Name:
Boilers No. 2 and 3 (common ESP and stack)

Other Sister Sources:
None (Boiler No. 4 also shares common ESP and stack but does not burn haz waste)

Combustor Characteristics:
Watertube boilers. Both units identical, Combustion Engineering Stirling type boilers (Model VA-X) with Coen burners, watertube, single wall fired, 60,000 lb/hr steam

Soot Blowing:
Yes, every 8 hrs (6 blowers activated for 15sec each, duration 15 min)

Hazardous Wastes Description:
Resinate filer cake, HC920/spage oil, acrylic process spent organics and overheads

Permitting Status:
Has Low Risk Waste Exemption (no PM/DRE), Tier I for metals/chlorine


Combustor Characteristics:
Watertube boiler. Riley-Stoker design, model P1-31-WW, generating of 150000 lb/hr steam, four burners in front and arranged two by two square.

APCS Characteristics:
2-stage ESP made by Research-Cottrell, Model No. G.O.2981, treat 120000 cfm @ 450F (Mechanical collector and hopper collector not used anymore)

Permitting Status:
Tier lll for metals (As, Cr) and HCl/Cl2; Tier I for other metals


Combustor Characteristics:
Erie City package boiler, built in 1970, 50000 lb/hr steam (450 psig @ 450°F)

Hazardous Wastes Description:
Liquid ignitable (D001), distillation bottoms, vinyl acetate, other HCs, waste oils

Permitting Status:
Tier I for metals; plans to get comparable fuels exemption


APCS Characteristics:
Quench, venturi scrubber, packed tower, demister


Combustor Characteristics:
The incinerator unit features a 35' long x 11' dia. Rotary kiln followed by a secondary combustion chamber. Liquid waste is fed by air atomized waste nozzles. Solid wastes are fed through a drum chute.

APCS Characteristics:
Quench Chamber, Packed Tower Wet Scrubber, Two Parallel Ionizing Wet Scrubbers.

Hazardous Wastes Description:
Non Polar Solvents(NPS): Primarily toluene 45-65%,  Cl < 0.3%, Si~5.4%.  POHC Mixture:Mixture of NPS waste, carbon tetrachloride, and chlorobenzene.  Acid Polor Solvents(APS): Liquid mixture of water, HCl and polar solvents.Cl~5.8%, Si~1.4%.  Waste Slurry:Mixture of chlorinated silanes and silicon powder,Cl~30%, Si~25%.  Poly Waste:High Viscosity Siloxanes. Si ~35%, Cl~0.1%.  Drummed Waste: Contaminated soil and bentonite clay (floor-dry)


Other Sister Sources:
No. 4 Boiler (Burns waste when No. 7 is down (2-6 wks per year))

Combustor Characteristics:
Watertube boiler. Riley Stoker, water tube, forced draft, with superheater and air preheater, built in 1954, steam generating capacity of 110,000 lb/hr (605 psig @ 750°F)

Hazardous Wastes Description:
Liquid NP nitrogenated heads (D001/D002) produced from nitroparaffins

Permitting Status:
Low Risk Waste Exemption; Tier IA for all metals


Combustor Characteristics:
Combustor/waste heat boiler. McGill Envir. 3 zone low NOx combustor (oxidizing chamber, reducing chamber, reoxidation chamber), waste heat boiler, economizer, 9000 lb/hr steam @ 650 psig and 650°F

Hazardous Wastes Description:
Liq ignitable wastes (DOO1) from amines production, methanol (F003), process vent gases, butanediol light ends


Combustor Characteristics:
Watertube boiler. Babcock and Wilcox, D shaped, gas fired watertube field erected boiler with superheater and economizer, 285 MMBtu/hr, 205000 lb/hr steam @ 650 psig and 750°F

Hazardous Wastes Description:
Ignitable (D001), methanol, mixed alcohols, from production of THF and PTHF, butanediol light ends, TDA


Combustor Characteristics:
Watertube boiler. Babcock and Wilcox, D shaped, gas fired watertube field erected boiler with superheater and economizer, 250000 lb/hr steam @ 650 psig and 750°F


Combustor Characteristics:
Watertube boiler. Foster-Wheeler, three firing guns, 48 MMBtu/hr, 35,000 lb/hr steam


Combustor Characteristics:
Firetube boiler, Johnston Boiler Company, horizontal-fired combustion chamber made by John Zink Company, capacity 28 MMBtu/hr, operated @ 1700C

APCS Characteristics:
HCl absorber, chlorine scrubber.  T-401 Chlorine Scrubber, the gases and water are contacted and caustic in scrubbing medium which incorporates an inorganic reducing agent to capture chlorine.

