Q 

V€OUA 

ONM€NTAL 5€r 

Comprehensive Performance Test Report 

Fixed Hearth Incinerator - Unit 2 

Fixed Hearth Incinerator - Unit 3 

Rotary Kiln Incinerator - Unit 4 

Veolia ES Technical Solutions, LLC . 

7 Mobile Avenue 

Sauget, Illinois 62201 

January 28,2014 
URS 

40 CFR §63 Subpart EEE 

Comprehensive Performance Test Report 

for 

Fixed Hearth Incinerator - Unit 2 

Fixed Hearth Incinerator - Unit 3 

Rotary Kiln Incinerator - Unit 4 

Prepared for: 

Veolia ES Technical Solutions, L.L.C. 

7 Mobile Avenue 

Sauget, IL 62201 

Prepared by: 

URS Corporation 

9400 Amberglen Blvd. 

Austin, TX 78729 

January 28, 2014 

URS Corporation 

940O Amberglen Boulevard 

Austin, TX 78729 

P.O. Box 201088 

Austin, TX 78720-1088 

Tel: 512,454.4797 

Fax: 512.454.8807 

www.urscorp.com 

VES017670 
Table of Contents 

Page 

1.0 Introduction 1-1 

1.1 Incinerator Overview 1-2 

1.2 Test Objectives 1-3 

1.3 Test Protocol Summary 1 -4 

1.4 CPT Schedule 1-9 

1.5 Summary of Results 1-10 

1.6 Report Organization 1-10 

2.0 Process Operations - 2-1 

2.1 Process Overview 2-1 

2.2 Process Operating Data and Waste Feedrates 2-6 

2.2.1 Unit 2 2-6 

2.2.2 Unit 3 2-6 

2.2.3 Unit 4 2-7 

2.3 Spiking of Metals and Chlorine 2-7 

3.0 Sampling, Analysis, and Monitoring Procedures 3-1 

3.1 Sampling Locations and Procedures 3-1 

3.1.1 Liquids Sampling Procedures 3-1 

3.1.2 Solids Sampling Procedures 3-6 

3.1.3 Stack Gas Sampling Procedures 3-6 

3.1.3.1 Sample Port Locations 3-10 

3.1.3.2 EPA Methods 2 and 4 (Flowrate and Moisture) 3-10 

3.1.3.3 EPA Method 5 (PM) 3-10 

3.1.3.4 Modified EPA Method 26A (HC1/C12) 3-11 

3.1.3.5 EPA Method 29 (Metals) 3-11 

3.1.3.6 SW-846 Method 0023A (Dioxins/Furans) 3-12 

3.1.3.7 Continuous Emissions Monitoring (THC, C02, CO and 02 ) 3-13 

3.2 Analysis Procedures 3-13 

3.2.1 Composition and Physical Parameters Analysis 3-14 

3.2.2 Metals Analysis 3-14 

3.2.3 PM Analysis 3-14 

3.2.4 HCI/CI2 Analysis 3-14 

3.2.5 Dioxins/Furans Analysis 3-15 

3.3 Process Monitoring Procedures 3-15 

iii 

VES017671 
Table of Contents (continued) 

Page 

4.0 Results 4-1 

4.1 Waste Feedstreams 4-1 

4.2 Stack Gas 4-18 

4.2.1 PM in Stack Gas 4-18 

4.2.2 HC1/C12 in Stack Gas 4-22 

4.2.3 Metals in Stack Gas 4-26 

4.2.4 Dioxins/Furans in Stack Gas 4-34 

4.2.5 THC in Stack Gas 4-39 

4.3 Chlorine, Ash, and Metals Feedrates 4-41 

4.3.1 Chlorine Feedrates 4-41 

4.3.2 Ash Feedrates 4-41 

4.3.3 Metals Feedrates 4-48 

5.0 Quality Assurance/Quality Control ......... .5-1 

5.1 Audit Samples 5-2 

5.2 Analysis of Waste Feeds 5-2 

5.2.1 Analysis of Waste Feeds for Metals 5-2 

5.2.2 Analysis of Waste Feeds for Physical and Chemical Parameters 5-4 

5.3 Stack Gas 5-5 

5.3.1 Isokinetic Sample Collection 5-5 

5.3.2 Analysis of Stack Gas Samples for Determination of PM 5-6 

5.3.3 Analysis of Stack Gas Samples for Determination of HC1/C13 5-6 

5.3.4 Analysis of Stack Gas Samples for Determination of Metals 5-7 

5.3.5 Analysis of Stack Gas Samples for Determination of Dioxins/Furans 5-8 

5.3.6 Monitoring of Stack Gas for 02, C02, and THC 5-9 

5.4 Process Data 5-9 

5.5 Spiking 5-10 

iv 

VES017672 
List of Appendices 

APPENDIX A - CEMS RATA Reports 

APPENDIX B-Spiking Report 

APPENDIX C-Process Operating Data 

APPENDIX D - CMS Performance Evaluation Test Report 

APPENDIX E - Chains-of-Custody/Field Logbook 

APPENDIX F-Sampling Documentation 

APPENDIX G - Analytical Data Reports 

APPENDED G l - Laboratory Reports - Analysis of Liquid and Solid Waste Feed 

Samples for Metals, Total Chlorine, Ash, and Physical 

Parameters 

APPENDIX G2- Laboratory Reports - Analysis of Stack Samples for 

Dioxins/Furans 

APPENDIX G3 - Laboratory Reports - Analysis of Stack Samples for Metals 

APPENDDX G4 - Laboratory Reports - Analysis of Stack Samples for Particulate 

Matter, Hydrogen Chloride, and Chlorine 

APPENDIX G5 - Laboratory Reports - Analysis of Spike Materials 

APPENDIX G6 - Audit Report 

APPENDIX H - Data Quality Assessments 

APPENDIX I - Sampling Equipment/Instrumentation Calibration Documentation 

v 

VES017673 
List of Tables 

Page 

1-1 Applicable HWC MACT Emission Standards 1-3 

1-2 Data Used To Establish OPLs 1 -8 

1-3 Unit 2 Compliance Summary 1-11 

1- 4 Unit 3 Compliance Summary 1-12 

1 -5 Unit 4 Compliance Summary 1-13 

2- 1 Unit 2 - Summary of Process Data and Feedrates During the EPA Method 5 Stack 

Sampling for PM 2-8 

2-2 Umt 2-Summary of Process Data and Feedrates During the Modified EPA 

Method 26A Stack Sampling for HC1/C12 2-9 

2-3 Unit 2 - Summary of Process Data and Feedrates During the EPA Method 29 Stack 

Sampling for Metals 2-10 

2-4 Unit 2 - Summary of Process Data and Feedrates During the SW-846 MethodOO 23A 

Stack Samphng for Dioxins/Furans 2-11 

2-5 Unit 3 - Summary of Process Data and Feedrates During the EPA Method 5 Stack 

Sampling for PM 2-12 

2-6 Unit 3 - Summary of Process Data and Feedrates During the Modified EPA 

Method 26A Stack Sampling for HC1/C12 2-13 

2-7 Unit 3 - Summary of Process Data and Feedrates During the EPA Method 29 Stack 

Sampling for Metals 2-14 

2-8 Unit 3 - Summary of Process Data and Feedrates During the SW-846 Method 0023A 

Stack Sampling for Dioxins/Furans 2-15 

2-9 Unit 4 - Summary of Process Data and Feedrates During the EPA Method 5 Stack 

Sampling for PM 2-16 

2-10 Unit 4 - Summary of Process Data and Feedrates During the Modified EPA 

Method 26A Stack Sampling for HC1/C12 2-17 

2-11 Unit 4 - Summary of Process Data and Feedrates During the EPA Method 29 Stack 

Samplmg for Metals 2-18 

2-12 Unit 4 - Summary of Process Data and Feedrates During the SW-846 Method 0023A 

Stack Sampling for Dioxins/Furans 2-19 

2-13 Unit 2 - Chlorine Spiking Rates During the HC1/HC12 Stack Sampling 2-20 

2-14 Unit 3 - Chlorine Spiking Rates During the HC1/HC12 Stack Sampling 2-20 

2-15 Unit 4 - Chlorine Spiking Rates During the HC1/HC12 Stack Sampling 2-20 

2-16 Unit 2 - Spiking Rates During the Metals Stack Sampling 2-21 

2-17 Unit 3 - Spiking Rates During the Metals Stack Sampling 2-21 

2-18 Unit 4 - Spiking Rates During the Metals Stack Samphng 2-21 

vi 

VES017674 
List of Tables (continued) 

Page 

2-19 Unit 2 - Analytical Results for the Chromium Spiking Solution 2-22 

2-20 Unit 2 - Analytical Results for the Mercury Spiking Solution 2-22 

2-21 Unit 3 - Analytical Results for the Chromium Spiking Solution 2-23 

2-22 Unit 3 - Analytical Results for the Mercury Spiking Solution 2-23 

2-23 Unit 4 - Analytical Results for the Chromium Spiking Solution 2-24 

2- 24 Unit 4 - Analytical Results for the Mercury Spiking Solution 2-24 

3- 1 Measurement Frequency 3-3 

3-2 Sampling Methods 3-4 

3-3 Unit 2 - Summary of Isokinetic S ampling 3-7 

34 Unit 3 - Summary of Isokinetic Sampling 3-8 

3-5 Unit 4 - Summary of Isokinetic Sampling 3-9 

3- 6 Summary of Analytical Methods 3-13 

4- 1 Unit 2 - Analytical Results for Chlorine, Ash, Metals, and Physical Parameters 

in the Low-Btu Liquid Waste Feed 4-5 

4-2 Unit 2 - Analytical Results for Chlorine, Ash, Metals, and Physical Parameters 

in the High-Btu Liquid Waste Feed 4-6 

4-3 Unit 2 - Analytical Results for Chlorine, Ash, Metals and Physical Parameters 

in the Specialty Liquid Waste Feed 4-7 

4-4 Unit 2 - Analytical Results for Chlorine, Ash, Metals and Physical Parameters 

in the Containerized Solids Waste Feed 4-8 

4-5 Unit 3 - Analytical Results for Chlorine, Ash, Metals, and Physical Parameters 

in the Low-Btu Liquid Waste Feed 4-9 

4-6 Unit 3 - Analytical Results for Chlorine, Ash, Metals, and Physical Parameters 

in the High-Btu Liquid Waste Feed 4-10 

4-7 Unit 3 - Analytical Results for Chlorine, Ash, Metals and Physical Parameters 

in the Specialty Liquid Waste Feed 4-11 

4-8 Unit 3 - Analytical Results for Chlorine, Ash, Metals and Physical Parameters 

in the Containerized Solids Waste Feed 4-12 

vii 

VES017675 
List of Tables (continued) 

Page 

4-9 Unit 4 - Analytical Results for Chlorine, Ash, Metals, and Physical Parameters 

in the Low-Btu Liquid Waste Feed to the Kiln 4-13 

4-10 Unit 4 - Analytical Results for Chlorine, Ash, Metals, and Physical Parameters 

in the High-Btu Liquid Waste Feed to the Kiln 4-14 

4-11 Unit 4 - Analytical Results for Chlorine, Ash, Metals and Physical Parameters 

in the Liquid Waste Feed to the SCC .4-15 

4-12 Unit 4 - Analytical Results for Chlorine, Ash, Metals and Physical Parameters 

in the Containerized Solids Waste Feed 4-16 

4-13 Unit 4 - Analytical Results for Chlorine, Ash, Metals and Physical Parameters 

in the Bulk Solids Waste Feed 4-17 

4-14 Unit 2 - Results of PM in Stack Gas 4-19 

4-15 Unit 3 - Results of PM in Stack Gas 4-21 

4-16 Unit 4 - Results of PM in Stack Gas 4-22 

4-17 Unit 2 - Results of HC1/C12 in Stack Gas 4-23 

4-18 Unit 3 - Results of HC1/C12 in Stack Gas 4-25 

4-19 Unit 4 - Results of HC1/C12 in Stack Gas 4-25 

4-20 Unit 2 - Analytical Results of Metals in Stack Gas 4-27 

4-21 Unit 2 - Results of Metals in Stack Gas 4-28 

4-22 Unit 3 - Analytical Results of Metals in Stack Gas 4-29 

4-23 Unit 3 - Results of Metals in Stack Gas 4-30 

4-24 Unit 4 - Analytical Results of Metals in Stack Gas 4-32 

4-25 Unit 4 - Results of Metals in Stack Gas 4-33 

4-26 Unit 2 - Results of Dioxins/Furans in Stack Gas 4-35 

4-27 Unit 3 - Results of Dioxins/Furans in Stack Gas 4-37 

4-28 Unit 4 - Results of Dioxins/Furans in Stack Gas 4-38 

4-29 Unit 2 - Results of THC in Stack Gas 4-39 

4-30 Unit 3 - Results of TCH in Stack Gas 4-40 

4-31 Unit 4 - Results of THC in Stack Gas 4-40 

4-32 Unit 2-Chlorine Feedrate 3-42 

4-33 Unit 3 - Chlorine Feedrate 3-43 

4-34 Unit 4-Chlorine Feedrate 3-44 

viii 

VES017676 
List of Tables (continued) 

Page 

4-35 Unit 2 - Ash Feedrate During the EPA Method 5 Stack Sampling for PM 4-45 

4-36 Unit 3 - Ash Feedrate During the EPA Method 5 Stack Samplmg for PM 4-46 

4-37 Unit 4 - Ash Feedrate During the EPA Method 5 Stack Sampling for PM 4-47 

4-38 Unit 2 - Metals Feedrate 4-49 

4-39 Unit 2 - HWC MACT Metals Feedrate 4-51 

4-40 Unit 3 - Metals Feedrate 4-52 

4-41 Unit 3 - HWC MACT Metals Feedrate 4-53 

4-42 Unit 4-Metals Feedrate 4-54 

4- 43 Unit 4 - HWC MACT Metals Feedrate 4-56 

5- 1 Results of Analysis of Audit Samples 5-2 

List of Figures 

Page 

2-1 Unit 2 Process Flow Diagram 2-3 

2-2 Unit 3 Process Flow Diagram 2-4 

2-3 Unit 4 Process Flow Diagram 2-5 

ix 

VES017677 
1.0 Introduction 

Veolia ES Technical Solutions, L.L.C. (Veoha) operates three incinerators at its Sauget, 

Illinois facility. Two of the incinerators are fixed hearth units (Units 2 and 3), and the third 

incinerator is a rotary kiln unit (Unit 4). All of the incinerators treat certain wastes that are 

classified as hazardous under state and/or federal regulations, and are subject to the National 

Emission Standards for Hazardous Air Pollutants (NESHAPs) for Hazardous Waste 

Combustors (Title 40 of the Code of Federal Regulations, Part 63 [40 CFR Part 63], Subpart 

EEE), (le., the HWC MACT). 

In August and September of 2008, Veolia conducted tests of Units 2, 3, and 4 required by 

the information collection requests from U.S. EPA Region 5 dated June 5, 2008 and September 

12, 2008. Those tests began on August 11, 2008 for Unit 2, August 5, 2008 for Unit 3, and 

August 21,2008 for Unit 4 following test plans approved by U.S. EPA Region 5. Initial 

Comprehensive Performance Tests (CPTs) of Units 2, 3, and 4 commenced on December 8, 2009 

for Unit 2; on December 1, 2009 for Unit 3; and on December 16,2009 for Unit 4, and were 

performed in accordance with Comprehensive Performance Test Plans approved by U.S. EPA 

Region 5.The HWC MACT, at 40 CFR § 63.1207(d), states "The date of commencement ofthe 

initial comprehensive performance test is the basis for establishing the deadline to commence the 

initial confirmatory perfonnance test and the next comprehensive performance test. You may 

conduct performance testing at any time prior to the required date. The deadline for 

commencing subsequent confirmatory and comprehensive performance testing is based on the 

date of commencement of the previous comprehensive performance test." EPA Region 5 

considers that the start of the subsequent CPTs be based on the initiation of the metals tests 

performed in 2008, requiring that the subsequent CPT be started by September 5, 2013, and that 

a site-specific test plan be submitted before this date. Veolia originally submitted to EPA its 

notification of intent and site-specific test plans (i.e., comprehensive performance test plans) for 

all three units and a Quality Assurance Project Plan (QAPjP) for the subsequent CPT on 

September 5, 2012. Revisions to the CPT Plans and QAPjP were made based on negotiations with 

EPA Region 5. The CPT Plan and QAPjP dated September 25,2013 were approved by EPA 

Region 5. 

EPA Region 5 considers that testing of the three incinerators comprises the CPT for 

Veolia's facility in Sauget. Veoha Sauget started the CPT of the three incinerators at the Sauget 

facility on September 4, 2013 with the performance of the RATA of the CO and 0 2 continuous 

monitoring systems (CEMS) of Unit 4. The RATA of the CO and 0 2 CEMS of Unit 3 was 

performed on September 5, 2013, and the RATA of the CO and 0 2 CEMS of Unit 2 was 

performed on September 6,2013. Testing for the applicable parameters of the HWC MACT 

including dioxins/furans, total hydrocarbons (THC), carbon monoxide (CO), particulate matter 

1-1 

VES017678 
(PM), hydrogen chloride/chlorine gas (HC1/C12), mercury, SVM, and LV M was completed on 

October 30,2012. In accordance with 40 CFR §63.1207(j)(l)(i) and §63.1207(j)(3), the 

Notification of Compliance (NOC) and CPT Report are being filed within 90 days of completion 

of the CPT. 

Per 40 CFR §63.1206(b)(7)(i)(A), compliance with the DRE standard is required to be 

demonstrated only one time, and Veolia Sauget demonstrated DRE during RCRA Trial Bums of 

Units 2, 3, and 4 performed in January 1993, November 1996, and December 1995, respectively. 

The HWC MACT requires that DRE only be demonstrated one time as long as "you do not feed 

hazardous waste at a location in the combustion system other than the normal flame zone" 

(§63.1207(c)(2)(iv)). Veolia did not re-demonstrate DRE in the subsequent CPT. DRE, and the 

associated OPLs, were demonstrated during the January 1993, November 1996, and December 

1995 RCRA Trial Bums, respectively for Units 2, 3, and 4, and operations of the incinerators 

have not significantly changed since that test. 

This test (i.e., the subsequent CPT) demonstrated applicable emission standards and 

established OPLs as required by the HWC MACT for dioxins/furans, THC, CO, PM, 

HCI/CI2, mercury, SVM, and LVM. The results of this are used to revise the NOC for the 

three incinerators. 

1.1 Incinerator Overview 

Units 2 and 3 are identical fixed hearth incineration systems with primary and secondary 

combustion chambers that treat solid wastes as well as aqueous and organic liquids. The 

processes are monitored and controlled by individual distributed control systems (DCS) capable 

of continuously monitoring the processes to assure all operational parameters are within 

regulatory and permit limits while waste is being fed to the unit. In addition, Units 2 and 3 are 

equipped with a Continuous Emissions Monitoring System (CEMS) that continuously samples 

the exhaust gases for carbon monoxide and oxygen in the stack gas exhaust stream. 

Unit 4 is a rotary kiln incineration system with primary and secondary combustion 

chambers that treats solid wastes as well as aqueous and organic hquids. The process is 

monitored and controlled by a DCS capable of continuously monitoring the process to assure all 

operational parameters are within regulatory and permit limits while waste is being fed to the 

unit. In addition, this incinerator is equipped with a CEMS that continuously samples the 

exhaust gases for carbon monoxide and oxygen in the stack gas exhaust stream. 

1-2 

VES017679 
1.2 Test Objectives 

This subsequent CPT for the Final Replacement Standards of the HWC MACT was 

designed and conducted to demonstrate compliance with the standards and associated OPLs of 

the HWC MACT for existing incinerators at §63.1219. The CPT: 

• Demonstrated that the incinerators meet the applicable HWC MACT emission 

limits while treating hazardous waste; and 

• Re-established operating parameter limits (OPLs) on key operating variables that 

will ensure that the incinerator operates within the HWC MACT emission Hmits 

while treating hazardous waste. 

The test program included feeding liquid and solid waste materials to the 

incinerators, samphng and analyzing the feedstreams, spiking waste feedstreams with metals 

and chlorine, monitoring certain process parameters, conducting emissions testing, and 

sampling of waste streams and spiking materials. Apphcable emissions standards under the 

HWC MACT regulations demonstrated during the CPT are summarized in Table 1-1. 

Table 1-1. Applicable HWC MACT Emission Standards 

Emissions Parameter Limit Citation 

Dioxins/Furans (TEQ basis) 

< 0.20 ng/dscm - Units 2 & 3 

< 0.40 ng/dscm - Unit 4 

40 CFR 63.1219(a)(l)(i)(A) 

40CFR63.1219(a)(l)(i)(B) 

Mercury < 130 ug/dscm 40 CFR § 63.1219(a)(2) 

Semivolatile Metals (SVM) (Cadmium and 

Lead) < 230 ug/dscm 40 CFR § 63.1219(a)(3) 

Low Volatile Metals (LVM) (Arsenic, 

Beryllium and Chromium) < 92 ug/dscm 40 CFR § 63.1219(a)(4) 

Carbon Monoxide (CO) < 100 ppmv, dry 40 CFR § 63.1219(a)(5)© 

Total Hydrocarbons (THC) < 10 ppmv, dry 40CFR§63.1219(a)(5)(ii) 

Hydrogen Chloride & Chlorine (HCVC12) < 32 ppmv dry, as Cl" 40 CFR § 63.1219(a)(6) 

Particulate Matter (PM) < 0.013 gr/dscf 40 CFR § 63.1219(a)(7) 

Destruction and Removal Efficiency (DRE) > 99.99 % 40 CFR § 63.1219(c)(1) 

Note: All emission concentrations are corrected to 7% oxygen. 

( 

1-3 

VES017680 
The objectives for the subsequent CPT for the Final Replacement Standards of the HWC 

MACT for each of the three incinerators were to: 

• Demonstrate compliance with stack gas emissions less than or equal to the 

following limits, corrected to 7% 02: 

— Carbon Monoxide: 100 ppmv, dry; 

— Total Hydrocarbons: 10 ppmv, dry; 

— Dioxins/Furans: 0.20 ng TEQ/dscm for Units 2 and 3, and 0.40 ng TEQ/dscm for 

Unit 4; 

— Particulate Matter (PM): 0.013 grains/dscf; 

— Mercury: 130 |j,g/dscm; 

— Semivolatile Metals (SVM) (Cd and Pb combined): 230 \ig /dscm; 

— Low Volatility Metals (LVM) (As, Be and Cr combined): 92 tig /dscm; and 

— Hydrogen Chloride/Chlorine (HC1/C12): 32 ppmv as CT equivalent, dry. 

• Compliance with the DRE standard (99.99% DRE) is demonstrated using data from 

previous RCRA trial bums. 

• Establish limits for operating parameters. 

• Conduct a Continuous Monitoring System (CMS) performance evaluation test. 

• Conduct a Relative Accuracy Test Audit (RATA) for the CO and 0 2 Continuous 

Emissions Monitoring Systems (CEMS. 

1.3 Test Protocol Summary 

A definition of the applicable emission limits and the resulting operating parameter limits 

(OPLs) are given in Section 4.0 ofthe CPT plans for each incinerator. The subsequent CPT of 

each of the incinerators included one test condition, and the test condition included one mode of 

operation. One set of OPLs was developed for each incinerator. 