Permitting Status:
Tier lll for Cr+6, Tier l for other metals


Combustor Characteristics:
Watertube boiler. Direct fired combustion chamber, Combusion Engineering, capacity of 229 MMBtu/hr, operated @ 1700-2200F, soot blowing capabilities


Combustor Characteristics:
Cleaver-Brooks firetube boiler, Cleaver-Brooks horizontal direct fired comb chamber, capacity 1600 HP, operated @ 700-1200C

APCS Characteristics:
HCl absorber, chlorine scrubber.  T-72 Chlorine Scrubber, gases contact water and caustic in scrubber medium, inorganic reducing agent used to capture chlorine


Combustor Characteristics:
Firetube boiler made by Johnston company, horizontal direct fired combustion chamber made by John Zink Company, capacity of 50.2 MMBtu/hr

APCS Characteristics:
(Quench and HCl absorber, venturi scrubber, wet scrubber)  Gases contacted with caustic water in an ejector venturi (VE-214) then pass through scrubbing medium in T-214 chlorine scrubber

Hazardous Wastes Description:
Liquid wastes (Epi Heavies, Allyl Tars mix, TCP, BO Heavies)

Permitting Status:
Tier l for metals except Tier lll for Cr+6 and Tier III for Cl and Tier III Pb?


Combustor Characteristics:
Cleaver-Brooks firetube boiler, Cleaver-Brooks horizontal direct fired comb chamber, capacity 23.4 MMBtu/hr, operated @ 700-1200C

APCS Characteristics:
T-20 Chlorine Scrubber, water/caustic liquor

Hazardous Wastes Description:
Liquid waste (Epi Heavies/Lights and BO Heavies)

Permitting Status:
Tier l for metals except Tier lll for Cr+6


Combustor Characteristics:
Firetube boiler. Cleaver-Brooks boiler, horizontal direct fired comb chamber, capacity 32.2 MMBtu/hr, operated @ 1200C

APCS Characteristics:
D-830 Venturi scrubber, caustic used in scrubber liquor, scrubber liquid tank gases passed through also


APCS Characteristics:
Quench, acid absorber, caustic scrubber.  Acid absorber includes two falling-film absorbers and a wetted packed bed column; dilute aqueous NaOH in caustic scrubber

Permitting Status:
Tier I for all metals except As, Cd, and Cr+6 (Tier lll).  Nickel spiked but not Tier III?


Combustor Characteristics:
T-Thermal, liquid injection, down fired, 48 MMBtu/hr, dual parallel units with common APCS

APCS Characteristics:
Water spray quench, 3 stage HCl absorbers, vent scrubber, Dynawave caustic scrubber.  Water used in 3-stage HCl and vent scrubbers; caustic used in Dynawave scrubber

Permitting Status:
HAF operation; Tier III for Cr, HCl, Cl2; Tier I for other metals


Combustor Characteristics:
T-Thermal Model # 5-02-3825-D oxidizer furnace, 30 MMBtu/hr; no energy recovery features; no waste heat boiler.

Soot Blowing:
No, this unit does not have soot blowing capacity

APCS Characteristics:
HCl quench tank / primary absorber / secondary caustic scrubber column;  18-19% HCl product in primary abosrber column, Cl2 and residual HCl removed in the final absorber/scrubber column


Unit ID Name:
IN-662 (Industrial Furnace for VCM and EDC production units)

Combustor Characteristics:
Liquid injection, horizontal fired T-Thermal, 70 MM Btu/hr

APCS Characteristics:
Waste heat boiler, 4-stage HCl absorber, caustic scrubber. Waste heat boiler (single pass horizontal firetube, 240 psig steam, 450°F exit gas), 4 stage HCl absorbers, caustic wet scrubber (packed bed with demister)

Hazardous Wastes Description:
Liquid wastes -- vinyl chlorine monomer light ends (K022, K019)

Permitting Status:
The unit's classification has been changed from incinerator to BIF HAF


APCS Characteristics:
Waste heat boiler, quench tower, gas cooler, wet ESPs, SO2-SO3 converter, Oleum tower, 2 stage absorber scrubbers

Permitting Status:
Tier l metals (Sb, Pb, Hg, Ba, Ag, Tl, Ni, Se); Tier lll metals (As, Be, Cd, Cr+6)


Unit ID Name:
DSSI Mixed Waste Industrial Boiler System

Combustor Class:
Liquid-fired boiler, commercial, mixed waste

Combustor Characteristics:
Firetube boiler. 3-pass dry back Scotch Marine firetube, Superior Boiler Model # 4-X-1758-S200-CF, 1990 installed, 14.7 MM BTU/hr, John Zink burner LN-HIV-30

APCS Characteristics:
Spray dryer, fabric filter, packed bed scrubber, reheater, high efficiency particulate air filter.  Fabric filter -- Gore-Tex cloth filter, 4:1 A/C, 250F; PBS -- 1.8 L/G, NaOH

Hazardous Wastes Description:
Organic chemicals.  Permitted to burn all codes except F020-F027.

Permitting Status:
BIF Tier I: Sb, Ba, Hg, Ag, Tl; Tier III: As, Be, Cd, Cr, Pb, Cl


APCS Characteristics:
quench, venturi scrubber, absorber scrubber, caustic scrubber


Combustor Characteristics:
Watertube boiler, 323 MMBtu/hr, inlet water at 380F, 6 opposed firing burners

Permitting Status:
Tier l : Sb, Ba, Hg, Ag, Pb, Tl; Tier lll : As, Be, Cd, Cr, Cl


Other Sister Sources:
None (Boiler 4 no longer burning hazardous waste)

Combustor Characteristics:
Watertube boiler. Babcox and Wilcox Type FH Integral, 4 liquid burners, 160,000 lb/hr of steam @ 600 psig and 750°F, 200 MMBtu/hr

Hazardous Wastes Description:
Liquid wastes.  Propionic acid heads residue, ethanol residue, hazardous ignitable


Combustor Characteristics:
Watertube boiler. Riley/Union Iron Works, Model MH, 150,000 lb/hr steam, 183 MMBtu/hr

Hazardous Wastes Description:
Liq organic wastes (benzene, waste lubricating oil, AMS distillation bottoms, phenol waste water, aniline distillation) including codes D001, D018, D035, K022


Other Sister Sources:
Sister to Units UA, UC (2 other identical units)

Combustor Characteristics:
Watertube boiler. Riley/Union Iron Works, Model MH, 150,000 lb/hr steam, 190 MMBtu/hr


Other Sister Sources:
Sister to Units UB, UA (2 other identical units)


Combustor Characteristics:
Watertube boiler. Babcock and Wilcox Model FM-117-97C, 150,000 lb/hr steam, 183 MMBtu/hr

Hazardous Wastes Description:
Liquid organic wastes (benzene, waste lubricating oil, phenol waste water, AMS distillation bottoms, etc.) D001, D018 and D035


Combustor Characteristics:
Rotary Kiln Incinerator with afterburner, F.L. Smidth, 12' x 35' long, 120 MMBtu/hr

APCS Characteristics:
Quench, venturi scrubber (Air Pollution Industries, variable throat, up to 80" water drop), variable cyclonic liquid gas separator

Hazardous Wastes Description:
Synthetic packs, wide range of liquids and solids

Permitting Status:
Tier I for all metals except Cr and Pb (Tier III)


# SVM SRE

SVM SRE Comment:
Data from source 403 represents current performance of this kiln for metals


SVM SRE Comment:
NE - Did not pass RCRA limits for Pb, Cd


SVM SRE Comment:
assumed normal for Pb, no cd emission data


SVM SRE Comment:
Not evaluated: not burning hazardous waste


SVM SRE Comment:
Data from source 473 represents current performance of this kiln


SVM SRE Comment:
NE - metals tested for evaluation purposes only


SVM SRE Comment:
Data from source 300 currently represents current performance of this kiln


SVM SRE Comment:
Assumed normal for lead/no Cd emission data


SVM SRE Comment:
Assumed normal for Cd, No Pb emission data


SVM SRE Comment:
assumed normal for Cd, no lead emission data