In the first part of the test for each incinerator, Veolia demonstrated compliance with the 

particulate matter standard of the HWC MACT while the plant was operated to establish the 

maximum ash feedrate and maximum combustion gas flowrate OPLs as required by the HWC 

MACT for the particulate matter standard. Compliance with the standard for carbon monoxide 

was also demonstrated during this portion ofthe test. 

In the second part of the test for each incinerator, Veolia demonstrated compliance, and 

developed OPLs, with the HC1/C12, dioxins/furans, THC, CO, LVM, SVM, and mercury 

standards of the HWC MACT while the plant was operated to establish maximum total 

hazardous waste feedrate, maximum pumpable hazardous waste feedrate, minimum primary 

combustion chamber (PCC) temperature, minimum secondary combustion chamber (SCC) 

temperature, maximum LVM, SVM, and Hg feedrates, maximum chlorine feedrate, maximum 

1-4 

VES017681 
combustion gas flowrate, and maximum inlet temperature to the baghouse. Ash was fed to the 

incinerators at normal (or higher) levels during this portion of the test. Compliance with the 

standard for carbon monoxide was also demonstrated during this test 

Samples of the wastes fed during the tests were sampled every 15 minutes and 

composited for analysis. Waste feed samples were collected in coordination with the PM, 

HCI/CI2, metals, and dioxins/furans stack testing. Composite liquid waste feed samples 

associated with each ofthe four sampling trains were analyzed for ash, total chlorine, heat content, 

moisture, density, and viscosity. The composite liquid waste feed samples collected during the 

Method 29 stack sampling from the second part of the test were also analyzed for metals (arsenic, 

berylHum, chromium, cadmium, lead, and mercury). All of the composite solid waste feed 

samples, containerized and bulk, from the first and second parts of the test were analyzed for total 

chlorine, ash, moisture, and heat content. The composite containerized waste feed samples for Units 

2,3, and 4, and bulk solid waste feed samples from Unit 4, collected during the Method 29 stack 

sampling from the second part of the test were also analyzed for metals (arsenic, beryllium, 

chromium, cadmium, lead, and mercury). 

The incinerators were operated for 30 minutes at the desired feedrates and operating 

conditions before samphng began for a given condition of the testing to assure all operating 

parameters were stabiHzed at the desired settings to achieve steady state. Spiking with chromium, 

lead, mercury, and chlorine was initiated at least 30 minutes before beginning sampling in the 

second part of each test run for HC1/C12, metals, and dioxins/furans to assure that feedrates of 

spiking materials had stabilized before samphng began. Spiking of the waste feed with 

chromium, lead, mercury, and chlorine continued through the completion of the stack sampling 

for dioxins/furans, the last sampling to be completed. 

Chlorine and the metals lead, chromium and mercury were spiked into each of the three 

incinerators during, and throughout, the second part of each test run. The LVM category for 

incinerators includes arsenic, beryllium and chromium. Chromium was spiked as a solution of 

chromic acid into the PCC of the respective incinerators. The SVM category for incinerators 

includes cadmium and lead. Lead was spiked as sohd lead nitrate fed to the incinerators in premeasured plastic baggies at regular intervals with the containerized solid waste. Mercury is the 

only high volatility metal of the HWC MACT. Mercury was spiked as a mercuric nitrate solution, 

and was fed in vials fed to the incinerator at regular intervals with the containerized sohd waste. The 

concentration of the solution of mercuric nitrate was different (higher) for Unit 4 than for Units 2 

and 3. One vial containing 10 mLs of the mercuric nitrate solution was fed per charge of the 

containerized soUd waste to Units 2 and 3, and one vial containing 20 mLs were fed with each 

charge of the containerized sohd wastes to Unit 4. 

40 CFR §63.1207(g)(1)(A) requires feeding normal (or higher) levels of chlorine during the 

test for dioxins/furans. Chlorine was spiked the second part of the test and throughout the 

dioxins/furans testing to provide a consistent feedrate of chlorine throughout the dioxins/furans 

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VES017682 
sampling. The average feedrate of chlorine for Unit 2 from December 2012 through May 2013 was 

35 lb/hr; the average feedrate of chlorine for Unit 3 from December 2012 through May 2013 was 

31 lb/hr; and the average feedrate of chlorine for Unit 4 from December 2012 through May 2013 

was 82 lb/hr. The spiking rate of chlorine was about 200 lbs/hr for all three incinerators. 

Pursuant to 40 CFR §63.1209(m)(3), Veoha is establishing a maximum ash feedrate during 

the CPT for each of the three incinerators, developed in association with the sampling ofthe stack 

gas for particulate matter. The desired ash feedrate was achieved as the ash fed to the incinerator 

with the wastes, primarily sohd wastes. The requirement in 40 CFR §63.1207 (g) (1)(B) for feeding 

normal (or higher) levels of ash during the SVM and LVM performance tests was achieved by the 

feeding of sohd wastes. The average solids feedrate of ash in the first part of the test was 503.0 

lbs/hr for Unit 2, 525.8 lbs/hr for Unit 3, and 4,777.2 lbs/hr for Unit 4. The feeding of solid 

wastes continued throughout the second part of the test at rates similar to those in the first part of 

the test. The average feedrate of ash for Unit 2 from December 2012 through May 2013 was 102 

lb/hr; the average feedrate of ash for Unit 3 from December 2012 through May 2013 was 109 lb/hr; 

and the average feedrate of ash for Unit 4 from December 2012 through May 2013 was 949 lb/hr. 

40 CFR 63.1207(g)(l)(i)(C) requires that tests for PM, SVM, LVM, mercury, and 

dioxins/furans include a normal cleaning cycle of the PM control device. For each of the three 

units, the baghouse is the unit of the air pollution control train that is designed and operated to 

control particulate matter. Testing in all three runs for PM, SVM, LVM, mercury, and 

dioxins/furans was performed including a cleaning cycle of the fabric filter (i.e., baghouse). 

Per 40 CFR §63.1206(b)(7)(i)(A) compliance with the DRE standard is required to be 

demonstrated only one time and Veolia demonstrated DRE for each of the three incinerators in 

RCRA trial bums. The RCRA trial bum for Unit 2 was conducted in January 1993, and the 

RCRA trial bum for Unit 3 was conducted in November 1996. The RCRA trial bum for Unit 4 

was conducted in December 1995. Veolia did not re-demonstrate DRE in the subsequent CPT for 

the Final Replacement Standards of the HWC MACT because DRE, and the associated OPLs, 

were demonstrated during the RCRA trial bums, and operations of the incinerators have not 

significantly changed since those tests. The operating limits associated with the standard for 

DRE for Unit 2 are: 

• Maximum Total Pumpable Waste Feedrate 3,107 lb/hr; 

• Maximum Total Waste Feedrate 4,017 lb/hr; 

• Minimum Stack Gas Flowrate 15,605 acfm; 

• Minimum Temperature in the Primary Combustion Chamber 1,658°F; and 

• Minimum Temperature in the Secondary Combustion Chamber 1,848°F. 

1-6 
The operating limits associated with the standard for DRE for Unit 3 are: 

• Maximum Total Pumpable Waste Feedrate 4,045 lb/hr; 

• Maximum Total Waste Feedrate 5,098 lb/hr; 

• Minimum Stack Gas Flowrate 16,061 acfm; 

• Minimum Temperature in the Primary Combustion Chamber 1,627°F; and 

• Minimum Temperature in the Secondary Combustion Chamber 1,845°F. 

The operating limits associated with the standard for DRE for Unit 4 are: 

Maximum Total Pumpable Waste Feedrate to the Kiln 

Maximum Total Pumpable Waste Feedrate to the SCC 

Maximum Total Waste Feedrate to the Kiln 

Maximum Total Waste Feedrate to the SCC 

Minimum Stack Gas Flowrate 

3,312 lb/hr; 

1,788 lb/hr; 

18,667 lb/hr; 

1,788 lb/hr; 

44,900 acfm; 

• Minimum Temperature in the Primary Combustion Chamber 1,415°F; and 

• Minimum Temperature in the Secondary Combustion Chamber 1,798°F. 

The OPLs associated with each of the applicable emission standards (i.e., PM, HC1/CI2 

gas, metals, and dioxins/furans) were developed using process data taken during the collection 

ofthe applicable sampling train (i.e., EPA Method 5 for particulate matter, Modified EPA 

Method 26A for HCyCl 2, EPA Method 29 for metals, and SW-846 Method 0023A for 

dioxins/furans). Operating parameter data were used as shown in Table 1-2 to develop HWC 

MACT OPLs. 

THC is typically monitored in CPTs during the measurement of DRE. The OPLs for 

THC (i.e., minimum combustion chamber temperature in the primary combustion chamber, 

minimum combustion chamber temperature in the secondary combustion chamber, maximum 

flue gas flowrate, maximum pumpable hazardous waste feedrate, and maximum total waste 

feedrate) are the same as the OPLs for DRE and dioxins/furans. Even though DRE was not 

demonstrated, THC was measured during the second part of each test ran of the CPT for each 

unit. 

1-7 
Table 1-2. Data Used to Establish OPLs 

Demonstrated OPLs 

Emission 

OPLs Developed 

During the CPT 

Demonstrated OPLs Standard Unit 2 Unit 3 Unit 4 

Maximum Pumpable Waste Feedrate 

D R E 1993 1996 1995 

Maximum Pumpable Waste Feedrate T H C • • Maximum / Pumpable Waste Feedrate 

Dioxins/Furans • • / 

Maximum Total Waste Feedrate 

D R E 1993 1996 1995 

Maximum Total Waste Feedrate T H C • • Maximum / Total Waste Feedrate 

Dioxins/Furans • • V 

Maximum Stack Gas Flowrate 

S V M V / 

Maximum Stack Gas Flowrate 

L V M • V •/ 

Maximum Stack Gas Flowrate 

P M • V / 

Maximum Stack Gas Flowrat Flowrate HCI/C12 • • • 

D R E 1993 1996 1995 

Maximum Stack Gas Flowrate 

T H C • V 

Maximum Stack Gas Flowrate 

Dioxins/Furans • •/ S 

Minimum Combustion Chamber Temperature in the PCC 

D R E 1993 1996 1995 

Minimum Combustio Combustion Chamber Temperatur Temperature in the PCC T H C • • 

Dioxins/Furans • S 

Minimum Combustion Chamber Temperature in the SCC 

D RE 1993 1996 1995 

Minimum Combustion Chamber Temperature in the SCC T H C • • V Combustion Chamber Temperature in the SCC 

Dioxins/Furans • 

Maximum Total Feedrate of LV M (As, Be, Cr) L V M • • 

Maximum Pumpable Feedrate of LV M (As, Be, Cr) L V M • • </ 

Maximum Feedrate of SV M (Pb, Cd) S V M • • • 

Maximum Feedrate of Mercury (Hg) Hg 

Maximum Feedrate of Ash P M • 

Maximum Feedrate of Total Chlorine/Chloride 

HC1/C12 • • • 

Maximum Feedrate of Total Chlorine/Chloride L V M • V •/ Feedrate of Total Chlorine/Chloride 

S V M • • •/ 

Maximum Baghouse Inlet Temperature 

T HC • S 

Maximum Baghouse Inlet Temperature 

Dioxins/Furans • s Maximum Baghouse Inlet Temperature 

L V M • • 

Maximum Baghouse Inlet Temperature 

S V M • • s 

Minimu m Carbon Feedrate 

Dioxins/Furans N A N A 

Minimu m Carbon Feedrate 

H g N A N A • 

Minimum Sorbent Feedrate HC1/C12 • • 

Minimum Carrier Fluid Flowrate HCVC12 • • 

1993 - Operating data from the January 1993 RCR A Trial Burn for Unit 2. 

1996 - Operating data from the November 1996 RCR A Trial Bum for Unit 3. 

1995 - Operating data from the December 1995 RCR A Trial Bum for Unit 4. 

1-8 

VES017685 
1.4 CPT Schedule 

The subsequent CPT of the three incinerators at the Sauget facility began with the 

performance of RATAs. The RATA of the CO and 0 2 continuous monitoring systems (CEMS) 

of Unit 4 was performed on September 4, 2013. The RATA of the CO and 0 2 CEMS of Unit 3 

was performed on September 5,2013, and the RATA of the CO and 0 2 CEMS of Unit 2 was 

performed on September 6, 2013. 

The CPT with testing for dioxins/furans, THC, CO, PM, HC1/C12 gas, mercury, SVM, 

and LV M was conducted in October 2013. The CPT testing for each of the three incinerators was 

observed by staff from the Illinois Environmental Protection Agency (IEPA). Due to the federal 

government shutdown in the earlier stages of October 2013, staff from EPA Region 5 observed 

the CPT testing only of Unit 4, the last unit tested. 

The subsequent CPT of Unit 2 was begun October 8, 2013. Run 1 of the test was 

successfully completed on this day. Run 2 was performed on October 9, 2013. The first part of 

Run 2 was successfully completed. During the second part of Run 2, the THC monitor failed and 

drifted well beyond the emission limit of the HWC MACT for THC. It was recognized that the 

THC monitor used to demonstrate compliance with the HWC MACT had malfunctioned because 

Veolia monitors stack gases for THC, and the concentration of THC monitored by Veolia had 

not increased. The second part of Run 2 was stopped for this reason. The THC monitor was 

replaced and Run 3 was performed on October 10,2013. With the successful completion of Run 

3, three runs for PM had been successfully completed. The third run of the second part of the test 

of Unit 2 (i.e., Run 4) was performed on October 11,2013. At the completion of Run 4, the leakcheck of the pitot tubes of the dioxins/furans sampling train did not meet the full requirements of 

the applicable EPA test method (i.e., EPA Method 2) although it was considered that the leakcheck of the pitot tubes was acceptable. Because it was felt that the results of the dioxins/furans 

samphng train were acceptable, this mn of the CPT of Unit 2 was not re-done. Personnel from 

EPA Region 5 declared that the dioxins/furans samphng train was unacceptable when on-site the 

week of October 21, 2013. Another mn of the second part ofthe test, for HC1/C12, metals, and 

dioxins/furans, (i.e., Run 5) was performed on October 30, 2013. 

The subsequent CPT of Unit 3 was begun October 15, 2013. The first part of Run 

1, for PM, was successfully completed on this day. However, the isokinetic sampling rate 

ofthe dioxins/furans sampling train did not meet method acceptance criteria, and the 

second part of this ran, for HC1/C12, metals, and dioxins/furans, had to be repeated as Run 

4. Run 2 was performed on October 16, 2013, and Run 3 was performed on October 17, 

2013. The third successful ran of the second part of the test of Unit 3 (i.e., Run 4) was 

performed on October 18, 2013. 

1-9 
The subsequent CPT of Unit 4 was begun October 23,2013 with the successful 

completion of Run 1. Run 2 was performed on October 24, 2013. The glass nozzle of the PM 

sampling train was chipped with the withdrawal of the sampling probe from the stack at the 

completion of the run. Although the sampling train met all acceptance criteria, including the final 

leak-check, the second mn for PM was repeated. Run 3 was performed on October 25, 2013. The 

third (accepted) run for PM (i.e., Run 4) was performed at the conclusion of Run 3 for PM. 

Incinerator operating conditions required for the PM testing were maintained through both of 

these test runs. 

1.5 Summary of Results 

Veolia successfully demonstrated compliance with all of the applicable regulatory 

requirements of the HWC MACT for Unit 2, Unit 3, and Unit 4 using the results from the single 

test condition of each unit. Table 1-3 summarizes the results of the emissions testing of Unit 2. 

Table 1-4 summarizes the results of the emissions testing of Unit 3, and Table 1-5 summarizes 

the results of the emissions testing of Unit 4. The test for each unit consisted of three reported 

runs for each parameter of interest. The term "test condition" refers to the sum of all the testing 

activities designed to demonstrate the operation ofthe waste incinerator under particular 

operating parameters (e.g., development of operating parameter limits) under the HWC MACT. 

The term "test run" refers to the replicate testing periods. A complete definition of the test 

protocol and methodology is defined in the CPT Plan and QAPjP. 

1.6 Report Organization 

The remainder of this report presents the following sections: 

• Section 2.0 - Process Operations; 

• Section 3.0 - Sampling, Analysis, and Monitoring Procedures; 

• Section 4.0 - Results; and 

• Section 5.0 - Quality Assurance/Quality Control. 

The appendices provide raw data, including chain-of-custody forms, samphng data sheets 

and logs, laboratory reports, process data, CMS PET sheets, spiking reports, and sampling 

equipment calibration forms. 

1-10 
Table 1-3. Unit 2 Compliance Summary 

Unit 2 

Parameter H W C MAC T Limit Runl 

10-8-13 

Run 2 

10-9-13 

Run 3 

10-10-13 

Run 5 

10-30-13 

Average 

Particulate Matter - EP A Method 5 0.013 gr/dscf corrected to 7% 0 2 <0.00087 <0.00068 <0.00058 <0.00071 

HCl/Cl 2 - Modified EP A Method 26A 32 ppmv dry, as CI', corrected to 7% 0 2 <29 <13 <18 <20 

Metals - EP A Method 29 

L V M 

S V M 

Mercury 

92 (ig/dscm corrected to 7% 0 2 

230 ug/dscm corrected to 7% 0 2 

130 ug/dscm corrected to 7% 0 2 

<2.8 

< U 

<90 

<2.4 

<0.78 

<120 

<2.5 

<1.0 

<95 

<2.6 

<0.95 

<100 

Dioxins/Furans - SW-846 Method 0023A 0.20 ng/dscm conected to 7% 0 2 0.00543 0.00624 0.0157 0.00912 

Total Hydrocarbons (THC) - EP A Method 25A 10 ppmv, dry corrected to 7% 0 2 1.6 0.18 0.49 0.75 

Carbon Monoxide (CO) 1 100 ppmv, dry corrected to 1% 0 2 0.00 0.00 0.15 0.05 

1

 THC and C O results collected during the stack sampling for dioxins/furans. 

1-11 

VES017688 
] 

Table 1-4. Unit 3 Compliance Summary 

Parameter H W C MAC T Limit 

Unit 3 

Parameter H W C MAC T Limit Run l 

10-15-13 

R u n 2 

10-16-13 

R u n 3 

10-17-13 

R u n 4 

10-18-13 

Average 

Particulate Matter - EP A Method 5 0.013 gr/dscf corrected to 7% 0 2 0.00194 0.00202 0.00204 0.00200 

HC1/C12 - Modified EP A Method 26A 32 ppmv dry, as Cl" , corrected to 7% 0 2 <4.5 <4.4 <1.8 <3.6 

Metals - EP A Method 29 

L V M 

S V M 

Mercury 

92 ug/dscm corrected to 7% 0 2 

230 ug/dscm corrected to 1% 0 2 

130 ug/dscm corrected to 1% 0 2 

<8.6 

<20 

<59 

<8.9 

<14 

<39 

<11 

<12 

<46 

<9.4 

<15 

<48 

Dioxins/Furans - SW-846 Method 0023A 0.20 ng/dscm corrected to 7% 0 2 0.00103 0.00115 0.00134 0.00118 

Total Hydrocarbons (THC) - EP A Method 25A 10 ppmv, dry corrected to 7% 0 2 0.44 0.26 0.57 0.43 

Carbon Monoxide (CO) 1 100 ppmv, dry corrected to 7% 0 2 0.00 0.00 0.00 0.00 

1

 TH C and CO results coUected during the stack sampling for dioxins/furans. 

1-12 

VES017689 
Table 1-5. Unit 4 Compliance Summary 

Unit 4 

Parameter H W C MAC T Limit Runl Run 2 Run 3 Run 4 

Average 

10-23-13 10-24-13 10-25-13 10-25-13 

Average 

Particulate Matter - EP A Method 5 0.013 gr/dscf corrected to 7% 0 2 0.00269 0.00183 <0.0019 <O.0021 

HCl/Cl 2 - Modified EP A Method 26A 32 ppmv dry, as Cl", corrected to 7% 0 2 <11 <8.0 <23 <14 

Metals - EP A Method 29 

L V M 92 (tg/dscm corrected to 7% 0 2 <12 <9.8 <7.5 <9.7 

S V M 230 ug/dscm corrected to 7% O z <8.6 <4.5 <10 <7.8 

Mercury 130 ug/dscm corrected to 1% 0 2 <7.1 <8.1 <15 <10 

Dioxins/Furans - SW-846 Method 0023A 0.40 ng/dscm corrected to 7% 0 2 0.138 0.132 0.139 0.137 

Total Hydrocarbons (THC) - EP A Method 25A 10 ppmv, dry corrected to 7% 0 2 0.51 0.60 0.85 0.65 

Carbon Monoxide (CO) 1 100 ppmv, dry corrected to 1% 0 2 0.07 0.06 0.08 0.07 

1

 TH C and C O results collected during the stack sampling for dioxins/furans. 

1-13 

VES017690 
2.0 Process Operations 

This section presents brief descriptions of the three incinerators at Veoha's facility in 

Sauget, IL, and process and feedrate results from the CPTs of the three incinerators. 

2.1 Process Overview 

Veolia operates two Fixed Hearth Dual Chambered incinerators (Units 2 and 3) and one 

rotary kiln incinerator (Unit 4) at the Sauget, DL facility. The two fixed hearth units are rated at 16 

million Btu/hr each. Unit 3 is a mirror image of Unit 2. Both of these units have their own waste 

handling systems. 

Units 2 and 3 feature a two-stage combustion process. Ignition of waste material takes 

place in the primary flower) combustion chamber (PCC). A secondary (upper) combustion 

chamber (SCC) serves as an "afterburner" for process gases. Liquid wastes, organic and aqueous, 

and solid wastes are fed to the PCC. Air-atomizing injectors are used for injection of high-Btu 

hquids, low-Btu liquids and specialty feed liquids. Sohds, usually packaged in plastic or fiberboard 

containers, are introduced into the incinerator through a PLC controlled airlock-ram system located 

at the lower front of the PCC. 

The air pollution control systems of Units 2 and 3 consist of a spray dryer absorber and 

fabric filter baghouse modules. The air pollution control system neutralizes acidic compounds and 

removes particulate matter from the exhaust gas. Two subsystems, the spray dryer absorber and the 

fabric filter, carry out the chemical neutralization and particulate removal functions, respectively. 

An induced draft fan and stack provide the mechanical energy required to transport the flue gas 

through the interconnecting ductwork, to its eventual discharge point to atmosphere. The only 

difference between Units 2 and 3 is that Unit 2 is equipped with four (4) baghouse modules, while 

Unit 3 is equipped with three (3) baghouse modules. However, each incinerator is operated 

identically with only three baghouse modules in service during operation. 

A complete description of Units 2 and 3 is provided in the CPT Plan. A process flow 

diagram for Unit 2 is presented in Figure 2-1, and a process flow diagram for Unit 3 is presented in 

Figure 2-2. 

2-1 
Unit 4 is rated at 50 million Btu/hr and is equipped with its own tank farm system, drum 

storage, bulk solids storage and feed systems. Unit 4 includes a rotary kiln as the PCC, and a SCC. 

Liquids are fed to either the kiln PCC or the SCC. Bulk solid wastes are fed to the kiln through the 

ram feeder. Containerized wastes are fed to the kiln through the ram feeder or the auxiliary ram 

feeder. The liquid waste injectors used in the combustion chambers are air-atomizing injectors, and 

are used for injection of pumpable sludges, aqueous wastes and organic liquid wastes to the kiln 

and for injection of organic liquid waste to the SCC. 

The air pollution control system consists of a tempering chamber, two spray dryer 

absorbers, and fabric filter baghouse modules with carbon injection. The air pollution control 

system neutralizes acidic compounds and removes particulate from the exhaust gas. Two 

subsystems, the spray dryer absorber and the fabric filter, carry out the chemical neutralization and 

particulate removal functions, respectively. An induced draft fan and stack provide the mechanical 

energy required to transport the flue gas through the interconnecting ductwork, to its eventual 

discharge point to atmosphere. 

A complete description of Unit 4 is provided in the Comprehensive Performance Test Plan. 

A process flow diagram for Unit 4 is presented in Figure 2-3. 

2-2 

VES017692 
Figure 2-1. Unit 2 Process Flow Diagram 

TANK FARM 

DIRECT INJECT, 

HIGH 

BTU 

LIQUIDS 

SOLIDS 

Mil l 

IIII I 

J f ,T_T X T 

COMBUSTION 

AIR 

BLOWER 

I (• * 

lOOOOOOM 

TANK FARM R LOW 

8TU; 

DIRECT INJECT , UQUJQS 

INCINERATOR 

LOWER 

CHAMBER 

LIQUID CONTAINERS,, 

GAS CYLINDERS. 

SPECiAVTY 

FEEQER 

\ PRIMARY V 

/ FUEL / 

5K0N0ARY 

AT 

BiERC0fOf: 

STARS 

INCINERATOR 

UPPER 

CHAMBER 

WET AStf 

DUMPSTER 

t~~F 

I

 : l i i 

UME 

PREPARATION 

SYSTEM 

SPRAY 

DRY 

ABSORBER 

MAIN STACKSTACX MS 

ANAtfZWS • 

BAGHOUSE: 1.0. FAN 

DRY SCRUBBER DRY SCRUBBER 

SOUDS { OSS ) SOUDS ( OSS ) 

END DUMP END DUMP 

cooooc*-

toooo* -

.FUELS/UQWD WASTE FLOW 

COMBUSTION A18 FLOW 

STACK OAS FLOW 

A SH FLOW 

SOLID WASTE RO W 

U M C SLURRY FLOW 

2-3 

VES017693 
Figure 2-2. Unit 3 Process Flow Diagram 

TANK FARM 

DIRECT MJECI 

I I I I I 

I 1 I I I 

T..T.TJT.ITANK FARM „ LOW 

BTU 

DIRECT INJECT LIQUIDS 

ssmmi 

INONERATOR 

LOWER 

CHAMBER 

I 

woisMnr' 

STACX 

U ME 

PREPARATION 

SYSTEM 

MAIN STACKSWCK CAS 

ANALYSIS' 

INCINERATOR 

UPPER 

CHAMBER 

WET m 

DUMPSTER 

T f 

i i i i 

SPRAY 

PRY 

A8S0RBER 

SPECIALTY FEEDER 

FUME HOOD 

EMISSION CONTROL 

SYSTEM 

PRIMARY 

FUEL > 

8AGHOUSE 1.0. FA N 

ORY SCRUBBER DRT SCRUBBER 

SOLIDS ( OSS ) SOUOS ( DSS ) 

END "DUMP END DUMP 

CLOVE BOX 

EMISSION CONTROL! 

SYSTEM 

-—*-

ooccooFuasAwuro WASTE FLOW 

COMBUSTION AIR FLOW 

STACK OAS FLOW 

A SH FLOW 

SOUD WASTE FLOW 

U M E SLURRY FLOW 

2-4 

VES017694 
Figure 2-3. Unit 4 Process Flow Diagram 

TANK FARM j 

SECONDARY 

QCMBUSTM 

CHAMBE R 

TEMPERING 

SECONDARY 

QCMBUSTM 

CHAMBE R 

CHAMBE R 

ORY SCRUBBER, 

,S0l!DS { OSS ) 

END PUMP 

SPRAY 

DRY 

ABSORBER 

PREPARATION 

SYSTEM 

SPRAY 

DRY 

ABSORBER 

WET ASH ORY ASH 

DUMPSTER DUMPSTER ORY SCRUBBER 

S0U0S(0S S ) 

END DUMP 

ORY SCRUBBER 

iSOUDS ( DSS ) 

END DUMP 

BACHOUS E 

MAIN STACK -

CARBON 

INJECTION 

SYSTEM 

BAGHOUSE J— J 

STACK CAS 

AWZERS 

1,0. FA N 

ORY SCRUBBER 

jsOUOS ( DSS ) 

ENO DUMP 

fUELS/UOUlO WASTE ROW 

COMBUSTION AIR FLOW 

STACK GAS no w 

ASH FLOW 

SOUD WASTE FLOW 

U M E SLURRY FLOW 

2-5 

VES017695 
2.2 Process Operating Data and Waste Feedrates 

Process parameters that were monitored and recorded during the test by Veolia, and 

feedrates that result from the combination of waste feedrates with the respective waste feed 

analyses, are presented in this section. Process data recorded by Veolia every 15 seconds are used to 

create one-minute averages (OMAs). The DCS calculates hourly rolling averages (HRAs) for 

applicable parameters using the OMA from the first minute and the OMAs from previous 59 

minutes of data. The raw data from Veolia's DCS are provided in Appendix C. 

2.2.1 Unit 2 

Process data and waste and parameter feedrates have been determined and are presented for 

the time periods over the collection of the stack gas sampling trains for particulate matter (EPA 

Method 5), HC1/C12 (Modified EPA Method 26A), metals (EPA Method 29), and dioxins/furans 

(SW-846 Method 0023A) and THC (EPA Method 25A). 

Table 2-1 presents process data summaries and waste feedrates during the particulate matter 

(PM) stack gas sampling of the first part of each test mn for Unit 2. 

Table 2-2 presents process data summaries and waste feedrates during the HC1/C12 stack gas 

sampling of the second part of each test run for Unit 2. 

Table 2-3 presents process data summaries and waste feedrates during the metals stack gas 

sampling of the second part of each test run for Unit 2. 

Table 2-4 presents process data summaries and waste feedrates during the dioxins/furans 

and THC stack gas sampling and monitoring of the second part of each test run for Unit 2. 

2.2.2 Unit 3 

Table 2-5 presents process data summaries and waste feedrates during the PM stack gas 

sampling of the first part of each test ran for Unit 3. 

Table 2-6 presents process data summaries and waste feedrates during the HCI/CI2 stack gas 

sampling of the second part of each test ran for Unit 3. 

Table 2-7 presents process data summaries and waste feedrates during the metals stack gas 

sampling of the second part of each test run for Unit 3. 

Table 2-8 presents process data summaries and waste feedrates during the dioxins/furans 

and THC stack gas sampling and monitoring ofthe second part of each test run for Unit 3. 

2-6 

VES017696 
2.2.3 Unit 4 

Table 2-9 presents process data summaries and waste feedrates during the PM stack gas 

sampling of the first part of each test mn for Unit 4. 

Table 2-10 presents process data summaries and waste feedrates during the HCVCI2 stack 

gas sampling of the second part of each test run for Unit 4, 

Table 2-11 presents process data summaries and waste feedrates during the metals stack gas 

sampling of the second part of each test ran for Unit 4. 

Table 2-12 presents process data summaries and waste feedrates during the dioxins/furans 

and THC stack gas sampling and monitoring of the second part of each test run for Unit 4. 

2.3 Spiking of Metals and Chlorine 

During the test of each incinerator, the metals chromium, lead, and mercury were spiked into 

the incinerator. The spiking was performed by Veolia. Details concerning the spiking of metals and 

chlorine are presented in Appendix B. 

The spiking rates of chlorine during the HCI/CI2 stack sampling of the second part of each 

ran are presented in Table 2-13 for Unit 2, Table 2-14 for Unit 3, and 2-15 for Unit 4. 

The spiking rates of chromium, lead, mercury, and chlorine during the metals stack 

samphng of the second part of each ran are presented in Table 2-16 for Unit 2, Table 2-17 for Unit 

3, and 2-18 for Unit 4. 

The spiking solutions of chromium (chromic acid) and mercury (mercuric nitrate) were 

sampled at the beginning, at port change, and at the end of the EPA Method 29 stack sampling for 

metals of each ran, and each of these samples were analyzed for chromium or mercury, 

respectively. The analytical results for chromic acid and mercuric nitrate solutions are presented in 

Tables 2-19 and 2-20 for Unit 2, Tables 2-21 and 2-22 for Unit 3, and Tables 2-23 and 2-24 for Unit 

4. 

2-7 

VES017697 
) 

Table 2-1. Unit 2 - Summary of Process Data1 and Feedrates During 

the EPA Method 5 Stack Sampling for PM 

Operating Parameter Units Basis 

Run l 

10-8-13 

11:50 -13:00 

Run 2 

10-9-13 

09:45-10:53 

Run 3 

10-10-13 

09:15 -10:23 

Average Operating Parameter Units Basis 

Max Avg Min Max Avg M in Max Avg M in Max Avg M i n 

Stack Gas Flowrate ACFM HRA 15,015 14,955 14,876 15,529 15,430 15,324 15,690 15,374 15,240 15,412 15,253 15,147 

Low-Btu Liquid Waste Feedrate lb/hr OMA 1,947.7 1,277.2 899.3 1,948.6 1,353.3 749.5 2850.8 1288.3 299.8 2,249.0 1,306.3 649.5 

High-Btu Liquid Waste Feedrate lb/hr OMA 1,009.9 1,000.2 982.6 1,142.2 997.7 792.3 1008.4 998.5 985.5 1,053.5 998.8 920.1 

Specialty Liquid Waste Feedrate lb/hr OMA 351.7 270.8 190.5 424.9 256.5 131.9 468.9 296.7 161.2 415.1 274.6 161.2 

Containerized Solids Waste Feedrate lb/hr OMA 734.9 738.4 746.0 739.8 

Ash Feedrate lb/hr OMA 501.6 513.2 494.2 503.0 

PCC Temperature °F OMA 1,735 1,708 1,640 1,733 1,691 1.650 1,759 1,698 1,638 1,742 1,699 1,643 

SCC Temperature °F OMA 1,894 1,880 1,867 1,893 1,880 1,869 1,900 1,882 1,870 1,896 1,881 1,869 

CO, Corrected to 7% 0 2 ppmvd OMA 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 O.OO 

Baghouse Inlet Temperature2 °F OMA 440 420 396 444 420 400 438 421 393 441 420 396 

' Process data are the averages for the duration of the emissions sampling run for particulate matter in stack. 

2

 Measured as the SDA (Spray Dryer/Absorber) Outlet Temperature. 

Note: Values in bold used to develop OPL. 

2-8 

VES017698 
I 

Table 2-2. Unit 2 - Summary of Process Data1 and Feedrates During 

the Modified EPA Method 26A Stack Sampling for HCI/CI2 

Operating Parameter Units Basis 

Run l 

10-8-13 

15:40 -16:40 

Run 3 

10-10-13 

, 12:30 -13:30 

Run 5 

10-30-13 

12:45 -13:45 

Average 

Operating Parameter Units Basis 

Max M i n Max Avg Min Max Avg Min Max Avg M i n 

Stack Gas Flowrate acfm HRA 15,410 15,278 15,142 15,854 15,652 15,310 15,407 15,225 15,038 15,557 15.385 15,163 

Low-Btu Liquid Waste Feedrate lb/hr OMA 2,546.4 1,422.1 299.8 2,246.8 1,500.9 899.6 2,321.8 1,451.9 374.9 2371.6 1458.3 524.8 

High-Btu Liquid Waste Feedrate lb/hr OMA 1,424.2 1,370.8 1,191.0 1,129.5 1,098.7 1,051.6 1,226.6 1,200.0 1,163.7 1260.1 1223.1 1135.5 

Specialty Liquid Waste Feedrate lb/hr OMA 586.1 485.9 410.3 527.5 398.2 307.7 615.4 440.8 263.7 576.3 441.6 327.2 

Containerized Solids Waste Feedrate2 lb/hr 884.8 902.0 880.4 889.0 

Total Chlorine Feedrate lb/hr 208.0 207.5 202.8 206.1 

Sorbent Feedrate lb/lb Ch HRA 2.32 2.18 2.21 2.24 

Carrier Fluid Flowrate gal/lb Cl 2 HRA 1.93 1.85 1.92 1.90 

PCC Temperature «p OMA 1,772 1,707 1,648 1,813 1,721 1,631 1,753 1,703 1,608 1,779 1,710 1,629 

SCC Temperature °F OMA 1,958 1,891 1,866 1,910 1,878 1,865 1,897 1,882 1,872 1,922 1,884 1,868 

CO, Corrected to 7% O2 ppmvd OMA 0.00 0.00 0.00 0.00 0.00 0.00 0.66 0.08 0.00 0.22 0.03 O.OO 

Baghouse Inlet Temperature3 °F OMA 447 421 392 439 418 399 439 419 394 441 420 395 

1

 Process data are the averages for the duration of the emissions sampling run for HCI/O2 in stack. 

2

 Containerized Waste Feedrate includes the spikes of hexachloroethane, lead nitrate, and mercuric nitrate solution. 

3

 Measured as the SDA (Spray Dryer/Absorber) Outlet Temperature. 

Note: Values in bold used to develop OPL. 

2-9 

VES017699 
Table 2-3. Unit 2 - Summary of Process Data1

 and Feedrates During the EPA Method 29 Stack Sampling for Metals 

Operating Parameter Units Basis 

Run l 

10-S-13 

15:40-18:43 

Run 3 

10-10-13 

12:30-15:10 

Run 5 

10-30-13 

12:45 -15:32 

Average 

Operating Parameter Units Basis 

Max Avg Min Max Avg Min Max Avg M in Max Avg M i n 

Stack Gas Flowrate acfm HRA 15,602 15,375 14,946 15,854 15,487 15,126 15,636 15,438 15,038 15,697 15,433 15,037 

Low-Btu Liquid Waste Feedrate lb/hr OMA 2,546.4 1,474.6 299.8 2,246.8 1,513.3 899.6 2,547.3 1,396.5 0.9 2,446.8 1,461.5 400.1 

High-Btu Liquid Waste Feedrate Ib/hr OMA 1,424.2 1,289.1 1,191.0 1,129.5 1,098.9 1,051.6 1,226.6 1,164.6 973.4 1,260.1 1,184.2 1,072.0 

Specialty Liquid Waste Feedrate lb/hr OMA 615.4 432.6 0.0 586.1 425.4 307.7 732.6 445.3 234.4 644.7 434.4 180.7 

Containerized Solids Waste Feedrate2 lb/hr 895.0 883.1 891.2 889.8 

S V M Feedrate lb/hr 61.9 61.7 62.0 61.9 

L V M Feedrate-Total lb/hr 45.8 47.3 45.9 46.3 

L V M Feedrate - Pumpable lb/hr 45.9 47.3 45.9 46.3 

Mercury Feedrate lb/hr 0.00205 0.00206 0.00224 0.00212 

Total Chlorine Feedrate lb/hr 209.6 203.6 205.1 206.1 

Baghouse Inlet Temperature3 

°F OMA 447 420 392 439 419 399 439 419 394 441 420 395 

PCC Temperature "F OMA 1,772 1,701 1,622 1,821 1,708 1,607 1,798 1,705 1,608 1,797 1,705 1,612 

SCC Temperature °F OMA 1,958 1,875 1,714 1,962 1,886 1,865 1,897 1,882 1,857 1,939 1,881 1,812 

CO, Corrected to 7% Oj ppmvd OMA 0.00 0.00 0.00 0.00 0.00 0.00 1.25 0.13 0.00 0.42 0.04 0.00 

1

 Process data are the averages for the duration of the emissions sampling run for Metals in stack. 

2

 Containerized Waste Feedrate includes the spikes of hexachloroethane, lead nitrate, and mercuric nitrate solution. 

3

 Measured as the SDA (Spray Dryer/Absorber) Outlet Temperature. 

Note: Values in bold used to develop OPL. 

2-10 

VES017700 
Table 2-4. Unit 2 - Summary of Process Data1

 and Feedrates During 

the SW-846 Method 0023A Stack Sampling for Dioxins/Furans 

Operating Parameter Units Basis 

Run l 

10-8-13 

15:40-18:55 

Run 3 

10-10-13 

12:30-15:40 

Run 5 

October 30,2013 

12:45-16:02 

Average Operating Parameter Units Basis 

Max Avg Min Max Avg Min Max Avg M i n Max Avg M i n 

Stack Gas Flowrate ACFM HRA 15,602 15,345 14,862 15,854 15,462 15,126 15,636 15,416 15,038 15,697 15,408 15,009 

Low-Btu Liquid Waste Feedrate lb/hr OMA 2546.4 1470.7 299.8 2,246.8 1,510.2 899.6 2547 1383 1 2,446.8 1,454.7 400.1 

High-Btu Liquid Waste Feedrate lb/hr OMA 1424.2 1286.7 1191.0 1,129.5 1,099.2 1,051.6 1227 1140 973 1,260.1 1,175.2 1,072.0 

Specialty Liquid Waste Feedrate lb/hr OMA 615.4 429.8 0.0 586.1 425.5 307.7 733 445 234 644.7 433.6 180.7 

Containerized Solids Waste Feedrate2 lb/hi 897.9 867.4 874.1 879.8 

Total Waste Feedrate3 lb/hr HRA 4,473.4 4,317.4 4,060.4 4,369.4 4,110.4 2,944.5 4,446.7 4,119.3 3,707.4 4,429.8 4,182.4 3,570.8 

Total Pumpable Waste Feedrate3 lb/hr HRA 3,564.8 3,429.5 3,241.7 3,469.0 3,276.5 2,507.5 3.519.5 3,267.4 2,930.6 3,517.8 3,324.5 2,893.3 

P CC Temperature °F OMA 1,772 1,701 1,622 1,821 1,707 1,594 1,798 1,701 1,608 1,797 1,703 1,608 

SCC Temperature °F OMA 1,958 1,875 1,714 1,962 1,884 1,865 1,899 1,883 1,857 1,940 1,881 1,812 

Baghouse Inlet Temperature4 °F OMA 447 420 392 439 419 399 439 419 394 441 420 395 

CO, Corrected to 7% 0 2 ppmvd OMA 0.00 0.00 0.00 0.00 0.00 0.00 1.62 0.15 0.00 0.54 0.05 0.00 

1

 Process data are the averages for the duration of the emissions sampling run for Dioxins/Furans in stack. 

2

 Containerized Waste Feedrate includes the spikes of hexachloroethane, lead nitrate, and mercuric nitrate solution. 

3

 Total Waste Feedrate and Total Pumpable Waste Feedrate, maximum, average, and minimum, includes the average chromic acid solution feedrate. 

4

 Measured as the SDA (Spray Dryer/Absorber) Outlet Temperature. 

Note: Values in bold used to develop OPL. 

2-11 

VES017701 
Table 2-5. Unit 3 - Summary of Process Data1

 and Feedrates During 

the EPA Method 5 Stack Sampling for PM 

Operating Parameter Units Basis 

Run l 

10-15-13 

13:16 -14:25 

Run 2 

10-16-13 

11:15 -12:25 

Run 3 

10-17-13 

09:50 -10:57 

Average 

Operating Parameter Units Basis 

Max Avg M in Max Avg M in Max Avg M in Max Avg M in 

Stack Gas Flowrate ACFM HRA 15,245 15,167 15,149 15,407 15,279 15,173 15,278 15,064 14,901 15,310 15,170 15,074 

Low-Btu Liquid Waste Feedrate Ib/hr OMA 1,636.3 1,292.9 890.5 1,635.2 955.4 368.1 2,007.3 1,357.6 367.9 1,759.6 1,202.0 542.2 

High-Btu Liquid Waste Feedrate lb/hr OMA 861.1 847.9 833.4 887.5 818.2 742.2 933.0 875.3 810.1 893.8 847.1 795.2 

Specialty Liquid Waste Feedrate lb/hr OMA 395.6 307.9 131.9 381.0 269.1 190.5 791.2 457.4 263.7 522.6 344.8 195.4 

Containerized Solids Waste Feedrate lb/hr OMA 738.3 742.1 720.7 733.7 

Ash Feedrate lb/hr OMA 499.9 510.9 566.5 525.8 

PCC Temperature °F OMA 1,766 1,707 1,650 1,726 1,704 1,684 1,742 1,704 1,614 1,744 1,705 1,649 

SCC Temperature °F OMA 1,899 1,890 1,883 1,895 1,885 1,878 1.902 1,885 1,863 1,899 1,887 1,875 

CO, Corrected to 1% Ch ppmvd OMA 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 

Baghouse Inlet Temperature2 °F OMA 431 420 407 431 421 401 434 420 402 432 420 403 

' Process data are the averages for the duration of the emissions sampling run for particulate matter in stack. 

2

 Measured as the SDA (Spray Dryer/Absorber) Outlet Temperature 

Note: Values in bold used to develop OPL 

2-12 

VES017702 
) 

Table 2-6. Unit 3 - Summary of Process Data1 and Feedrates During 

the Modified EPA Method 26A Stack Sampling for HC1/CI2 

Operating Parameter Units Basis 

Run 2 

10-16-13 

14:00 -15:00 

Run 3 

10-17-13 

12:30 -13:33 

Run 4 

10-18-13 

09:35 -10:35 

Average 

Operating Parameter Units Basis 

Max Avg M i n Max Avg Min Max 

. Ayg.. Min Max Avg Min 

Stack Gas Flowrate acfm HRA 15,547 15,395 15,088 15,360 15,204 14,840 15,228 15,193 15,116 15,378 15,264 15,015 

Low-Btu Liquid Waste Feedrate lb/hr OMA 2,530.5 1,783.5 442.9 2,008.4 1,563.4 0.0 2,231.4 1,725.3 1,261.8 2,256.8 1,690.7 568.2 

High-Btu Liquid Waste Feedrate lb/hr OMA 1,053.0 977.2 926.8 1,212.3 1,151.9 1,039.1 1,263.1 1,163.5 1,003.3 1,176.1 1,097.6 989.7 

Specialty Liquid Waste Feedrate lb/hr OMA 380.9 177.5 87.9 556.8 407.7 322.3 410.3 248.8 146.5 449.3 278.0 185.6 

Containerized Solids Waste Feedrate2 lb/hr 904.4 893.8 861.3 886.5 

Total Chlorine Feedrate lb/to 207.0 206.0 201.0 204.7 

Sorbent Feedrate lb/lb Cl 2 HRA 2.13 1.99 2.13 2.09 

Carrier Fluid Flowrate gal/lb Cl 2 HRA 1.86 1.78 1.88 1.84 

PCC Temperature »F OMA 1,746 1,709 1,675 1,770 1,715 1,691 1,743 1,719 1,694 1,753 1,714 1,686 

SCC Temperature °F OMA 1,909 1,887 1,867 1.931 1,884 1,842 1,923 1,881 1,864 1,921 1,884 1,858 

CO, Corrected to 7% 0 2 ppmvd OMA 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 

Baghouse Inlet Temperature3 °F OMA 430 420 395 433 420 380 429 415 385 431 418 386 

1

 Process data are the averages for the duration of the emissions sampling run for HCI/CI2 in stack. 

2

 Containerized Waste Feedrate includes the spikes of hexachloroethane, lead nitrate, and mercuric nitrate solution. 

3

 Measured as the SDA (Spray Dryer/Absorber) Outlet Temperature. 

Note: Values in bold used to develop OPL. 

2-13 

VES017703 
Table 2-7. Unit 3 - Summary of Process Data1

 and Feedrates During the EPA Method 29 Stack Sampling for Metals 

Operating Parameter Units Basis 

Run 2 

10-16-13 

14:00 -16:50 

Run 3 

10-17-13 

12:30 -15:25 

Run 4 

10-18-13 

09:35-12:20 

Average 

Operating Parameter Units Basis 

Max Avg Min Max Avg Min Max Avg Min Max Avg M in 

Stack Gas Flowrate acfm HRA 15,547 15,274 15,088 15,429 15,230 14,840 15,277 15,133 14,983 15,417 15,212 14,970 

Low-Btu Liquid Waste Feedrate lb/hr OMA 2,531.2 1,787.6 442.9 2,157.8 1,685.3 0.0 2,231.4 1,707.4 1,261.8 2,306.8 1,726.8 568.2 

High-Btu Liquid Waste Feedrate lb/hr OMA 1,114.5 1,043.9 926.8 1,212.3 1,166.5 1,039.1 1,263.1 1,197.7 1,001.3 1.196.6 1,136.0 989.1 

Specialty Liquid Waste Feedrate lb/hr OMA 410.3 202.9 0.0 556.8 350.0 0.0 410.3 244.8 146.5 459.1 265.9 48.8 

Containerized Solids Waste Feedrate2 lb/hr 890.9 888.0 873.6 884.2 

S V M Feedrate lb/hr 62.1 62.5 62.2 62.3 

L V M Feedrate - Total lb/hr 46.3 46.1 45.7 46.1 

L V M Feedrate - Pumpable Ib/hr 46,3 46.1 45.7 46.0 

Mercury Feedrate lb/hr 0.00221 0.00214 0.00227 0.00221 

Total Chlorine Feedrate lb/hr 204.2 204.6 203.7 204.2 

Baghouse Inlet Temperature3 

"F OMA 430 419 395 433 420 380 436 421 385 433 420 386 

PCC Temperature °F OMA 1,752 1,710 1,675 1,770 1,707 1,657 1,743 1,708 1,610 1,755 1,708 1,647 

SCC Temperature °F OMA 1,909 1,885 1,867 1,931 1,885 1,842 1,923 1,886 1,864 1,921 1,885 1,858 

CO, Corrected to 7% 0 2 ppmvd OMA 0.00 0.00 0.00 0.00 o.oo 0.00 0.00 0.00 0.00 0.00 0.00 0.00 

1

 Process data are the averages for the duration of the emissions sampling run for Metals in stack. 

2

 Containerized Waste Feedrate includes the spikes of hexachloroethane, lead nitrate, and mercuric nitrate solution. 

' Measured as the SDA (Spray Dryer/Absorber) Outlet Temperature. 

Note: Values in bold used to develop OPL. 

2-14 

VES017704 
) 

Table 2-8. Unit 3 - Summary of Process Data1 and Feedrates During 

the SW-846 Method 0023A Stack Sampling for Dioxins/Furans 

Operating Parameter Units Basis 

Run 2 

10-161-13 

14:00-17:20 

Run 3 

10-17-13 

12:30 -15:55 

Run 4 

10-18-13 

09:35 -12:50 

Average Operating Parameter Units Basis 

Max Avg Min Max Avg Min Max Avg Min Max Avg Min 

Stack Gas Flowrate ACFM H RA 15,547 15,248 15,088 15,429 15,219 14,840 15,277 15,125 14,983 15,417 15,197 14,970 

Low-Btu Liquid Waste Feedrate lb/hr O MA 2,531.2 1,806.5 442.9 2,157.8 1,688.0 0.0 2,231.4 1,718.8 1,261.8 2,306.8 1,737.7 568.2 

High-Btu Liquid Waste Feedrate lb/hr O MA 1,114.5 1,052.3 926.8 1,212.3 1,167.4 1,039.1 1,263.1 1,188.4 805.7 1,196.6 1,136.0 923.9 

Specialty Liquid Waste Feedrate lb/hr O MA 410.3 199.6 0.0 556.8 340.4 0.0 410.3 246.2 146.5 459.1 262.1 48.8 

Containerized Solids Waste Feedrate2 Ib/hr 887.2 870.5 872.5 876.7 

Total Waste Feedrate3 Ib/hr H RA 4,288.0 4,057.1 2,491.4 4,503.5 4,250.4 2,904.3 4,437.3 4,233.2 3,734.8 4,409.6 4,180.2 3,043.5 

Total Pumpable Waste Feedrate3 lb/hr HRA 3,412.8 3,209.1 2,055.4 3,613.3 3,410.5 2,467.1 3,556.0 3,393.0 3,238.5 3,527.4 3,337.5 2,587.0 

PCC Temperature °F O MA 1,752 1,709 1,675 1,770 1,707 1,657 1,757 1,712 1,610 1,760 1,709 1.647 

SCC Temperature °F O MA 1,909 1,885 1,867 1,931 1,885 1,842 1,923 1,884 1,864 1,921 1,885 1,858 

Baghouse Inlet Temperature4 

°F OMA 430 419 395 433 421 380 436 420 385 433 420 386 

CO, Corrected to 7% Oj ppmvd O MA 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 

1

 Process data are the averages for the duration of the emissions sampling run for Dioxins/Furans in stack. 

2

 Containerized Waste Feedrate includes the spikes of hexachloroethane, lead nitrate, and mercuric nitrate solution. 

3

 Total Waste Feedrate and Total Pumpable Waste Feedrate, maximum, average, and minimum, includes the average chromic acid solution feedrate. 

4

 Measured as the SDA (Spray Dryer/Absorber) Outlet Temperature. 

Note: Values in bold used to develop OPL. 

2-15 

VES017705 
Table 2-9. Unit 4 - Summary of Process Data1

 and Feedrates During 

the EPA Method 5 Stack Sampling for PM 

Operating Parameter Units Basis 

Runl 

10-23-13 

09:30-10:42 

Run 3 

10-25-13 

09:35 -10:40 

Run 4 

10-25-13 

10:50 -11:55 

Average 

Operating Parameter Units Basis 

Max Avg Min Max Avg Min Max Avg Min Max Avg Min 

Stack Gas Flowrate ACFM HRA 37,755 37,632 37,333 37,997 37,824 37,479 37,647 36,949 36,518 37,800 37,468 37,110 

Low-Btu Liquid Waste to Kiln Feedrate lb/hr OMA 2,080.6 1,899.6 1,646.9 2,180.2 1,901.0 1,730.0 1,957.9 1,896.8 1,807.7 2,072.9 1,899.2 1,728.2 

High-Btu Liquid Waste to Kiln Feedrate lb/hr OMA 1,124.8 1,101.4 1,081.3 1,403.2 1,098.1 1,010.0 1,200.5 1,108.9 996.8 1,242.8 1,102.8 1,029.4 

Liquid Waste to SCC Feedrate lb/hr OMA 1,185.5 1,095.6 1,003.0 1,158.5 1,100.7 1,026.9 1,153.8 1,102.8 1,068.8 1,166.0 1,099.7 1,032.9 

Containerized Solids Waste Feedrate lb/hr OMA 565.8 568.6 553.8 562.8 

Bulk Solids Waste Feedrate Ib/hr OMA 6,286.7 6,408.0 5,992.6 6,229.1 

Ash Feedrate Ib/hr O MA 4,806.0 4,835.6 4,689.9 4,777.2 

PCC Temperature °F OMA 1,631 1,591 1,537 1,623 1,574 1,503 1,601 1,559 1,508 1,618 1,575 1,516 

SCC Temperature °F OMA 1,909 1,885 1,866 1,905 1,886 1,863 1,896 1,882 1,870 1,903 1,884 1,866 

CO, Corrected to 7% 02 ppmvd OMA 0.33 0.14 0.00 0.26 0.09 0.00 0.21 0.08 0.00 0.27 0.10 O.OO 

Baghouse Inlet Temperature2 °F O MA 402 398 392 403 397 391 407 401 396 404 399 393 

Carbon Injection Rate lb/hr OMA 6.7 6.2 5.9 6.7 6.2 5.9 7.0 6.2 5.7 6.8 6.2 5.8 

' Process data are the averages for the duration of the emissions sampling run for particulate matter in stack. 

2

 Measured as the SDA (Spray Dryer/Absorber) Outlet Temperature 

Note: Values in bold used to develop OPL 

2-16 

VES017706 
Table 2-10. Unit 4 - Summary of Process Data1

 and Feedrates During 

the Modified EPA Method 26A Stack Sampling for HCI/CI2 

Operating Parameter Units Basis 

Runl 

10-23-13 

12:36 -13:36 

Run 2 

10-24-13 

12:35-13:35 

Run 3 

10-25-13 

13:35 -14:35 

Average Operating Parameter Units Basis 

Max Avg Min Max A V E Min Max Avg Min Max Avg Min 

Stack Gas Flowrate acfm HRA 38,042 37,935 37,857 37,265 37,170 37,063 36,872 36,754 36,572 37,393 37,286 37,164 

Low-Btu Liquid Waste to Kiln Feedrate lb/hr OMA 2,105.9 1,943.7 0.0 2,057.1 1,996.5 1,863.0 2,068.1 1,999.6 1,942.1 2,077.0 1,980.0 1,268.4 

High-Btu Liquid Waste to Kiln Feedrale lb/hr OMA i,224.9 1,167.0 0.0 1,230.8 1,205.4 1,172.2 1,294.3 1,201.0 1,094.0 1,250.0 1,191.2 755.4 

Liquid Waste to SCC Feedrate Ib/hr OMA 1,261.5 1,165.6 0.0 1.240.6 1,203.1 1,126.5 1,238.0 1,196.3 1,171.4 1,246.7 1,188.3 766.0 

Containerized Solids Waste Feedrate2 lb/hr 860.0 857.0 843.0 853.3 

Bulk Solids Waste Feedrate Ib/hr 6,093.0 5,448.0 5739.0 5,760.0 

Total Chlorine Feedrate lb/hr 203.0 203.5 203.2 203.2 

Sorbent Feedrate 

1Mb 

CI2 

HRA 2.23 2.07 2.07 2.13 

Carrier Fluid Flowrate 

Gal/lb 

Cl 2 

HRA 3.16 3.07 3.07 3.10 

PCC Temperature °F OMA 1,635 1,589 1,493 1,623 1,569 1,507 1,567 1,513 1,460 1,609 1,557 1,487 

SCC Temperature °F OMA 1,909 1,883 1,801 1,901 1,880 1,838 1,905 1,878 1,847 1,905 1,880 1,828 

CO, Corrected to 7% O2 ppmvd OMA 0.23 0.08 0.00 0.21 0.06 0.00 0.27 0.09 0.00 0.24 0.08 0.00 

Baghouse Inlet Temperature3 °F OMA 409 398 383 403 399 393 406 400 392 406 399 389 

Carbon Injection Rate lb/hr OMA 6.7 6.0 0.0 6.5 6.2 6.1 6.7 6.2 6.0 6.6 6.1 4.0 

1

 Process data are the averages for the duration of the emissions sampling run for HC1/CI2 in stack. 

2

 Containerized Waste Feedrate includes the spikes of hexachloroethane, lead nitrate, and mercuric nitrate solution. 

3

 Measured as the SDA (Spray Dryer/Absorber) Outlet Temperature. 

Note: Values in bold used to develop OPL. 

2-17 

VES017707 
Table 2-11. Unit 4 - Summary of Process Data1

 and Feedrates During the EPA Method 29 Stack Sampling for Metals 

Operating Parameter Units Basis 

Runl 

10-23-13 

12:36 -15:20 

Run 2 

10-24-13 

12:35 -15:15 

Run 3 

10-25-13 

13:35 -16:11 

Average 

Operating Parameter Units Basis 

Max Avg Min Max Avg Min Max Avg Min Max Avg Min 

Stack Gas Flowrate acfm HRA 38,042 37,659 37,010 37,267 37,087 36,864 38,297 37,199 36,572 37,869 37,315 36,815 

Low-Btu Liquid Waste to Kiln Feedrate lb/hr OMA 2,105.9 1,978.5 0.0 2,113.9 1,986.6 1,711.7 2,072.2 1,999.0 1,939.2 2,097.3 1,988.0 1,217.0 

High-Btu Liquid Waste to Kiln Feedrate lb/hr OMA 1,232.7 1,189.2 0.0 1,239.1 1,201.2 1,159.0 1,340.2 1,201.8 1,094.0 1,270.7 1,197.4 751.0 

Liquid Waste to SCC Feedrate Ib/hr OMA 1,261.5 1,186.2 0.0 1,240.6 1,201.5 1,077.4 1,238.0 1,196.2 1,167.1 1,246.7 1,194.6 748.1 

Containerized Solids Waste Feedrate2 lb/hr 862.7 849.0 856.5 856.1 

Bulk Solids Waste Feedrate lb/hr 5,251.5 5,598.4 5345.0 5,398.3 

SVM Feedrate lb/hr 62.2 61.6 62.2 62.0 

LVM Feedrate - Total lb/hr 46.2 46.3 46.0 46.2 

LVM Feedrate - Pumpable lb/hr 46.0 46.0 45.8 45.9 

Mercury Feedrate lb/hr 0.0402 0.0400 0.0403 0.0402 

Total Chlorine Feedrate Ib/hr 205.3 204.1 205.5 205.0 

Baghouse Inlet Temperature3 «p O MA 409 399 383 409 399 390 410 399 388 410 399 387 

Carbon Injection Rate lb/hr OMA 6.7 6.1 0.0 6.7 6.2 5.9 6.9 6.2 5.9 6.8 6.2 3.9 

PCC Temperature «p OMA 1,666 1,582 1,493 1,623 1,571 1,507 1,602 1,525 1,460 1,631 1,559 1,487 

SCC Temperature °F O MA 1,928 1,885 1,801 1,901 1,879 1,838 1,912 1,879 1,831 1,914 1,881 1,823 

CO, Corrected to 7% 02 ppmvd OMA 0.23 0.08 0.00 0.21 0.06 0.00 0.27 0.08 0.00 0.24 0.07 0.00 

1

 Process data are the averages for the duration of the emissions sampling run for metals in stack. 

2

 Containerized Waste Feedrate includes the spikes of hexachloroethane, lead nitrate, and mercuric nitrate solution. 

3

 Measured as the SDA (Spray Dryer/Absorber) Outlet Temperature. 

Note: Values in bold used to develop OPL. 

2-18 

VES017708 
Table 2-12. Unit 4 - Summary of Process Data1

 and Feedrates During 

the SW-846 Method 0023A Stack Sampling for Dioxins/Furans 

Operating Parameter Units Basis 

Runl 

10-23-13 

12:36 -15:50 

Run 2 

10-24-13 

12:35-15:45 

Run 3 

10-25-13 

13:35 -16:41 

Average Operating Parameter Units Basis 

Max Avg Min Max Avg Min Max Min Max Avg Min 

Stack Gas Flowrate ACFM HRA 38,042 37,547 36,881 37,267 37,028 36,454 38,297 37,325 36,572 37,869 37,300 36,635 

Low-Btu Liquid Waste to Kiln Feedrate lb/hr OMA 2,105.9 1,982.8 0.0 2,113.9 1,950.9 1,711.7 2,072.2 1,998.3 1,939.2 2,097.3 1,977.4 1,217.0 

High-Btu Liquid Waste to Kiln Feedrate lb/hr OMA 1,232.7 1,190.9 0.0 1,239.1 1,201.0 1,159.0 1,340.2 1,200.9 1,094.0 1,270.7 1,197.6 751.0 

Liquid Waste to SCC Feedrate lb/hr OMA 1,261.5 1,187.5 0.0 1,240.6 1,201.3 1,077.4 1,238.0 1,196.9 1,167.1 1,246.7 1,195.2 748.1 

Containerized Solids Waste Feedrate2 lb/hr 862.6 841.6 854.2 852.8 

Bulk Solids Waste Feedrate lb/hr 5,322.4 5,090.8 5,284.2 5,232.5 

Total Waste Feedrate to PCC3 lb/hr HRA 10,621.4 9,551.1 7,192.1 10,662.8 9,512.7 7,097.6 10,610.4 9,407.6 6,913.6 10,631.5 9,490.5 7,067.8 

Total Pumpable Waste Feedrate to PCC3 lb/hr HRA 3,466.7 3,418.2 3,095.1 3,465.0 3,430.7 3,151.6 3,473.2 3,447.0 3,129.6 3,468.3 3,432.0 3.12S.4 

Total Waste Feedrate to SCC (Pumpable) lb/hr HRA 1,201.9 1,184.2 1,078.0 1,207.0 1,197.8 1,082.2 1,199.5 1,192.4 1,077.6 1,202.8 1,191.5 1,079.3 

PCC Temperature °F O MA 1,666 1,580 1,493 1,626 1,575 1,507 1,602 1,527 1,460 1,632 1,561 1,487 

SCC Temperature °F OMA 1,928 1,885 1,801 1.910 1,881 1,838 1,912 1,879 1,831 1,917 1,881 1,823 

Baghouse Inlet Temperature4 °F OMA 410 400 383 409 399 390 413 399 388 411 399 387 

Carbon Injection Rate lb/hr OMA 6.8 6.2 0.0 7.1 6.2 5.9 6.9 6.2 5.9 6.9 6.2 3.9 

CO, Corrected to 7% 0 2 ppmvd OMA 0.23 0.07 0.00 0.21 0.06 0.00 0.27 0.08 0.00 0.24 0.07 0.00 

' Process data are the averages for the duration of the emissions samphng run for Dioxins/Furans in stack. 

2

 Containerized Waste Feedrate includes the spikes of hexachloroethane, lead nitrate, and mercuric nitrate solution. 

3

 Total Waste Feedrate to PCC and Total Pumpable Waste Feedrate to PCC, maximum, average, and minimum, include the average chromic acid solution feedrate. 

4

 Measured as the SDA (Spray Dryer/Absorber) Outlet Temperature. 

Note: Values in bold used to develop OPL. 

2-19 

VES017709 
Table 2-13. Unit 2 - Chlorine Spiking Rates During the HCI/CI2

 Stack Sampling 

Spiking 

Constituent 

Spiking Rate (lbs/hr) 

Spiking 

Constituent Target 

Run 1 

10-8-13 

15:40 -16:40 

Run 3 

10-10-13 

12:30 -13:30 

Run 5 

10-30-13 

12:45 -13:45 

Chlorine 200-250 197.9 203.1 197.9 

Table 2-14. Unit 3 - Chlorine Spiking Rates During the HCI/CI2 Stack Sampling 

Spiking 

Constituent 

Spiking Rate (lbs/hr) I 

Spiking 

Constituent Target 

Run 2 

10-16-13 

14:00 -15:00 

Run 3 

10-17-13 

12:30 -13:33 

Run 4 1 

10-18-13 

09:35-10:35 \ 

Chlorine 200-250 203.1 203.3 197.9 1 

Table 2-15. Unit 4 - Chlorine Spiking Rates During the HCI/CI2 Stack Sampling . 

Spiking 

Constituent 

Spiking Rate (lbs/hr) 

Spiking 

Constituent Target 

Run l 

10-23-13 

12:36 -13:36 

Run 2 

10-24-13 

12:35 -13:35 

Run 3 

10-25-13 

13:35-14:35 

Chlorine 200-250 197.9 197.9 197.9 

2-20 

VES017710 
Table 2-16. Unit 2 - Spiking Rates During the Metals Stack Sampling 

Spiking 

Constituent 

Spiking Rate (lbs/hr) 

Spiking 

Constituent Target 

Runl 

10-8-13 

15:40 -18:43 

Run 3 

10-10-13 

12:30 -15:10 

Run 5 

10-30-13 

12:45 -15:32 

Chromium 40-45 45.8 47.3 45.8 

Lead 60-65 61.9 61.7 62.0 

Mercury 0.001-0.003 0.00196 0.00196 0.00204 

Chlorine 200 - 250 199.7 199.2 200.2 

Table 2-17. Unit 3 - Spiking Rates During the Metals Stack Sampling 

Spiking 

Constituent 

Spiking Rate (lbs/hr) 

Spiking 

Constituent Target 

Run 2 

10-16-13 

14:00 -16:50 

Run 3 

10-17-13 

12:30 -15:25 

Run 4 

10-18-13 

09:35 -12:20 

I Chromium 

40-45 46.3 46,1 45.7 

I Lead 

60-65 62.1 62.5 62.2 

j iVlercury 

0.001-0.003 0.00204 0.00200 0.00209 

Chlorine 200 - 250 200.3 201.7 200.7 

Table 2-18. Unit 4 - Spiking Rates During the Metals Stack Sampling 

Spiking 

Constituent 

Spiking Rate (lbs/hr) 

Spiking 

Constituent Target 

Run l 

10-23-13 

12:36 -15:20 

Run 2 

10-24-13 

12:35 -15:15 

Run 3 

10-25-13 

13:35 -16:11 

Chromium 40-45 46.0 46.0 45.8 

Lead 60-65 62.0 61.1 62.0 

Mercury 0.02-0.06 0.0393 0.0388 0.0394 

Chlorine 200 - 250 200.0 197.2 200.3 

2-21 
Table 2-19. Unit 2 - Analytical Results for the Chromium Spiking Solution 

Chromium 

Run 1 Run 3 Run 5 

Chromium 

COA 

Concentration 

Analytical 

Result 

COA 

Concentration 

Analytical 

Result 

COA 

Concentration 

Analytical 

Result Chromium 

(mg/kg) (mg/kg) (mg/kg) 

Beginning of Method 29 Sample 

178,881 

178,000 

178,871 

178,000 

178,881 

174,000 

Middle of Method 29 Sample 178,881 172,000 178,871 174,000 178,881 173,000 

End of Method 29 Sample 

178,881 

169,000 

178,871 

178,000 

178,881 

170,000 

Table 2-20. Unit 2 - Analytical Results for the Mercury Spiking Solution 

Mercury 

Runl Run 3 Run 5 

Mercury 

Calculated 

Concentration 

Analytical 

Result 

Calculated 

Concentration 

Analytical 

Result 

Calculated 

Concentration 

Analytical 

Result Mercury 

(lig/rol) (mg/kg) (pg/ml) (mg/kg) (lig/ml) (mg/kg) 

Beginning of Method 29 Sample 

2,323 

1,960 

2,323 

2,370 

2,323 

2,210 

Middle of Method 29 Sample 2,323 2,050 2,323 2,150 2,323 2,120 

End of Method 29 Sample 

2,323 

2,390 

2,323 

1,950 

2,323 

2,250 

2-22 

VES017712 
Table 2-21. Unit 3 - Analytical Results for the Chromium Spiking Solution 

Chromium 

Run 2 Run 3 Run 4 

Chromium 

COA 

Concentration 

Analytical 

Result 

COA 

Concentration 

Analytical 

Result 

COA 

Concentration 

Analytical 

Result Chromium 

(mg/kg) (mg/kg) (mg/kg) 

Beginning of Method 29 Sample 

179,137 

176,000 

179,137 

176,000 

179,137 

176,000 

Middle of Method 29 Sample 179,137 173,000 179,137 179,000 179,137 172,000 

End of Method 29 Sample 

179,137 

177,000 

179,137 

174,000 

179,137 

173,000 

Table 2-22. Unit 3 - Analytical Results for the Mercury Spiking Solution 

Mercury 

Run 2 Run 3 Run 4 

Mercury 

Calculated 

Concentration 

Analytical 

Result 

Calculated 

Concentration 

Analytical 

Result 

Calculated 

Concentration 

Analytical 

Result Mercury 

(Ug/ml) (mg/kg) (ug/ml) (mg/kg) (ug/ml) (mg/kg) 

Beginning of Method 29 Sample 

2,323 

2,420 

2,323 

2,460 

2,323 

2,480 

Middle of Method 29 Sample 2,323 2,380 2,323 2,390 2,323 2,500 

End of Method 29 Sample 

2,323 

2,380 

2,323 

2,480 

2,323 

2,480 

2-23 

VES017713 
Table 2-23. Unit 4 - Analytical Results for the Chromium Spiking Solution 

Chromium 

Runl Run 2 Run 3 

Chromium 

COA 

Concentration 

Analytical 

Result 

COA 

Concentration 

Analytical 

Result 

COA 

Concentration 

Analytical 

Result Chromium 

(mg/kg) (mg/kg) (mg/kg) 

Beginning of Method 29 Sample 

179,137 

171,000 

179,137 

173,000 

179,009 

169,000 

Middle of Method 29 Sample 179,137 175,000 179,137 172,000 179,009 172,000 

End of Method 29 Sample 

179,137 

169,000 

179,137 

174,000 

179,009 

176,000 

Table 2-24. Unit 4 - Analytical Results for the Mercury Spiking Solution 

Mercury 

Runl Run 2 Run 3 

Mercury 

Calculated 

Concentration 

Analytical 

Result 

Calculated 

Concentration 

Analytical 

Result 

Calculated 

Concentration 

Analytical 

Result Mercury 

(Ug/ml) (mg/kg) (ug/ml) (mg/kg) (Mg/ml) (mg/kg) 

Beginning of Method 29 Sample 

23,228 

21,300 

23,228 

19,700 

23,228 

22,000 

Middle of Method 29 Sample 23,228 18,700 23,228 19,900 23,228 21,300 

End of Method 29 Sample 

23,228 

19,300 

23,228 

21,000 

23,228 

21,400 

2-24 

VES017714 
3.0 Sampling, Analysis, and Monitoring Procedures 

The subsequent CPT was performed at one test condition on each of the three incinerators 

to demonstrate system performance and to establish appropriate operating parameter limits 

(OPLs) for all of the applicable standards of the HWC MACT. The CPT included three replicate 

sampling runs on each incinerator at the one test condition. Table 3-1 summarizes the parameters 

that were measured during the test of each of the three incinerators and the frequency of 

measurement. The CPT was conducted in accordance with the comprehensive performance test 

plans for Units 2,3, and 4 (i.e. the CPT Plan) and Quality Assurance Project Plan (QAPjP) dated 

September 25, 2013 that were approved by EPA Region 5. 

3.1 Sampling Locations and Procedures 

Samples were collected of solid, liquid, and gas streams during the CPT. Table 3-2 

summarizes the sampling methods for each stream and the parameters that were determined. 

Refer to the QAPjP for more detailed descriptions of the methods and the quality control 

activities for each method. Section 5.0 presents a discussion of the QA/QC activities performed 

for the CPT. 

3.1.1 Liquids Sampling Procedures 

Samples ofthe liquid waste feeds were collected every 15 minutes during each ofthe 

three runs of the CPT for each of the three incinerators beginning at the start of stack 

sampling through completion of stack sampling for both the first and second parts of the CPT. 

Individual samples (i.e., sub-samples) were collected every 15 minutes throughout the test, 

and composited for analysis. 

Samples ofthe liquid waste feeds were collected at 15-minute intervals during the 

collection of the Method 5 sampling train of the first part of each run of the test, and during 

the collection of the Modified Method 26A, Method 29, and Method 0023A sampling trains 

of the second part of each run of the test. Composite samples were prepared of the samples 

collected during each of the Method 5, Modified Method 26A, Method 29, and Method 

0023A sampling times. All of the composite liquid waste feed samples from the first part and 

the second part of the CPT were analyzed for ash, total chlorine, heat content, moisture, density, 

and viscosity. The composite liquid waste feed samples collected during the Method 29 stack 

sampling were also analyzed for metals (arsenic, beryllium, chromium, cadmium, lead, and 

mercury). 

3-1 
In addition to the collection of sub-samples every 15 minutes of the liquid wastes, 

individual samples were collected and archived for further analysis, if required. 

Samples ofthe chromium and mercury spiking solutions were collected in each run of 

the second part of the test of each incinerator. At the beginning, middle (at port change), and 

end of the Method 29 sampling of the second part of the test, samples of the chromium and 

mercury spiking solutions were collected. The individual samples of the chromium and 

mercury spiking solutions collected during each Method 29 sampling run ofthe test of each 

incinerator were analyzed for chromium or mercury, respectively. A fourth sample of the 

chromium and mercury spiking solutions was collected at the completion of the Method 

O023A sampling train. This fourth sample was archived (i.e., not analyzed). 

Liquid waste samples were collected upstream of any metal spiking location. Split 

samples of the composite liquid waste feed and the chromium and mercury spiking solutions from 

one run were taken by the Illinois EPA and/or U.S. EPA Region 5. 

3-2 

VES017716 
Table 3-1. Measurement Frequency 

— ^ ' ^ 

Sample Frequency for 

Stream/Parameters 

the Subsequent CPT 

First Part Second Part 

Liquid Waste Feed 

Ash 3 3 

Chlorine •'3 3 

Moisture 3 3 

Heating Value 3 3 

Viscosity, Density 3 3 

Metals 3' 

Solid Waste Feed - Containerized and Bulk (Unit 4) 

Ash 3 3 

Chlorine 3 3 

Moisture 3 3 

Heating Value 3 3 

Metals 3' 

Spiking Materials2 

Mercury Spiking Solution 3 

Lead Solid Spiking Material 3 

Chromium Spiking Solution 3 

Chlorine Solid Spiking Material (if spiked) 3 

Stack Gas 

Metals 3

1 

Particulate Matter 3 

HCl/Cl 2 

3 

Dioxins/Furans 3 

C 0 2 ) 0 2 Continuous Continuous3 

1 Total Hydrocarbons Continuous3 

Moisture Concurrent with Concurrent with 

isokinetic sampling isokinetic sampling 

CO, 0 2

4 Continuous Continuous 

1

 Analysis is for As, Be, Cd, Cr, Pb, and Hg. 

2

 Each collected sample ofthe mercury and chromium spiking solutions were analyzed for the target spiking 

metal. Samples ofthe lead and chlorine spiking materials were archived. 

3

 Allowing for hourly calibration of the THC monitor. 

4

 Plant monitors. 
Table 3-2. Sampling Methods 

Stream Sampling Method Sampling Frequency 

Compositing 

Approach 

Analytical 

Parameters 

Liquid Waste Feed 

Units 2 and 3 

Low-Btu 

- High-Btu 

Liquid 

(Specialty) 

Waste 

Unit 4 

Low-Btu to 

Kiln 

High-Btu to 

Kiln 

Liquid Waste 

to SCC 

Tap 

(Method S004) 

First part of the test 

condition - Every 15 

Minutes During 

Method 5 sampling 

Second part of the test 

condition - Every 15 

Minutes During 

Modified Method 

26A, Method 29, and 

Method 0023A 

sampling 

Subsamples from 

each test period 

composited 

Ash 

Chlorine 

Moisture 

Heating Value 

Density 

Viscosity 

Metals1 

Solid Waste Feed 

Units 2 and 3 

Containerized 

XInit4 

Containerized 

• Bulk 

Grab or Scoop 

(Method S007)~ Solids 

First part of the test 

condition - Every 15 

Minutes During 

Method 5 samphng 

Second part of the test 

condition - Every 15 

Minutes During 

Modified Method 

26A, Method 29, and 

Method 0023A 

sampling 

Subsamples from 

each test period 

composited 

Ash 

Chlorine 

Moisture 

Heating Value 

Metals1 

Chromium Spiking 

Solution 

Tap 

(Method SOW) 

Second part of the test 

condition - Beginning, 

middle, and end of 

Method 29 sampling 

End of Method 0023A 

sampling 

Subsamples 

collected during 

Method 29 sampling 

analyzed 

Subsample collected 

at end of Method 

0023A sampling 

archived 

Chromium 

Mercury Spiking 

Solution 

Grab 

Second part of the test 

condition - Beginning, 

middle, and end of 

Method 29 sampling 

End of Method 0023A 

sampling 

Subsamples 

collected during 

Method 29 sampling 

analyzed 

Subsample collected 

at end of Method 

0023A sampling 

archived 

Mercury 

3-4 

VES017718 
Table 3-2. (continued) Sampling Methods 

Stream Sampling Method Sampling Frequency 

Compositing 

Approach 

Analytical 

Parameters 

Lead and Chlorine 

Spiking Materials 

Grab 

Second part of the test 

condition - Beginning, 

middle, and end of 

Method 29 sampling 

End of Method 0023A 

sampling 

None - Archive Archive 

Stack Gas 

EPA Method 2 

Concurrent with 

isokinetic sampling for 

EPA Methods 5, 29, 

and SW-846 Melhod 

0023A 

NR Flowrate 

Stack Gas 

EPA Method 3A 

Concurrent with 

isokinetic sampling -

First and Second Parts 

of the Test 

NR 02

, C0 2 

Stack Gas 

EPA Method 4 

Concurrent with 

isokinetic samphng -

First and Second Parts 

ofthe Test 

NR Moisture 

Stack Gas 

EPA Method 5 1+hour collected 

isokinetically - First 

Part of the Test 

NR PM 

Stack Gas 

Modified EPA Method 26A 

1+ hour collected 

isokinetically at single 

point - Second Part of 

the Test 

NR HC1/C12 

Stack Gas 

EPA Method 29 

2+ hour collected 

isokinetically - Second 

Part of the Test 

NR Metals

 1 

Stack Gas 

SW-846 Method 0023A 

3+ hour collected 

isokinetically - Second 

Part of the Test 

NR Dioxins/Furans 

Stack Gas 

EPA Method 25A 

Concurrent with 

isokinetic sampling -

Second Part of the 

Test 

NR THC 

Stack Gas 

Plant CEMS Continuous NR CO,0 2 

Analysis for As, Be, Cd, Cr, Pb, and Hg only in samples from the second part of the test condition collected during Method 

29 stack samphng. 

NR = Not Required 

3-5 

VES017719 
3.1.2 Solids Sampling Procedures 

Samples of the containerized solid waste feed fed to Units 2, 3, and 4, and the bulk 

solids fed to Unit 4, were collected every 15 rninutes during the collection of the Method 5 

sampling train of the first part of each run of the test, and during the collection of the 

Modified Method 26A, Method 29, and Method 0023A sampling trains of the second part of 

each run of the test. Composite samples were prepared of the samples collected during each 

ofthe Method 5, Modified Method 26A, Method 29, and Method 0023A sampling times. All 

of the composite solid waste feed samples from the first part and the second part of the CPT 

were analyzed for ash, total chlorine, heat content, and moisture. The composite solid waste feed 

samples collected during the Method 29 stack samphng were also analyzed for metals (arsenic, 

beryllium, chromium, cadmium, lead, and mercury). 

In addition to the collection of sub-samples every 15 minutes of the solid wastes, 

individual samples were collected and archived for further analysis, if required. 

Spikes of solid lead and chlorine were added to the containerized solid waste in the test of 

each incinerator. Samples of the lead (as lead nitrate) and the chlorine (as hexachloroethane) were 

collected during the Method 29 stack sampling in the second part of the test. Three grab samples of 

the chlorine and lead spiking materials were collected at the beginning, middle (at port change), 

and end of the Method 29 sampling of the second part of the test. A fourth sample of the lead and 

chlorine spiking materials was collected at the completion of the Method 0023A sampling train in 

the second part of the test. All samples ofthe lead and chlorine spiking materials were archived 

(i.e., not analyzed). Samples of the composite solid waste feeds and the chlorine and lead spiking 

solutions from one run were taken by the Illinois EPA and/or U.S. EPA Region 5. 

3.1.3 Stack Gas Sampling Procedures 

Stack gas emissions were sampled for determination of the parameters indicated in 

Tables 5-1 and 5-2. The stack samples collected using isokinetic sampling methods were 

particulate matter by EPA Method 5, HCI and Ch using a Modified Method 26A, metals by EPA 

Method 29, and dioxins/furans by SW-846 Method 0023A. Table 3-3, Table 3-4, and Table 3-5 

present summaries of the sampling data for the isokinetic samplmg trains for the CPT testing of 

Unit 2, Unit 3, and Unit 4, respectively. 

3-6 
Table 3-3. Unit 2 - Summary of Isokinetic Sampling 

Run Analytical Parameter Date Time 

Average 

Stack 

Temperature 

CF) 

Velocity 

(ft/sec) 

Flue Gas 

Moisture 

<%) 

o2 

(vol %) 

co2 

(vol %) 

Avg 

Flowrate 

(acfm) 

Avg 

Flowrate 

(dscfm) 

Volume 

at Meter 

(dscf) 

Isokinetic 

Sampling 

Rate 

{•%) 

1 

PM 

10-8-13 

11:50-13:00 390 30.50 41.2 11.56 6.35 14,796 5,395 40.815 97.9 

1 

HC1/C12 

10-8-13 

15:40-16:40 391 29.97 45.1 10.08 7.95 14,537 4,942 37.384 103.5 

1 

Metals 

10-8-13 

15:40-18:43 389 31.41 45.5 10.08 7.95 15,235 5,156 84.952 107.1 

1 

Dioxins/Furans 

10-8-13 

15:40-18:55 387 30.05 44.7 10.08 7.95 14,578 5,017 121.164 104.6 

2 PM 10-9-13 09:45-10:53 390 31.07 41.6 11.23 6.56 15,070 5,451 42.356 100.5 

3 

PM 

10-10-13 

09:15-10:23 391 30.42 42.0 11.48 6.28 14,753 5,287 41.278 101.0 

3 

HCI/C12 

10-10-13 

12:30-13:30 396 31.95 45.9 10.38 7.50 15,498 5,150 37.290 99.0 

3 

Metals 

10-10-13 

12:30-15:10 393 31.36 45.8 10.38 7.50 15,212 5,081 78.951 101.0 

3 

Dioxins/Furans 

10-10-13 

12:30-15:40 396 32.05 45.3 10.38 7.50 15,544 5,225 119.568 99.1 

5 

HC1/C12 

10-30-13 

12:45-13:45 392 31.21 43.8 10.50 7.25 15,138 5,225 36.879 96.1 

5 Metals 10-30-13 12:45-15:32 386 31.06 43.8 10.50 7.25 15,064 5,236 79.607 97.9 

Dioxins/Furans 

10-30-13 

12:45-16:02 389 33.10 42.9 . 10.50 7.25 16,056 5,650 124.921 95.3 

3-7 

VES017721 
\ 

Table 3-4. Unit 3 - Summary of Isokinetic Sampling 

Run Analytical Parameter Date Time 

Average 

Stack 

Temperature 

(°F) 

Velocity 

(ft/sec) 

Flue Gas 

Moisture 

(%) 

(vol %) 

co2 

(vol %) 

Avg 

Flowrate 

(acfm) 

Avg 

Flowrate 

(dscfm) 

Volume 

at Meter 

(dscf) 

Isokinetic 

Sampling 

Rate 

(%) 

I P M 10-15-13 13:16-14:25 365 29.94 38.3 12.87 5.31 14,523 5,675 41.229 98.9 

2 

P M 

10-16-13 

11:15-12:25 366 30.75 36.2 13.38 4.96 14,916 6,034 42.461 96.2 

2 

HC1/C12 

10-16-13 

14:00-15:00 368 30.98 41.6 11.19 6.88 15,028 5,542 36.088 101.6 

2 

Metals 

10-16-13 

14:00-16:50 367 30.68 43.5 11.19 6.88 14,882 5,319 71.708 103.6 

2 

Dioxins/Furans 

10-16-13 

14:00-17:20 367 30.92 42.9 11.19 6.88 14,996 5,420 106.303 102.5 

3 

P M 

10-17-13 

09:50-10:57 368 30.66 41.0 11.74 6.02 14,870 5,549 41.921 103.3 

3 

HCI/C12 

10-17-13 

12:30-13:33 366 30.35 43.2 10.72 7.36 14,721 5,293 34.597 101.9 

3 

Metals 

10-17-13 

12:30-15:25 367 30.22 44.5 10.72 7.36 14,658 5,150 69.016 102.9 

3 

Dioxins/Furans 

10-17-13 

12:30-15:55 367 30.72 44.4 10.72 7.36 14,901 5,248 102.724 102.3 

4 

HC1/C12 

10-18-13 

09:35-10:35 368 32.06 43.4 10.87 7.26 15,549 5,579 35.241 98.5 

4 Metals 10-18-13 09:35-12:20 368 31.52 44.1 10.87 7.26 15,292 5,414 71.540 101.5 

Dioxins/Furans 

10-18-13 

09:35-12:50 368 30.59 43.7 10.87 7.26 14,839 5,290 102.624 101.4 

3-8 

VES017722 
I 

Table 3-5. Unit 4 - Summary of Isokinetic Sampling 

Run Analytical Parameter Date Time 

Average 

SUck 

Temperature 

(°F) 

Velocity 

(ft/sec) 

Flue Gas 

Moisture 

(%) 

o2 

(vol %) 

co2 

(vol %) 

Avg 

Flowrate 

(acfm) 

Avg 

Flowrate 

(dscfm) 

Volume 

at Meter 

(dscf) 

Isokinetic 

Sampling 

Rate 

(%) 

1 

PM 

10-23-13 

09:30-10:42 - 374 57.55 39.4 12.22 5.59 43,275 16,483 38.181 97.9 

1 

HC1/C12 

10-23-13 

12:36-13:36 377 60.30 39.6 12.27 5.86 45,345 17,157 39.935 99.1 

1 

Metals 

10-23-13 

12:36-15:20 371 57.26 39.7 12.27 5.86 43,061 16,382 76.068 100.1 

1 

Dioxins/Furans 

10-23-13 

12:36-15:50 370 55.12 39.2 12.27 5.86 41,455 15,919 110.791 100.7 

2 

HC1/C12 

10-24-13 

12:35-13:35 377 57.91 38.6 12.37 5.74 43,550 16,824 39.264 99.3 

2 Metals 10-24-13 12:35-15:15 370 57.72 38.6 12.37 5.74 43,410 16,917 76.498 97.5 

Dioxins/Furans 

10-24-13 

12:35-15:45 370 55.32 38.3 12.37 5.74 41,598 16,284 112.803 100.3 

3 

PM 

10-25-13 

09:35-10:40 372 57.35 38.7 12.48 5.45 43,126 16,847 39.691 100.3 

3 

HC1/C12 

10-25-13 

13:35-14:35 378 54.66 39.3 12.00 5.96 41,102 15,796 37.034 99.8 

3 

Metals 

10-25-13 

13:35-16:11 373 57.94 39.8 12.00 5.96 43,575 16,723 76.846 99.1 

3 

Dioxins/Furans 

10-25-13 

13:35-16:41 374 56.95 39.3 12.00 5.96 42,829 16,550 115.284 100.8 

4 PM 10-25-13 10:50-11:55 374 54.52 39.5 12.11 5.71 40,998 15,768 36.759 100.5 

3-9 

VES017723 
3.1.3.1 Sample Port Location 

The Unit 2 and Unit 3 stacks are 90-feet high and have an inside diameter of 39 inches. 

There are two sets of two orthogonal ports located at two slightly different levels. Only the upper 

set of orthogonal ports are suitable for, and were used for, isokinetic sampling. An additional 

port located about four feet below the upper orthogonal ports, and about 45° between the 

orthogonal ports, was used for the Modified Method 26A samphng for HCI/CI2. The number of 

sampling points for the isokinetic sampling by Method 5, Method 29, and Method 0023A was 

determined in accordance with EPA Method 1. 

The Unit 4 stack is 100-feet high and has an inside diameter of 48 inches. There are four 

orthogonal ports located at one level. An additional port located about four feet below the upper 

orthogonal ports, and about 45° between the orthogonal ports, was used for the Modified Method 

26A sampling for HC1/C12. The number of sampling points for the isokinetic sampling by 

Method 5, Method 29, and Method 0023A was determined in accordance with EPA Method 1. 

3.1.3.2 EPA Methods 2 and 4 (Flowrate and Moisture) 

Concurrent with the performance of the isokinetic samphng trains, measurements were 

made to detennine gas velocity by 40 CFR Part 60, Appendix A, Method 2, and moisture by 

Method 4. The absence of cyclonic flow was determined by performing a cyclonic flow check, 

prescribed in EPA Method 2, prior to the CPT testing of each incinerator. 

3.1.3.3 EPA Method 5 (PM) 

Samples for the determination of particulate matter (PM) in stack emissions were 

collected in the first part of the tests of each incinerator using EPA Method 5. This sample train 

consisted of the following components: 

• Glass (quartz) nozzle; 

• Heated, glass (quartz)-lined probe; 

• Heated filter with a Teflon filter support; 

• Optional empty knockout impinger; 

• Modified Greenburg-Smith impinger containing 100 mL of DI water; 

• Greenburg-Smith impinger containing 100 mL of DI water; 

• Empty Modified Greenburg-Smith impinger; and 

• Modified Greenburg-Smith impinger containing silica gel. 

The procedures specified in EPA Method 5 protocol were used to determine particulate matter. 

These procedures require the isokinetic extraction of particulate matter on a filter maintained at a 

controlled temperature between 223°F and 273°F. The particulate mass includes the mass 

3-10 
determined gravimetrically in the probe and nozzle rinse (PNR) with acetone, after evaporation 

and desiccation, and filter after desiccation. 

3.1.3.4 Modified EPA Method 26A (HCI/CI2) 

During the second part of the test of each incinerator, samples for the determination of 

HC17C12 in stack emissions were collected using a modification of EPA Method 26A proposed 

and approved by EPA Region 5. This sample train consisted of the following components: 

• Glass (quartz) nozzle; 

• Heated, glass (quartz)-lined probe; 

• Heated Teflon mat filter with a Teflon® filter support; 

• Teflon® transfer line; 

• Optional empty knockout impinger; 

• Greenburg-Smith impinger containing 100 mL of 0.1 N H2SO4; 

• Greenburg-Smith impinger containing 100 mL of 0.1 N H2SO4; 

• Modified Greenburg-Smith impinger containing 100 mL of 0.1 N NaOH; 

• Modified Greenburg-Smith impinger containing 100 mL of 0.1 N NaOH; and 

• Modified Greenburg-Smith impinger containing silica gel. 

The procedures specified in EPA Method 5, as referenced in EPA Method 26A, were used for 

the isokinetic collection of the sample except that the sample was collected at a single point 

located at the center of the stack. A Teflon® union was used to connect the glass or quartz nozzle 

to the glass or quartz probe liner, and the filter and probe were kept at a temperature between 

248°F and 273°F. A Teflon®-backed filter was used, as specified in EPA Method 26A. 

3.1.3.5 EPA Method 29 (Metals) 

Samples of the stack gas emissions were collected for the determination of metals during 

the second part of the test of each incinerator. The stack gas samples were collected 

isokinetically for the HWC MACT metals As, Be, Cd, Cr, Pb, and Hg using Method 29 from 40 

CFR Part 60, Appendix A. 

This method is basically an EPA Method 5 sampling train with some very specific 

modifications: 

• Glass nozzle; 

• Heated, glass-lined probe; 

• Heated filter; 

3-11 
• Teflon transfer line; 

• Empty modified Greenburg-Smith impinger; 

• Modified Greenburg-Smith impinger containing 100 mL of 5% HNO3 and 10% 

H2 02; 

• Greenburg-Smith impinger containing 100 mL of 5% HNO3 and 10% H2 02; 

• Empty modified Greenburg-Smith impinger; 

• Modified Greenburg-Smith impinger containing 100 mL of 4% KMn04 and 10% 

H2S04; 

• Modified Greenburg-Smith impinger containing 100 mL of 4% KMn04 and 10% 

H2S04; and 

• Modified Greenburg-Smith impinger containing silica gel. 

A Teflon® transfer line was used between the filter and the first impinger. This is done to address 

space limitations on the stack, to allow for ease in probe moving, and to minimize potential 

hazards moving the very large and heavy impinger box. 

Following sampling, the probe and nozzle of the sampling train were recovered using a 

brash containing no metal using 0.1 normal nitric acid. 

3.1.3.6 SW-846 Method 0023A (Dioxins/Furans) 

Stack gas emissions were sampled isokinetically for dioxins/furans in the second part of 

the test of each incinerator using SW-846 Method 0023A. 

The sampling train consists ofthe following components: 

• Glass nozzle; 

• Heated, glass-lined probe; 

• Heated filter; 

• Heated Teflon® transfer line; 

• Sorbent module; 

• Knock-out impinger; 

• Greenburg-Smith impinger containing 100 mL water; 

• Modified Greenburg-Smith impinger containing 100 mL water; and 

• Modified Greenburg-Smith impinger containing silica gel. 

From the heated filter, sample gas was passed through a heated Teflon® transfer line before 

entering the sorbent module. The sorbent module consisted of a water-cooled condenser and a 

3-12 

VES017726 
resin trap containing XAD-2 resin. The condenser is used to ensure that the gas entering the 

resin trap is below 68°F. 

Isotopically-labeled dioxins/furans were spiked onto the XAD-2® resin both before field 

sampling (surrogate standards) and into appropriate places in the preparation prior to analysis 

after returning from the field. 

3.1.3.7 Continuous Emissions Monitoring (THC, C02 , CO and 02) 

CEMs were used to monitor the concentrations of total hydrocarbons (THC), carbon 

dioxide (C02), carbon monoxide (CO), and oxygen (O2) in the stack gas. 

CO, corrected to 7% 0 2 is reported for the stack gases from permanent installation CEMS 

on each of the three incinerators. The concentrations of THC, C02, and 0 2 in the stack gas were 

determined using EPA Methods 25A and 3A, respectively. CO2 and 0 2 were monitored using 

Method 3A to determine the stack gas composition (i.e., molecular weight) used to determine the 

flowrate of the stack gas, and to correct the stack sampling results to 7% oxygen. Both of these 

methods utilize continuous monitors. 

3.2 Analysis Procedures 

Samples collected during the CPT were analyzed for the parameters specified in 

Table 3-6. All analyses were performed by Test America Laboratories in Knoxville, TN. 

Analytical results for the waste feed samples are reported on an as-received or wet weight basis. 

Samples of the waste feed were not dried prior to analysis. 

Table 3-6. Summary of Analytical Methods 

Parameter Stream Analytical Method 

Moisture Stack Gas EPA Method 4 

Metals 

Waste Feeds, Spiking 

Solutions, Stack Gas 

ICPES - SW-846 Method 6010B 

CVAAS - Hg, SW-846 Method 7470A 

or 7471A 

PM Stack Gas Gravimetric - EPA Method 5 

HCUC\2 

Stack Gas IC-EPA Method 26A 

Dioxins/Furans Stack Gas HRGC/MS - SW-846 Method 8290A 

Composition/Physical Parameters Waste Feeds EPA and/or ASTM Standard Methods 

3-13 
3.2.1 Composition and Physical Parameters Analysis 

Samples of the waste feeds will be collected for determination of a number of chemical 

and physical parameters. Samples of the waste feeds were analyzed for the following parameters, 

by the referenced standard methods: 

• Ash-ASTM Method ASTM D-482; 

• Total Chlorine - SW-846 Methods 5050 and 9056A; 

• Moisture - ASTM Method E-203 or D-4017(Karl-Fischer titration) for liquid waste, 

and ASTM Method D-5142 or D-160.3 (loss on drying) for solid waste; 

• Calorific Value - ASTM Method D-5865 or D-240; 

• Density - ASTM Method D-1475; and 

• Viscosity - ASTM Method D-445. 

3.2.2 Metals Analysis 

Waste feed samples were analyzed for metals using a trace level inductively coupled 

argon plasma emission spectroscopy (ICPES) and atomic absorption spectroscopy. Samples were 

prepared for analysis using SW-846 Method 3050B. The metals analyzed by ICPES (SW-846 

Method 6010B) are arsenic (As), beryllium (Be), cadmium (Cd), chromium (Cr), and lead (Pb). 

Mercury (Hg) was analyzed using Method 7471A of SW-846. Spiking solutions of chromium 

and mercury were analyzed for chromium and mercury, respectively. 

The Method 29 sampling train used to collect samples of the stack gas for metals was 

analyzed using ICPES according to SW-846 Method 6010B for arsenic (As), beryllium (Be), 

cadmium (Cd), chromium (Cr), and lead (Pb), and mercury was analyzed using Method 7470A 

of SW-846. 

3.2.3 PM Analysis 

The PM concentration of the stack gas was determined following 40 CFR 60, Appendix 

A, Method 5 protocols. The wash from the nozzle, probe liner, and glassware prior to the filter 

(PNR) ofthe sampling train was evaporated, and the mass determined on an analytical balance. 

Tie filter recovered from the samphng train was desiccated, and weighed to determine the mass 

of particulate on the filter. The combined mass from the filter and the evaporated wash are used 

with the total volume of gas sampled to determine the particulate loading. 

3.2.4 HCI/CI2 Analysis 

The sulfuric acid and sodium hydroxide impinger catches and rinses from the Modified 

Method 26A sampling trains were analyzed for chloride ion concentrations using the analytical 

3-14 
approach specified in Method 26A. The Modified Method 26A sampling train was recovered to 

provide a rinse of the transfer line and contents and rinses of the acidic impingers (and knockout 

impinger) for determination of hydrogen chloride; and the contents and rinses of the alkaline 

impingers for determination of chlorine. Both were analyzed for chloride by ion chromatography 

(IC) for determination of chloride. The chloride found in the acid impingers (and rinses) is 

reported as HCI, and the chloride determined in the alkaline impingers (and rinses) is reported as 

Ch. Sodium thiosulfate was added to the collected alkaline impinger samples in the analytical 

laboratory before analysis. 

3.2.5 Dioxins/Furans Analysis 

Samples ofthe stack gas were collected using SW-846 Method 0023A, and were 

analyzed for dioxins/furans using SW-846 Method 8290A, high resolution gas chromatography 

(HRGC) with high resolution mass spectroscopy (HRMS) analytical technique. The analytical 

protocol includes quantitation of all dibenzodioxins and dibenzofurans including four or more 

chlorine atoms. The method provides congener class definition for each of the five congener 

groups (tetra-, penta-, hexa-, hepta-, and octa-). In addition, each individual isomer containing 

the 2,3,7,8-substitution pattern was individually quantified. 

Dioxins/furans concentrations are reported for: 

• Combination of the filter and all the rinses between the nozzle and filter; and 

• Combination of the sorbent and all the rinses between the filter and sorbent. 

3.3 Process Monitoring Procedures 

The incinerator systems are monitored to ensure operation is in accordance with the 

pennitted conditions. During the performance test, the automatic waste feed cutoff systems were 

operational; however, AWFCO limits in the current NOC were adjusted or disabled during the 

performance testing periods to allow target operations to be achieved. The CPT Plan prescribed a 

Continuous Monitoring System Performance Evaluation Test for each of the three incinerators. 

The Continuous Monitoring System Performance Evaluation Test Reports (CMSPETR) for the 

three incinerators are included as Appendix D. The raw process monitoring data from the CPT 

testing of each of the three incinerators are presented in Appendix C. 

3-15 

VES017729 
4.0 Results 

This section presents the results of the comprehensive performance test of Veolia's 

incinerators at Sauget. The analytical results for the waste feed streams and stack gas are 

presented in Sections 4.1 and 4.2. The collection of samples and the methods used for sampling 

and analysis are specified in the CPT Plan and QAPjP. 

Note that values presented in these tables (and throughout the report) are rounded to 

display an appropriate level of significance. All calculations are done with unrounded values, 

and therefore, it may not be possible to reproduce a calculated value exactly from the data shown 

in a table. It may be necessary to go to earlier tables, or the raw data in the appendices, to 

reproduce a calculated value exactly. 

4.1 Waste Feedstreams 

Four waste streams were sampled and analyzed in both the first part and the second part 

of each run of the CPT tests of Units 2 and 3, three liquid waste streams and one solid waste 

stream. All are fed to the primary combustion chamber (PCC). The streams sampled and 

analyzed are: 

• Low-Btu Liquid Waste; 

• High Btu Liquid Waste; 

• Liquid (Specialty) Waste; and 

• Containerized Solid Waste. 

Five waste streams were sampled and analyzed in both the first part and the second part 

of each run of the CPT test of Unit 4, three liquid waste streams and two solid waste streams 

including two liquid wastes and two solid wastes that were fed to the kiln (i.e., the primary 

combustion chamber - PCC), and one liquid waste that was fed to the secondary combustion 

chamber (SCC). The streams sampled and analyzed are: 

• Low-Btu Liquid Waste to Kiln; 

• High Btu Liquid Waste to Kiln; 

• Containerized Solid Waste; 

• Bulk Solid Waste; and 

• Liquid Waste to the SCC. 

Composite samples were prepared of the samples collected during each ofthe Method 5 

sampling time in the first part of each test, and the Modified Method 26A, Method 29, and 

4-1 
Method 0023A sampling times of the second part of each test. All ofthe composite liquid 

waste feed samples from the first part and the second part of the CPT tests were analyzed for 

ash, total chlorine, heat content, moisture, density, and viscosity. All of the composite solid 

waste feed samples from the first part and the second part of the CPT tests were analyzed for 

ash, total chlorine, heat content, and moisture. The composite liquid and solid waste feed 

samples collected during the Method 29 stack sampling were also analyzed for metals (arsenic, 

beryllium, chromium, cadmium, lead, and mercury). 

Each sample was given a unique log number that identifies the project and unit, run 

nurnber, and an identification code based upon the sample type and fraction. An example ofthe 

log number format follows: 

Proj-XY-ABC 

Where: 

Proj is a project specific identification; 

XY represent the condition and run number; and 

ABC is an alphanumeric sequence describing the particular sample. 

Here is a description of the sample codes used for the waste samples in the CPT. 

VS2 (Veolia Sauget and unit number 2, 3, or 4) - Stream Code - Test 

Condition/Run Number/Part A or B - Sample Description 

Stream Codes: 

LWF = Liquid Waste Feed (to SCC Unit 4) 

HBW = High-Btu Liquid Waste (to Kiln Unit 4) 

LBW = Low-Btu Liquid Waste (to Kiln Unit 4) 

CS = Containerized Solids (solids material sampled from the box containers) 

BS = Bulk Solids (Unit 4 only) 

CL Chlorine Spiking Material (samples of the chlorine spiking material 

from the box containers) 

PB = Lead Spiking Material (samples of the lead salts contained in the box 

containers) 

HG = Mercury Spiking Material (samples of the vials containing the mercury 

spiking solution in the box containers) 

CR Chromium Spiking Solution 

4-2 

VES017731 
Test Condition/Run Number/Part A or B: 

Test Condition is "1" for all samples and all runs. 

Run Numbers typically are 1,2,& 3, however additional runs performed to replace 

aborted and/or repeated runs continue in sequence, 4, 5, etc. 

Part A refers to the test segment associated with the PM emissions testing (i.e., 

the first part of the test). 

Part B refers to the test segment associated with the HCI/CI2, Metals, and 

Dioxins/Furans emissions testing (i.e., the second part of the test). 

Sample Description; 

Waste and spiking material samples included individual grab samples for 

archiving, and composite samples specific to each emissions test period. 

These are labeled as follows: 

Individual grab samples are labeled with the suffix as: 

-Grab 1, -Grab 2, -Grab 3, etc. in sequential order. 

Composite samples were collected during each emissions sampling period and are 

represented by the following ID suffix: 

COMP1 = Composite sample collected during the PM emissions test 

period 

COMP2A = Composite sample collected during the HCI/CI2 emissions 

test period 

COMP2B = Composite sample collected during the Metals emissions 

test period 

COMP2C = Composite sample collected during the dioxins/furans 

emissions test period 

Note that there should not be any COMP2A, B, or C samples labeled with a " -

xxA-" run number, nor should there be any COMP1 samples with a "-xxB-" run 

number. 

Examples: 

VS2-HBW-15B-Grab 4 is the 4t h grab sample of High-Btu liquid waste collected 

for archive during Run 5-Part B on Unit 2. 

VS3-LWF-12A-COMP1 is the composite sample of the liquid waste feed 

collected for analysis during PM emissions Run 2 test period (Part A) on Unit 

3. 

Table 4-1 presents the analytical results for chlorine, ash, metals, heat content, moisture, 

density, and viscosity in the Low-Btu Liquid Waste fed to Unit 2. 

Table 4-2 presents the analytical results for chlorine, ash, metals, heat content, moisture, 

density, and viscosity in the High-Btu Liquid Waste fed to Unit 2. 

4-3 

VES017732 
Table 4-3 presents the analytical results for chlorine, ash, metals, heat content, moisture, 

density, and viscosity in the Specialty Liquid Waste fed to Unit 2. 

Table 4-4 presents the analytical results for chlorine, ash, metals, heat content, and 

moisture in the Containerized Solid Waste fed to Unit 2. 

Table 4-5 presents the analytical results for chlorine, ash, metals, heat content, moisture, 

density, and viscosity in the Low-Btu Liquid Waste fed to Unit 3. 

Table 4-6 presents the analytical results for chlorine, ash, metals, heat content, moisture, 

density, and viscosity in the High-Btu Liquid Waste fed to Unit 3. 

Table 4-7 presents the analytical results for chlorine, ash, metals, heat content, moisture, 

density, and viscosity in the Specialty Liquid Waste fed to Unit 3. 

Table 4-8 presents the analytical results for chlorine, ash, metals, heat content, and 

moisture in the Containerized Solid Waste fed to Unit 3. 

Table 4-9 presents the analytical results for chlorine, ash, metals, heat content, moisture, 

density, and viscosity in the Low-Btu Liquid Waste fed to the kiln (PCC) of Unit 4. 

Table 4-10 presents the analytical results for chlorine, ash, metals, heat content, moisture, 

density, and viscosity in the High-Btu Liquid Waste fed to the kiln (PCC) of Unit 4. 

Table 4-11 presents the analytical results for chlorine, ash, metals, heat content, moisture, 

density, and viscosity in the Liquid Waste fed to the SCC of Unit 4. 

Table 4-12 presents the analytical results for chlorine, ash, metals, heat content, and 

moisture in the Containerized Solid Waste fed to Unit 4. 

Table 4-13 presents the analytical results for chlorine, ash, metals, heat content, and 

moisture in the Bulk Solid Waste fed to Unit 4. 

The detailed analytical reports are presented in Appendix Gl . 

4-4 

VES017733 
Table 4-1. Unit 2 - Analytical Results for Chlorine, Ash, Metals, and Physical Parameters in the Low-Btu Liquid Waste Feed 

Analytical Parameter Units 

Runl Run 2 Run 3 Run 5 

Analytical Parameter Units 1 

PM 

2A 

HC1/CI2 

2B 

Metals 

2C 

Dioxins/ 

Furans 

1 

PM 

1 

PM 

2A 

HCI/C12 

2B 

Metals 

2C 

Dioxins/ 

Furans 

2A 

HC1/C12 

2B 

Metals 

2C 

Dioxins/ 

Furans 

Chlorine mg/kg 345 340 347 363 346 374 404 364 393 340 357 372 

Ash mg/kg 3,140 2,940 2,970 2,990 2,960 3,250 3,860 3,180 3,130 3,130 3,100 2,940 

Arsenic mg/kg N A NA 2.7 NA NA NA NA 3.2 NA NA 2.1 NA 

Beryllium mg/kg NA NA <0.097 NA NA NA NA <0.096 NA NA <0.097 NA 

Cadmium mg/kg N A NA 7.2 NA NA NA NA 9.0 NA NA 7.0 NA 

Chromium mg/kg NA NA 0.8 NA NA NA NA 0.88 NA NA 0.74 NA 

Lead mg/kg N A NA 1.1 NA NA NA NA 1.7 NA NA 1.1 NA 

Mercury mg/kg N A NA 0.021 NA NA NA NA 0.042 NA NA 0.052 NA 

Percent Water % 98.1 98.0 98.2 98.3 97.9 98.4 97.5 96.6 98.2 99.9 99.0 99.2 

Heating Value Btu/lb <130 <130 <130 <130 <130 <130 <130 <130 <130 <130 178 <130 

Density g/m3 1.000 1.000 1.000 1.000 0.999 1.000 0.999 1.000 1.000 0.999 1.000 1.000 

Viscosity cSt 0.934 0.939 0.930 0.934 0.930 0.930 0.932 0.932 0.933 0.928 0.929 0.927 

4-5 

VES017734 
Table 4-2. Unit 2 - Analytical Results for Chlorine, Ash, Metals, and Physical Parameters in the High-Btu Liquid Waste Feed 

Analytical Parameter Units 

Run l Run 2 Run 3 Run 5 

Analytical Parameter Units 1 

P M 

2A 

HCI/C12 

2B 

Metals 

2C 

Dioxins/ 

Furans 

1 

P M 

1 

P M 

2A 

HC1/C12 

2B 

Metals 

2C 

Dioxins/ 

Furans 

2A 

HCl/Ck 

2B 

Metals 

2C 

Dioxins/ 

Furans 

Chlorine mg/kg 7,070 6,960 7,140 7,240 7,180 3,780 3,260 3,210 3,330 3,500 3,580 3,450 

Ash mg/kg 1,350 1,030 1,100 1,040 1,010 1,180 557 582 551 2,080 1,210 1,350 

Arsenic mg/kg NA NA 8.3 NA NA NA NA 2.8 NA NA <0.32 NA 

Beryllium mg/kg NA NA <0.096 NA NA NA NA <0.099 NA NA <0.096 NA 

Cadmium mg/kg NA NA <0.076 NA NA NA NA <0.078 NA NA <0.076 NA 

Chromium mg/kg NA NA 0.26 NA NA NA NA <0.22 NA NA <0.21 NA 

Lead mg/kg NA NA 1.0 N A NA NA NA 0.67 NA NA 6.7 NA 

Mercury mg/kg NA NA 0.026 NA NA NA NA 0.021 NA NA 0.096 NA 

Percent Water % 22.1 21,9 22.1 21.9 21.8 20.6 20.0 20.2 20.3 27.6 28.1 27.8 

Heating Value Btu/lb 9,090 9,000 9,040 9,050 9,040 9,120 9,160 9,130 9,150 8,630 8,630 8,660 

Density g/m3 0.880 0.879 0.880 0.878 0.879 0.875 0.868 0.869 0.869 0.883 0.883 0.883 

Viscosity cSt 1.31 1.30 1.29 1.29 1.28 1.19 1.18 1.18 1.17 1.60 1.62 1.60 

4-6 

VES017735 
Table 4-3. Unit 2 - Analytical Results for Chlorine, Ash, Metals, and Physical Parameters in the Specialty Liquid Waste Feed 

Analytical Parameter Units 

Runl Run 2 Run 3 Run 5 

Analytical Parameter Units 1 

PM 

2A 

HC1/C12 

2B 

Metals 

2C 

Dioxins/ 

Furans 

1 

PM 

1 

PM 

2A 

HC1/C12 

2B 

Metals 

2C 

Dioxins/ 

,_ Furans 

2A 

HCI/C12 

2B 

Metals 

2C 

Dioxins/ 

Furans 

Chlorine mg/kg 91.8 105 159 156 140 111 130 124 130 106 92.4 108 

Ash mg/kg 649 600 575 1,010 599 598 657 592 579 904 832 832 

Arsenic mg/kg N A N A <0.32 N A N A N A N A <0.3 N A N A <0.31 N A 

Beryllium mg/kg N A N A <0.096 N A N A N A N A <0.092 N A N A <0.093 N A 

Cadmium mg/kg N A N A <0.076 N A N A N A N A <0.073 N A N A <0.073 N A 

Chromium mg/kg N A N A <0.21 N A N A N A N A <0.2 N A N A <0.2 N A 

Lead mg/kg N A N A <0.27 N A N A N A N A <0.26 N A N A <0.26 N A 

Mercury mg/kg N A N A <0.009 N A N A N A N A <0.0086 N A N A <0.0099 N A 

Percent Water % 98.1 98.2 98.2 99.0 98.8 98.4 98.5 98.7 98.3 101.0 101.0 100.0 

Heating Value Btu/lb <130 <130 <130 <130 <130 <130 <130 <130 <130 <130 <130 <130 

Density g/m3 0.998 0.998 0.999 1.000 0.997 0.998 0.997 0.997 0.997 0.997 0.998 0.998 

Viscosity cSt 0.897 0.894 0.894 0.896 0.897 0.900 0.895 0.897 0.897 0.906 0.907 0.91 

4-7 

VES017736 
Table 4-4. Unit 2 - Analytical Results for Chlorine, Ash, Metals, and 

Physical Parameters in the Containerized Solids Waste Feed 

Analytical Parameter Units 

Runl Run 2 Run 3 Run 5 

Analytical Parameter Units 1 

PM 

2A 

HC1/C12 

2B 

Metals 

2C 

Dioxins/ 

Furans 

1 

PM 

1 

PM 

2A 

HCI/C12 

2B 

Metals 

2C 

Dioxins/ 

Furans 

2A 

HCVOz 

2B 

Metals 

2C 

Dioxins/ 

Furans 

Chlorine mg/kg 288 184 167 237 284 433 345 499 267 346 396 351 

Ash mg/kg 675,000 785,000 708,000 676,000 688,000 655,000 657,000 634,000 637,000 732,000 688,000 703,000 

Arsenic mg/kg N A N A 8.8 N A N A N A N A 7.5 N A N A 8.8 N A 

Beryllium mg/kg N A N A 0.48 N A N A N A N A 0.61 N A N A 0.73 N A 

Cadmium mg/kg N A N A 0.082 N A N A N A N A <0.077 N A N A 0.084 N A 

Chromium mg/kg N A N A 12.8 N A N A N A N A 19.3 N A N A 16.7 N A 

Lead mg/kg N A N A 11.6 N A N A N A N A 11.7 N A N A 13.5 N A 

Mercury mg/kg N A N A 0.045 N A N A N A N A 0.022 N A N A 0.016 N A 

Percent Water % 20.2 23.4 21.7 24.5 26.2 24.9 25.2 25.1 25.1 22.6 25.4 20.8 

Heating Value Btu/lb <130 <130 <130 <130 <130 <130 <130 <130 <130 <130 <130 <130 

Density g/m3 N A N A N A N A N A N A N A N A N A N A N A N A 

Viscosity cSt N A N A N A N A N A N A N A N A N A N A N A N A 

4-8 

VES017737 
Table 4-5. Unit 3 - Analytical Results for Chlorine, Ash, Metals, and Physical Parameters in the Low-Btu Liquid Waste Feed 

Analytical Parameter Units 

Run l R u n 2 R u n 3 R o n 4 

Analytical Parameter Units 1 

P M 

1 

P M 

2A 

HC1/CI 2 

2B 

Metals 

2C 

Dioxins/ 

Furans 

1 

P M 

2A 

HC1/C12 

2B 

Metals 

2C 

Dioxins/ 

Furans 

2A 

HC1/C12 

2B 

Metals 

2C 

Dioxins/ 

Furans 

Chlorine mg/kg 409 440 563 419 408 427 409 429 400 388 408 424 

Ash mg/kg 3,090 4,070 4,860 3,700 3,280 3,650 3,200 3,200 3,000 2,940 3,460 3,100 

Arsenic mg/kg N A N A N A 4.8 N A N A N A 3.2 N A N A 3.3 N A 

Beryllium mg/kg N A N A N A <0.096 N A N A N A <0.097 N A N A <0.096 N A 

Cadmium mg/kg N A N A N A 15.2 N A N A N A 9.4 N A N A 11.3 N A 

Chromium mg/kg N A N A N A 1.3 N A N A N A 0.87 N A N A 0.97 N A 

Lead mg/kg N A N A N A 3.1 N A N A N A 1.9 N A N A 1.9 N A 

Mercury mg/kg N A N A N A 0.065 N A N A N A 0.049 N A N A 0.08 N A 

Percent Water % 101.0 99.8 99.3 99.8 100.0 98.2 99.3 100.0 99.2 99.7 99.5 99.9 

Heating Value Btu/lb <130 173 361 256 158 462 209 181 213 154 <130 132 

Density g/m3 1.000 1.000 1.000 1.000 0.999 1.000 1.000 1.000 1.000 1.000 1.010 1.000 

Viscosity cSt 0.932 0.931 0.933 0.932 0.935 0.935 0.940 0.933 0.937 0.935 0.932 0.934 

4-9 

VES017738 
Table 4-6. Unit 3 - Analytical Results for Chlorine, Ash, Metals, and Physical Parameters in the High-Btu Liquid Waste Feed 

Analytical Parameter Units 

Runl Run 2 Run 3 Run 4 

Analytical Parameter Units 1 

PM 

1 

PM 

2A 

HC1/C13 

2B 

Metals 

2C 

Dioxins/ 

Furans 

1 

PM 

2A 

HC1/C12 

2B 

Metals 

2C 

Dioxins/ 

Furans 

2A 

HC1/C12 

2B 

Metals 

2C 

Dioxins/ 

Furans 

Chlorine mg/kg 3,450 2,410 2,460 2,720 2,430 1,730 1,690 1,650 1,620 1,910 1,810 1,830 

Ash mg/kg 1,260 937 1,100 1,160 730 599 478 586 648 734 693 730 

Arsenic mg/kg N A N A N A 12.4 N A N A N A 1.7 N A N A 2.4 N A 

Beryllium mg/kg N A N A N A <0.095 N A N A N A <0.1 N A N A <0.096 N A 

Cadmium mg/kg N A N A N A <0.075 N A N A N A <0.079 N A N A <0.076 N A 

Chromium mg/kg N A N A N A <0.21 N A N A N A <0.22 N A N A <0.21 N A 

Lead mg/kg N A N A N A 1.8 N A N A N A 1.0 N A N A 1.3 N A 

Mercury mg/kg N A N A N A 0.027 N A N A N A 0.029 N A N A 0.022 N A 

Percent Water % 24.0 23.9 23.9 24.1 24.0 23.3 23.0 23.0 23.1 25.2 25.2 25.4 

Heating Value Btu/lb 8,680 8,820 8,700 8,700 8,800 8,840 8,870 8,790 8,860 8,550 8,620 8,560 

Density g/m3 0.879 0.878 0.877 0.877 0.878 0.874 0.874 0.873 0.874 0.879 0.879 0.880 

Viscosity cSt 1.33 1.30 1.30 1.31 1.30 1.28 1.26 1.27 1.26 1.35 1.35 1.36 

4-10 

VES017739 
Table 4-7. Unit 3 - Analytical Results for Chlorine, Ash, Metals, and Physical Parameters in the Specialty Liquid Waste Feed 

Analytical Parameter Units 

Run l R u n 2 R u n 3 R u n 4 

Analytical Parameter Units 1 

P M 

1 

P M 

2A 

HC1/CI 2 

2B 

Metals 

2C 

Dioxins/ 

Furans 

1 

P M 

2A 

HC1/C12 

2B 

Metals 

2C 

Dioxins/ 

Furans 

2A 

HC1/C12 

2B 

Metals 

2C 

Dioxins/ 

Furans 

Chlorine mg/kg 188 174 1,480 696 587 111 101 125 112 113 127 92 

Ash mg/kg 591 622 917 713 733 588 520 520 521 648 620 606 

Arsenic mg/kg N A N A N A <0.32 N A N A N A <0.32 N A N A <0.33 N A 

Beryllium mg/kg N A N A N A <0.098 N A N A N A <0.096 N A N A <0.099 N A 

Cadmium mg/kg N A N A N A <0.077 N A N A N A <0.076 N A N A <0.078 N A 

Chromium mg/kg N A N A N A <0.22 N A N A N A <0.21 N A N A <0.22 N A 

Lead mg/kg N A N A N A <0.27 N A N A N A <0.27 N A N A <0.28 N A 

Mercury mg/kg N A N A N A <0.0088 N A N A N A <0.0094 N A N A <0.0099 N A 

Percent Water % 98.4 97.7 97.3 98.7 95.8 97.9 97.2 98.4 96.2 97.1 99.2 97.1 

Heating Value Btu/lb <130 <130 <130 <130 <130 <130 <130 <130 <130 <130 <130 <130 

Density g/m3 0.998 1.000 1.000 0.999 1.000 0.999 0.997 0.997 0.998 1.000 1.000 1.000 

Viscosity cSt 0.901 0.904 0.898 0.903 0.897 0.897 0.899 0.901 0.899 0.898 0.898 0.897 

4-11 

VES017740 
Table 4-8. Unit 3 - Analytical Results for Total Chlorine, Ash, Metals, and 

Physical Parameters in the Containerized Solids Waste Feed 

Analytical 

Parameter 

Units 

Runl Run 2 Run 3 Run 4 

Analytical 

Parameter 

Units 1 

P M 

1 

PM 

2A 

HCl/Clj 

2B 

Metals 

2C 

Dioxins/ 

Furans 

1 

PM 

2A 

HC1/C12 

2B 

Metals 

2C 

Dioxins/ 

Furans 

2A 

HCI/CI2 

2B 

Metals 

2C 

Dioxins/ 

Furans 

Chlorine mg/kg 253 229 482 195 129 347 115 271 204 382 255 297 

Ash mg/kg 670,000 682,000 663,000 775,000 737,000 778,000 655,000 715,000 682,000 721,000 686,000 698,000 

Arsenic mg/kg N A N A N A 7.5 N A N A N A 6.4 N A N A 8.4 N A 

Beryllium mg/kg N A N A N A 0.58 N A N A N A 0.55 N A N A 0.79 N A 

Cadmium mg/kg N A N A N A <0.071 N A N A N A <0.076 N A N A <0.071 N A 

Chromium mg/kg N A N A N A 13.6 N A N A N A 13.7 N A N A 18.9 N A 

Lead mg/kg N A N A N A 11.1 N A N A N A 10.7 N A N A 14.1 N A 

Mercury mg/kg N A N A N A 0.028 N A N A N A 0.028 N A N A 0.026 N A 

Percent 

Water 

% 18.2 15.8 22.5 27.4 22.0 28.7 20.8 25.0 19.0 27.5 24.8 22.6 

Heating 

Value 

Btu/lb <130 <130 <130 <130 <130 <130 <130 <130 <130 <130 <130 <130 

Density g/m3 N A N A N A N A N A N A N A N A N A N A N A N A 

Viscosity cSt N A N A N A N A N A N A N A N A N A N A N A N A 

4-12 

VES017741 
V 

Table 4-9. Unit 4 - Analytical Results for Chlorine, Ash, Metals, and 

Physical Parameters in the Low-Btu Liquid Waste Feed to the Kiln 

Analytical Parameter Units 

Runl Run 2 Run 3 Run 4 

Analytical Parameter Units 1 

PM 

2A 

HC1/C12 

2B 

Metals 

2C 

Dioxins/ 

Furans 

2A 

HCVCl2 

2B 

Metals 

2C 

Dioxins/ 

Furans 

1 

PM 

2A 

HCI/C12 

2B 

Metals 

2C 

Dioxins/ 

Furans 

1 

PM 

Chlorine mg/kg 472 416 413 449 467 393 422 537 486 532 439 530 

Ash mg/kg 2,790 2,910 3,100 2,570 3,060 3,260 2,940 3,320 3,220 2,630 3,260 3,250 

Arsenic mg/kg N A N A 5.5 N A N A 4.9 N A N A N A 2.9 N A N A 

Beryllium mg/kg N A N A <0.094 N A N A <0.098 N A N A N A <0.096 N A N A 

Cadmium mg/kg N A N A 13.6 N A N A 12.1 N A N A N A 9.4 N A N A 

Chromium mg/kg N A N A 1.3 N A N A 1.2 N A N A N A 0.84 N A N A 

Lead mg/kg N A N A 3.3 N A N A 2.9 N A N A N A 1.6 N A N A 

Mercury mg/kg N A N A 0.11 N A N A 0.14 N A N A N A 0.11 N A N A 

Percent Water % 98.8 97.3 97.7 97.0 96.5 95.8 97.3 97.1 98.1 98.6 96.9 98.8 

Heating Value Btu/lb <130 <130 <130 <130 <130 157 166 <130 197 <130 283 402 

Density g/m3 0.999 1.000 1.000 0.999 0.999 1.000 1.000 1.000 1.000 0.999 1.000 0.999 

Viscosity cSt 0.934 0.939 0.929 0.933 0.928 0.933 0.929 0.932 0.930 0.932 0.932 0.932 

4-13 

VES017742 
Table 4-10. Unit 4 - Analytical Results for Chlorine, Ash, Metals, and 

Physical Parameters in the High-Btu Liquid Waste Feed to the Kiln 

Analytical Parameter Units 

Run 1 Run 2 Run 3 Run 4 

Analytical Parameter Units 1 

PM 

2A 

HC1/CI2 

2B 

Metals 

2C 

Dioxins/ 

Furans 

2A 

HCI/C12 

2B 

Metals 

2C 

Dioxins/ 

Furans 

1 

PM 

2A 

HC1/C12 

2B 

Metals 

2C 

Dioxins/ 

Furans 

1 

PM 

Chlorine mg/kg 1,470 1,450 1,490 1,420 1,390 1,360 1,360 1,350 1,360 1,350 1,350 1,330 

Ash mg/kg 1,610 2,350 2,110 1,820 898 1,010 1,020 1,500 973 931 1,020 989 

Arsenic mg/kg N A N A 1.4 N A N A 0.37 N A N A N A <0.32 N A N A 

Beryllium mg/kg N A N A <0.099 N A N A <0.093 N A N A N A <0.097 N A N A 

Cadmium mg/kg N A N A 0.12 N A N A <0.073 N A N A N A <0.077 N A N A 

Chromium mg/kg N A N A 0.24 N A N A <0.2 N A N A N A <0.21 N A N A 

Lead mg/kg N A N A 1.1 N A N A 0.4 N A N A N A <0.27 N A N A 

Mercury mg/kg N A N A 0.048 N A N A 0.021 N A N A N A 0.018 N A N A 

Percent Water % 24.0 24.3 24.0 23.8 25.0 24.9 24.5 25.2 24.8 25.1 24.7 24.8 

Heating Value Btu/lb 8,740 8,700 8,690 8,750 8,780 8,760 8,730 8,760 8,790 8,750 8,780 8,810 

Density g/m3 0.876 0.877 0.876 0.877 0.877 0.877 0.877 0.877 0.877 0.878 0.877 0.877 

Viscosity cSt 1.29 1.28 1.28 1.29 1.37 1.37 1.37 1.38 1.36 1.37 1.36 1.36 

4-14 

VES017743 
Table 4-11. Unit 4 - Analytical Results for Chlorine, Ash, Metals, and 

Physical Parameters in the Liquid Waste Feed to the SCC 

Analytical Parameter Units 

Runl Run 2 Run 3 Run 4 

Analytical Parameter Units 1 

PM 

2A 

HC1/CI2 

2B 

Metals 

2C 

Dioxins/ 

Furans 

2A 

HCI/C12 

2B 

Metals 

2C 

Dioxins/ 

Furans 

1 

PM 

2A 

HC1/C12 

2B 

Metals 

2C 

Dioxins/ 

Furans 

1 

PM 

Chlorine mg/kg 1,250 1,230 1,250 1,210 1,260 2,500 1,240 1,270 1,280 1,250 1,280 1,320 

Ash mg/kg 744 511 485 478 694 673 672 787 651 604 591 743 

Arsenic mg/kg N A N A <0.3 N A N A <0.32 N A N A N A <0.31 N A N A 

Beryllium mg/kg N A N A <0.092 N A N A <0.098 N A N A N A <0.094 N A N A 

Cadmium mg/kg N A N A <0.073 N A N A <0.077 N A N A N A <0.074 N A N A 

Chromium mg/kg N A N A <0.2 N A N A <0.22 N A N A N A <0.21 N A N A 

Lead mg/kg N A N A 0.26 N A N A <0.27 N A N A N A <0.26 N A N A 

Mercury mg/kg N A N A 0.017 N A N A 0.019 N A N A N A 0.017 N A N A 

Percent Water % 27.0 26.5 26.5 26.2 26.9 26.7 27.0 26.8 26.6 25.6 26.6 26.9 

Heating Value Btu/lb 8,830 8,810 8,790 8,810 8,760 8,800 8,760 8,780 8,860 8,860 8,870 8,830 

Density g/m3 0.879 0.878 0.878 0.878 0.879 0.878 0.877 0.879 0.877 0.878 0.878 0.878 

Viscosity cSt 1.54 1.52 1.52 1.52 1.53 1.52 1.52 1.52 1.52 1.52 1.51 1.52 

4-15 

VES017744 
Table 4-12. Unit 4 - Analytical Results for Chlorine, Ash, Metals, and 

Physical Parameters in the Containerized Solids Waste Feed 

Analytical Parameter Units 

Runl Run 2 Run 3 Run 4 

Analytical Parameter Units 1 

PM 

2A 

HCl/Clj 

2B 

Metals 

2C 

Dioxins/ 

Furans 

2A 

HC1/C12 

2B 

Metals 

2C 

Dioxins/ 

Furans 

1 

PM 

2A 

HCI/CI2 

2B 

Metals 

2C 

Dioxins/ 

Furans 

1 

PM 

Chlorine mg/kg 176 192 190 167 205 201 257 227 207 180 271 244 

Ash mg/kg 758,000 828,000 739,000 728,000 728,000 731,000 745,000 724,000 749,000 730,000 719,000 771,000 

Arsenic mg/kg N A N A 2.4 N A N A 2.0 N A N A N A 2.1 N A N A 

Beryllium mg/kg N A N A 0.13 N A N A 0.16 N A N A N A <0.1 N A N A 

Cadmium mg/kg N A N A 0.46 N A N A 0.43 N A N A N A 0.45 N A N A 

Chromium mg/kg N A N A 45.2 N A N A 58.9 N A N A N A 35.1 N A N A 

Lead mg/kg N A N A 35.9 N A N A 212 N A N A N A 25.4 N A N A 

Mercury mg/kg N A N A 0.18 N A N A 0.24 N A N A N A 0.26 N A N A 

Percent Water % 7.64 8.10 6.75 9.10 7.93 8.29 7.82 9.88 8.11 7.94 9.31 6.31 

Heating Value Btu/lb <130 <130 <130 <130 <130 <130 <130 <130 <130 <130 <130 <130 

Density g/m3 N A N A N A N A N A N A N A N A N A N A N A N A 

Viscosity cSt N A N A N A N A N A N A N A N A N A N A N A N A 

4-16 

VES017745 
\ 

/ 

Table 4-13. Unit 4 - Analytical Results for Chlorine, Ash, Metals, and Physical Parameters in the Bulk Solids Waste Feed 

Analytical Parameter Units 

Runl Run 2 Ran 3 Run 4 

Analytical Parameter Units 1 

PM 

2A 

HCI / a 2 

2B 

Metals 

2C 

Dioxins/ 

Furans 

2A 

HC1/C12 

2B 

Metals 

2C 

Dioxins/ 

Furans 

1 

PM 

2A 

HC1/C12 

2B 

Metals 

2C 

Dioxins/ 

Furans 

1 

PM 

Chlorine mg/kg 171 184 219 265 257 243 236 193 191 173 182 164 

Ash mg/kg 695,000 646,000 715,000 784,000 770,000 720,000 674,000 689,000 729,000 737,000 695,000 710,000 

Arsenic mg/kg N A N A 2.2 N A N A 3.0 N A N A N A 2.2 N A N A 

Beryllium mg/kg N A N A 0.21 N A N A 0.28 N A N A N A 0.26 N A N A 

Cadmium mg/kg N A N A 0.28 N A N A 0.37 N A N A N A 0.30 N A N A 

Chromium mg/kg N A N A 35.6 N A N A 37.9 N A N A N A 29.8 N A N A 

Lead mg/kg N A N A 41.0 N A N A 58.1 N A N A N A 26.6 N A N A 

Mercury mg/kg N A N A 0.082 N A N A 0.12 N A N A N A 0.077 N A N A 

Percent Water % 14.2 18.8 10.3 11.6 16.6 19.2 19.9 13.3 19.3 17.3 15.6 24.7 

Heating Value Btu/lb <130 <130 <130 <130 <130 <130 <130 <130 <130 <130 <130 <130 

Density g/m3 N A N A N A N A N A N A N A N A N A N A N A N A 

Viscosity cSt N A N A N A N A N A N A N A N A N A N A N A N A 

4-17 

VES017746 
4.2 Stack Gas 

Samples of stack gas were collected for deterrnination of the following analytical 

parameters: 

• PM; 

• HC1/C12; 

• Metals; and 

• Dioxins/Furans. 

The stack gas concentration of the test parameters reported as the average of three test 

runs are used to document compliance. Stack gas concentration for a parameter may include 

analytical results for multiple components. For the determination of stack gas concentration 

measured in an individual sample, or run, for those sampling systems as applicable (other than 

SW-846 Method 0023A), the following convention is used to sum the results of multiple 

analyses: 

• In cases where all analytical results are hits (i.e., not "non-detects"), all analytical 

results will be summed. 

• In cases where all analytical results are "non-detects," all method detection limits will 

be summed, and the summed result reported as a maximum ("<"). 

• In cases where one or more analytical results are hits, and one or more analytical 

results are "non-detects," the hits and the "non-detects" will be summed and reported 

as a maximum ("<"). 

Example calculations of the HWC MACT emission limits for PM, HC1/C12, metals, 

dioxins/furans, and THC showing the calculations performed for a reported result are presented 

following the respective table. 

4.2.1 PM in Stack Gas 

Stack gas samples for determination of PM were collected according to EPA Method 5. 

These samples were analyzed gravimetrically for PM according to EPA Method 5. Two samples 

were recovered from each train for the determination of PM. They were as follows: 

• An acetone rinse of the probe and nozzle (PNR), and; 

• Filter (FILT). 

4-18 
The results for PM are presented in Table 4-14 for Unit 2, Table 4-15 for Unit 3, and 

Table 4-16 for Unit 4. The concentration of oxygen measured using CEMS and EPA Method 3 A 

during the collection of the EPA Method 5 samples are shown in the tables, and the 

concentration of PM in the stack gas corrected to 7% 0 2 is shown. 

The analytical results for the determination of PM are included in Appendix G4. 

Table 4-14. Unit 2 - Results of PM in Stack Gas 

Date 

Time 

Runl 

10-8-13 

11:50-13:00 

Run 2 

10-9-13 

09:45-10:53 

Run 3 

10-10-13 

09:15-10:23 

Volume Collected (dscf) 40.815 42356 41.278 

Oxygen Concentration (%) 11.56 11.23 11.48 

PM Found (mg) 

Filter <0.5 <0.5 <0.5 

Probe and Nozzle Rinse 1.05 0.80 0.55 

Total <1.55 <1.3 <1.05 

Stack Gas Loading 

Particulate Matter (mg/dscf) <0.038 <0.031 <0.025 

Particulate Matter (mg/dscm) <1.3 <1.1 <0.90 

Particulate Matter (mg/dscm, corrected to 7% 02 ) <2.0 <1.6 <1.3 

Particulate Matter (gr/dscf) <0.00059 <0.00047 <0.00039 

Particulate Matter (gr/dscf, corrected to 7% 02 ) 

<0.00087 <0.00068 <0.00058 

Particulate Matter (gr/dscf, corrected to 7% 02 ) 

<0.00071 

4-19 
Particulate Matter HWC MACT Sample Calculation, gr/dscf @ 7% 02 

Unit 2 - Run 2 

PM Stack Concentration (mg/dscf) = 

PM Stack Concentration (mg/dscf) = 

Total Mass Loading 

(mg) 

Sample Volume 

(dscf) 

<1.3 mg 

42.356 dscf 

<0.031 

PM Stack Concentration (gr/dscf) 

PM Stack Concentration (gr/dscf) 

Stack 

Concentration X 

(mg/dscf) 

<0.031 mg/dscf X 

0.01543 mg 

1 grain 

0.01543 mg 

1 grain 

<0.00047 

PM Stack Concentration (gr/dscf <§> 7% 02) 

PM Stack Concentration (gr/dscf @ 7% OJ 

Stack 

Concentration X 

(gr/dscf) 

0.0006 gr/dscf X 

(21% -7%) 

(21% - Meas. 02) 

(21-7) 

(21-11.23) 

0.00068 

( > 

4-20 

VES017749 
Table 4-15. Unit 3 - Results of PM in Stack Gas 

Date 

Time 

Run l 

10-15-13 

13:16-14:25 

Run 2 

10-16-13 

11:15-12:25 

Run 3 

10-1713 

09:50-10:57 

Volume Collected (dscf) 41.229 42.461 41.921 

Oxygen Concentration (%) 12.87 1338 11.74 

Particulate Matter Found (mg) 

Filter 1.05 1.3 1.15 

Probe and Nozzle Rinse 1.95 1.7 2.5 

Total 3.00 3.00 3.65 

Stack Gas Loading - Front-Half Only 

Particulate Matter (mg/dscf) 0.0728 0.0707 0.0871 

Particulate Matter (mg/dscm) 2.57 2.50 3.07 

Particulate Matter (mg/dscm, corrected to 7% 02 ) 4.45 4.61 4.67 

Particulate Matter (gr/dscf) 0.00112 0.00109 0.00134 

Particulate Matter (gr/dscf, corrected to 7% O2) 

0.00194 0.00202 0.00204 

Particulate Matter (gr/dscf, corrected to 7% O2) 

0.00200 

4-21 

VES017750 
Table 4-16. Unit 4 - Results of PM in Stack Gas 

Date 

Time 

Run l 

10-23-13 

09:30-10:42 

Run 3 

10-25-13 

09:35-10:40 

Run 4 

10-25-13 

10:50-11:55 

Volume CoUected (dscf) 38.181 39.691 36.759 

Oxygen Concentration (%) 12.22 12.48 12.11 

Particulate Matter Found (mg) 

Filter 1.95 0.5 <0.5 

Probe and Nozzle Rinse 2.2 2.35 2.4 

Front-Half Total 4.15 2.85 <2.9 

Stack Gas Loading - Front-Half Only 

Particulate Matter (mg/dscf) 0.109 0.0718 <0.079 

Particulate Matter (mg/dscm) 3.84 2.54 <2.8 

Particulate Matter (mg/dscm, corrected to 7% 02 ) 6.15 4.19 <4.4 

Particulate Matter (gr/dscf) 0.00168 0.00111 <0.0012 

Particulate Matter (gr/dscf, corrected to 7% 02 ) 

0.00269 0.00183 <0.0019 

Particulate Matter (gr/dscf, corrected to 7% 02 ) 

<0.0021 

4.2.2 HCI/CI2 in Stack Gas 

Stack gas samples for determination of HC/C12 were collected using a Modified Method 

26A. Samples were analyzed for the chloride ion using IC according to EPA Method 26A. Each 

train was recovered into multiple components for analysis as follows: 

• The first two impingers, which contained 0.1 N sulfuric acid (ACIDIMP); and 

• The fourth and fifth impingers, which contained 0.1 N sodium hydroxide (ALKIMP). 

The results for HC1/C12 are presented in Table 4-17 for Unit 2, Table 4-18 for Unit 3, and 

Table 4-19 for Unit 4. The concentration of oxygen measured using CEMS and EPA Method 3A 

during the second half of the run is shown in the tables, and the concentration of HC1/C12 

converted to chloride equivalents (Cl ) and corrected to 7% 0 2 is shown. 

The analytical results for the determination of HC1/C12 are included in Appendix G4. 

4-22 

VES017751 
Table 4-17. Unit 2 - Results of HCI/CI2

 in Stack Gas 

Date 

Time 

Runl 

10-8-13 

15:40-16:40 

Run 3 

10-10-13 

12:30-13:30 

Run 5 

10-30-13 

12:45-13:45 

Volume Collected (dscf) 37.384 37.290 36.879 

Oxygen Concentration (%) 10.08 10.38 10.50 

Hydrogen Chloride 36,600 15,500 21,600 

Chlorine <160 <180 <180 

Concentration (mg/dscf) 

Hydrogen Chloride 0.979 0.416 0.586 

Chlorine <0.0043 <0.0048 <0.0049 

Concentration (chloride equivalents, ppmvd) 

Hydrogen Chloride 22.8 9.68 13.6 

Chlorine <0.10 <0.12 <0.12 

Total <23 <9.8 <14 

Concentration (chloride equivalents, ppmvd, corrected to 7% 02 ) 

Total <29 <13 <18 

Average <20 

4-23 

VES017752 
HCI/Clz HWC MACT Sample Calculation, ppmvd @ 7% 02 

Unit 2-Run 2 

Sum of HCI Sample 

HCI Stack Concentration (mg/dscf) = Fraction Values (ng) X _ 

HCI Stack Concentration (mg/dscf) = 

Sample Volume (dscf) 

15,500 ng 

37.290 dscf 

lmg 

10'Hg 

lmg 0.416 

HCI Stack Concentration 

(chloride equivalents ppmvd) 

HCI Stack Concentration 

(chloride equivalents ppmvd) 

Cl 2 Stack Concentration (mg/dscf) = 

Cl 2 Stack Concentration (mg/dscf) 

Concentration (mg/dscf) 

28.317 L/cf 

24 L/g-mol 

Molecular Weight of HCI 

(g/g-mol) 

0.416 mg/dscf HCI 

28.317 L/cf 

24 L/g-mol 

36.5 g/g-mol 

Sum of Cl 2 Sample Fraction 

Values (ng) 

Sample Volume (dscf) 

<180 ng 

37.290 dscf 

lg 

103mg 

10s ppmvd 

lg 

ltFmg 

106 ppmvd 

lmg 

103ug 

lmg 

io3ng 

= 9.68 

= <0.0048 

CI2 Stack Concentration 

(chloride equivalents ppmvd) 

CI2 Stack Concentration 

(chloride equivalents ppmvd) 

Concentration (mg/dscf) 

28.317 L/cf 

24 L/g-mol 

[Molecular Weight of CI2 

(g/g-mol)] / 2 Chloride 

Equivalents 

<0.0048 mg/dscf CI2 

28.317 L/cf 

24 L/g-mol 

35.5 g/g-mol 

lg 

10 mg 

106 ppmvd 

lg 

103 mg 

106 ppmvd = <0.12 

Concentration (chloride equivalents 

ppmvd) 

Concentration (chloride equivalents 

ppmvd) 

HCI Stack Concentration 

(chloride equivalents 

ppmvd) 

9.68 ppmvd 

CI2 Stack 

Concentration 

(chloride 

equivalents 

ppmvd) 

<0.12 ppmvd 

<9.8 

Concentration (ppmvd @ 7% 02) = 

Concentration (ppmvd @ 7% 02] 

Concentration (chloride 

equivalents ppmvd) 

<9.80 ppmvd 

(21%-7%) 

(21% - Meas. 02) 

(21-7) = <13 

(21 -10.38) 

4-24 

VES017753 
Table 4-18. Unit 3 - Results of HC1/CI2

 in Stack Gas 

Date 

Time 

Run 2 

10-16-13 

14:00-15:00 

Run 3 

10-17-13 

12:30-13:33 

Run 4 

10-18-13 

09:35-10:35 

Volume Collected (dscf) 36.088 34.597 35.241 

Oxygen Concentration (%) 11.19 10.72 10.87 

Mass Found (ug) 

Hydrogen Chloride 4,740 4,720 1,810 

Chlorine <130 <120 <140 

Concentration (mg/dscf) 

Hydrogen Chloride 0.131 0.136 0.0514 

Chlorine <O.O036 <0.0035 <0.0040 

Concentration (chloride equivalents ppmvd) 

Hydrogen Chloride 3.06 3.18 1.20 

Chlorine <0.086 <0.083 <0.095 

Total <3.1 <3.3 <1.3 

Concentration (Chloride equivalents, ppmvd, corrected to 7% 02 ) 

Total <4.5 <4.4 <1.8 

Average <3.6 

Table 4-19. Unit 4 - Results of HCI/CI2 in Stack Gas 

Date 

Time 

Runl 

10/23/2013 

12:36-13:36 

Run 3 

10/24/2013 

12:35-13:35 

Run 4 

10/25/2013 

13:35-14:35 

Volume Collected (dscf) 39.935 39.264 37.034 

Oxygen Concentration (%) 12.27 12.37 12.00 

Mass Found (ug) 

Hydrogen Chloride 11,100 8,150 23,600 

Chlorine <130 <120 <140 

Concentration (mg/dscf) 

Hydrogen Chloride 0.278 0.208 0.637 

Chlorine <0.0033 <0.0031 <0.0038 

Concentration (chloride equivalents ppmvd) 

Hydrogen Chloride 6.47 4.84 14.8 

Chlorine <0.078 <0.073 <0.091 

Total <6.6 <4.9 <15 

Concentration (Chloride equivalents, ppmvd, corrected to 7% 02 ) 

Total <11 <8.0 <23 

Average <14 

4-25 

VES017754 
4.2.3 Metals in Stack Gas 

Metals were sampled in the stack gas using EPA Method 29. The samples were analyzed 

for the six (6) metals regulated by the HWC MACT. Five metals, arsenic, beryllium, cadmium, 

chromium, and lead) were analyzed using ICPES according to Method 601 OB of SW-846. 

Mercury analysis was performed by cold vapor atomic absorption spectroscopy according to 

Method 7470A of SW-846. 

The Method 29 sampling trains were recovered to provide the following fractions: 

• Probe and nozzle rinse with 0.1 N nitric acid (PNR); 

• Filter (FILT); 

• Content and rinse of the acidified peroxide impingers with 0.1 N nitric acid (NPI); 

• Contents and rinse of the empty impinger with 0.1 N nitric acid (EIR); 

• Contents and rinse of the acidified permanganate impingers with deionized water, 

0.1 N nitric acid, and permanganate solution (Perm); and; 

• Rinse of the permanganate impingers with hydrochloric acid (HClRns). 

The analytical results for metals in the individual sample fractions are presented in Table 

4-20 for Unit 2, Table 4-22 for Unit 3, and Table 4-24 for Unit 4. The concentrations of the 

metals in the stack gas are presented in Table 4-21 for Unit 2, Table 4-23 for Unit 3, and Table 

4-25 for Unit 4. The concentration of oxygen measured using CEMS and EPA Method 3A 

during the second half of the test are shown in Tables 4-21,4-23, and 4-25, and the concentration 

of metals in the stack gas corrected to 7% O2 is shown. The concentrations of cadmium and lead 

are shown summed as SVM, and the concentrations of arsenic, beryllium, and chromium are 

shown summed as LVM. 

The analytical results for the determination of metals in the stack gas are included in 

Appendix G3. 

4-26 

VES017755 
Table 4-20. Unit 2 - Analytical Results of Metals in Stack Gas 

Run Analyte 

Nitric 

Acid PNR 

& Filter 

Nitric Acid & 

Hydrogen 

Peroxide 

Impingers 

Empty 

Impinger 

Rinse 

Potassium 

Permanganate 

Impinger 

HCI 

Rinse 

Total 

1 

Arsenic <0.37 <0.25 <0.25 <0.87 

1 

Beryllium <0.015 <0.015 <0.015 <0.045 

1 

Cadmium <0.021 <0.021 <0.021 <0.O63 

1 

Chromium 3.3 0.78 0.33 - 4.41 

1 

Lead 1.3 0.35 <0.27 <1.9 

1 

Mercury <0.08 84.2 51.6 <31.136 1.1 <170 

3 

Arsenic <0.74 <0.25 <0.99 

3 

Beryllium <0.015 <0.015 <0.03 

3 

Cadmium <0.021 <0.021 <0.042 

3 

Chromium 2.5 0.55 3.05 

3 

Lead <1 0.27 <1.3 

3 

Mercury <0.08 182 0.57 0.5 17.2 <200 

5 

Arsenic 0.77 <0.25 <1 

5 

Beryllium 0.016 <0.015 <0.031 

5 

Cadmium <0.021 <0.021 <0.042 

5 Chromium 2.3 0.81 3.11 5 

Lead <1 0.66 <1.7 

5 

Mercury <0.08 142 <0.15 3.4 14.3 <160 

1

 The empty impinger was analyzed for As, Be, Cd, Cr, and Pb due to carry-over from the second nitric acid and 

hydrogen peroxide impinger. 

4-27 

VES017756 
Table 4-21. Unit 2 - Results of Metals in Stack Gas 

Runl Run 3 Run 5 

Date 10-8-13 10-10-13 10-30-13 

Time 15:40-18:43 12:30-15:10 12:45-15:32 Average 

Volume CoUected (dscf) 84.952 78.951 79.607 

Average 

Oxygen Concentration (%) 10.08 10.38 10.50 

Average 

Mass Found (ng) 

Arsenic <0.87 <0.99 <1.0 

Beryllium <0.045 <0.030 <0.031 

Cadmium <0.063 <0.042 <0.042 

Chromium 4.41 3.05 3.11 

Lead <1.9 <1.3 <1.7 

Mercury <170 <200 <160 

Stack Gas Concentration (ug/dscf) 

Arsenic <0.010 <0.013 <0.013 <0.012 

Beryllium <0.00053 <0.00038 <0.00039 <0.00043 

Cadmium <0.00074 <0.00053 <0.00053 <0.00060 

Chromium 0.0519 0.0386 0.0391 0.0432 

Lead <0.023 <0.016 <0.021 <0.020 

Mercury <2.0 <2.5 <2.0 <2.2 

Stack Gas Concentration (ng/dscm) 

Arsenic <0.36 <0.44 <0.45 <0.42 

Beryllium <0.019 <0.013 <0.014 <0.015 

Cadmium <0.026 <0.019 <0.019 <0.021 

Chromium 1.83 1.36 1.38 1.53 

Lead <0.80 <0.57 <0.74 <0.70 

Mercury <70 <90 <71 <77 

Stack Gas Concentration (ug/dscm, 7% 02 ) 

Arsenic <0.46 <0.59 <0.60 <0.55 

Beryllium <0.024 <0.018 <0.018 <0.020 

Cadmium <0.034 <0.025 <0.025 <0.028 

Chromium 2.35 1.80 1.84 2.00 

Lead <1.0 <0.75 <0.98 <0.92 

Mercury <90 <120 <95 <100 

SVM (Cd, Pb) <1.1 <0.78 <1.0 <0.95 

L V M (As, Be, Cr) <2.8 <2.4 <2.5 <2.6 

Mercury <90 <120 <95 <100 

4-28 

VES017757 
Table 4-22. Unit 3 - Analytical Results of Metals in Stack Gas 

Run Analyte 

Nitric 

Acid PNR 

& Filter 

Nitric Acid 

& Hydrogen 

Peroxide 

Impingers 

Empty 

Impinger 

Rinse 

Potassium 

Permanganate 

Impinger 

HCI 

Rinse 

Total 

2 

Arsenic <0.74 <0.25 <0.99 

2 

Beryllium <0.015 <0.015 <0.O3 

2 

Cadmium <0.021 <0.021 <0.042 

2 

Chromium 10.6 0.56 11.2 

2 

Lead 28.6 <0.27 <29 

2 

Mercury <0.08 81 0.29 0.21 2.5 <84 

3 

Arsenic <0.74 <0.25 <0.99 

3 

Beryllium <0.015 <0.015 <0.O3 

3 

Cadmium <0.021 <0.021 <0.O42 

3 

Chromium 11 0.79 11.8 

3 

Lead 19.4 <0.27 <20 

3 

Mercury <0.08 52.2 0.25 <0.048 2.6 <55 

4 

Arsenic <0.37 0.83 <1.2 

4 

Beryllium <0.015 <0.015 <0.03 

4 

Cadmium 0.91 <0.021 <0.93 

4 

Chromium 13.7 0.72 14.4 

4 

Lead 15.7 0.3 16 

4 

Mercury <0.08 54 0.18 0.16 12.8 <67 

4-29 

VES017758 
Table 4-23. Unit 3 - Results of Metals in Stack Gas 

Run 2 Run 3 Run 4 

Date 10-16-13 10-17-13 10-18-13 

Time 14:00-16:50 12:30-15:25 09:35-12:20 Average 

Volume Collected (dscf) 71.708 69.016 71.540 

Average 

Oxygen Concentration (%) 11.19 10.72 10.87 

Average 

Mass Found (ug) 

Arsenic <0.99 <0.99 <1.2 

Beryllium <0.030 <0.030 <0.030 

Cadmium <0.042 <0.042 <0.93 

Chromium 11.2 11.8 14.4 

Lead <29 <20 16.0 

Mercury <84 <55 <67 

Stack Gas Concentration (ug/dscf) 

Arsenic <0.014 <0.014 <0.017 <0.015 

Beryllium <0.00042 <0.00043 <0.00042 <0.00042 

Cadmium <0.00059 <0.00061 <0.013 <0.0047 

Chromium 0.156 0.171 0.202 0.176 

Lead <0.40 <0.29 0.224 <0.30 

Mercury <1.2 <0.80 <0.94 <0.97 

Stack Gas Concentration (ug/dscm) 

Arsenic <0.49 <0.51 <0.59 <0.53 

Beryllium <0.015 <0.015 <0.015 <0.015 

Cadmium <0.021 <0.021 <0.46 <0.17 

Chromium 5.50 6.03 7.12 6.22 

Lead <14 <10 7.90 <11 

Mercury <41 <28 <33 <34 

Stack Gas Concentration (ug/dscm, 7% 02 ) 

Arsenic <0.70 <0.69 <0.82 <0.74 

Beryllium <0.021 <0.021 <0.021 <0.021 

Cadmium <0.030 <0.029 <0.64 <0.23 

Chromium 7.87 8.23 9.87 8.66 

Lead <20 <14 10.9 <15 

Mercury <59 <39 <46 <48 

SVM (Cd, Pb) <20 <14 <12 <15 

L V M (As, Be, Cr) <8.6 <8.9 <11 <9.4 

Mercury <59 <39 <46 <48 

4-30 

VES017759 
Metals HWC MACT Sample Calculation, ug/dscm @ 7% 02 

Total Mass (pg) = Sum of Masses in Individual Sample Fractions 

(See Table 4-20) 

Unit 2 - Run 1, Arsenic 

Arsenic Mass (u.g) 

Metals Stack Concentration (ug/dscf) = 

Metals Stack Concentration (ug/dscf) = 

Sample Volume (dscf) 

<0.87 ug 

<0.01 0 

84.952 dscf 

Metals Stack Concentration (ug/dscm) 

Arsenic Stack 

Concentration (ug/dscf) 

Metals Stack Concentration (ug/dscm) = <0.010 ug/dscf 

35.315 dscf 

1 dscm 

35.315 dscf 

ldscm 

= <0.36 

Metals Stack Concentration (ug/dscm _ Arsenic Stack (21% - 7%) 

@ 7% 02) Concentration (ug/dscm) (21%. Meas. 02) 

Metals Stack Concentration (ug/dscm _ <Q3 g x Qkzll _ <Q 4 g 

@7%02) ~ * (21-10.08) 

4-31 

VES017760 
Table 4-24. Unit 4 - Analytical Results of Metals in Stack Gas 

Run Analyte 

Nitric 

Acid PNR 

& Filter 

Nitric Acid 

& Hydrogen 

Peroxide 

Impingers 

Empty 

Impinger 

Rinse 

Potassium 

Permanganate 

Impinger 

HCI 

Rinse 

Total 

1 

Arsenic 9.1 <0.25 <9.4 

1 

Beryllium <0.015 <0.015 <0.03 

1 

Cadmium 0.33 <0.021 <0.35 

1 

Chromium 5.5 0.82 6.32 

1 

Lead 10.4 0.71 11.1 

1 

Mercury <0.08 9 <0.12 <0.048 0.22 <9.5 

2 

Arsenic 7.9 <0.25 <8.2 

2 

Beryllium <0.015 <0.015 <0.03 

2 

Cadmium 0.15 <0.021 <0.17 

2 

Chromium 4.2 0.66 4.86 

2 

Lead 5.4 0.42 5.82 

2 

Mercury <0.08 10.4 <0.12 <0.047 <0.082 <11 

3 

Arsenic 2.7 <0.25 <3 

3 

Beryllium <0.015 <0.015 <0.O3 

3 

Cadmium 0.069 <0.021 <0.09 

3 Chromium 6.9 0.62 7.52 3 

Lead 14 0.44 14.4 

3 

Mercury <0.08 19.5 <0.12 <0.047 0.75 <20 

4-32 

VES017761 
Table 4-25. Unit 4 - Results of Metals in Stack Gas 

Runl Run 2 Run 3 

Date 10-23-13 10-24-13 10-25-13 

Time 12:36-15:20 12:35-15:15 13:35-16:11 Average 

Volume Collected (dscf) 76.068 76.498 76.846 

Average 

Oxygen Concentration (%) 12.27 12.37 12.00 

Average 

Mass Found (ug) 

Arsenic <9.4 <8.2 <3.0 

Beryllium <0.030 <0.030 <0.030 

Cadmium <0.35 <0.17 <0.090 

Chromium 6.32 4.86 7.52 

Lead 11.1 5.82 14.4 

Mercury <9.5 <11 <20 

Stack Gas Concentration (ug/dscf) 

Arsenic <0.12 <0.11 <0.038 <0.089 

Beryllium <0.00039 <0.00039 <0.00039 <0.00039 

Cadmium <0.0046 <0.0022 <0.0012 <0.0027 

Chromium 0.0831 0.0635 0.0979 0.0815 

Lead 0.146 0.0761 0.188 0.137 

Mercury <0.12 <0.14 <0.27 <0.18 

Stack Gas Concentration (ng/dscm) 

Arsenic <4.3 <3.8 <1.4 <3.2 

Beryllium <0.014 <0.014 <0.014 <0.014 

Cadmium <0.16 <0.079 <0.041 <0.094 

Chromium 2.93 2.24 3.46 2.88 

Lead 5.16 2.69 6.64 4.83 

Mercury <4.4 <5.0 <9.4 <6.3 

Stack Gas Concentration (ug/dscm, 7% 02) 

Arsenic <7.0 <6.1 <2.1 <5.1 

Beryllium <0.022 <0.023 <0.022 <0.022 

Cadmium <0.26 <0.13 <0.065 <0.15 

Chromium 4.73 3.66 5.40 4.59 

Lead 8.31 4.38 10.4 7.68 

Mercury <7.1 <8.1 <15 <10.0 

SVM (Cd, Pb) <8.6 <4.5 <10 <7.8 

L V M (As, Be, Cr) <12 <9.8 <7.5 <9.7 

Mercury <7.1 <8.1 <15 <10.0 

4-33 

VES017762 
4.2.4 Dioxins/Furans in Stack Gas 

Stack gas samples for deterrnination of dioxins/furans were collected using SW-846 

Method 0023A and were analyzed using SW-846 Method 8290, a high resolution gas 

chromatography (HRGC) with high resolution mass spectroscopy (HRMS) analytical technique. 

The sampling train was recovered to provide the following fractions: 

• Combined probe and nozzle rinse with acetone, methylene chloride and toluene 

(PNR); 

• Filter (FILT); 

• Condenser rinse with acetone, methylene chloride, and toluene (CR); and 

• XAD sorbent (XAD). 

Components recovered from the train were combined as follows: 

• Combination of the filter and all the rinses between the nozzle and filter; and 

• Combination of the sorbent and all the rinses between the filter and sorbent. 

After sample cleanup and concentration procedures at the analytical laboratory, an aliquot 

ofthe front-half extracts (i.e., PNR and filter) is combined and analyzed using SW-846 Method 

8290 for dioxins/furans separate from the back-half components (i.e., condenser rinses, XAD 

sorbent). Dioxins/furans results are presented in Table 4-26 for Unit 2, Table 4-27 for Unit 3, and 

Table 4-28 for Unit 4. The concentration of oxygen measured using CEMS and EPA Method 3A 

during the second half of the run are shown in the tables, and the concentration of dioxins/furans 

corrected to 7% 0 2 is shown. 

The analytical results for the dioxins/furans analyses are included in Appendix G2. 

Results for dioxins/furans are converted to 2,3,7,8-tetrachlorodibenzo-dioxin toxicity equivalents 

(TEQ). Note that Section §1208(b)(l)(iii) of the HWC MACT states that non-detects (all results 

preceded by a "<") of dioxins/furans can be assumed to be at zero concentrations. Additionally, 

results followed by an "*" are denoted as Estimated Possible Maximum Concentrations, and are 

likewise not included in the calculation of total mass. 

4-34 

VES017763 
Table 4-26. Unit 2 - Results of Dioxins/Furans in Stack Gas 

Date 

Time 

Runl 

10-8-13 

15:40-18:55 

Run 3 

10-10-13 

12:30-15:40 

Run 5 

10-30-13 

12:45-16:02 

Volume Collected (dscf) 121.164 119.568 124.921 

Oxygen Concentration (%) 10.08 10.38 10.50 

Analyte Toxicity Equivalent Factor1 Mass Found (pg)2 Analyte Toxicity Equivalent Factor1 

PNR/Filter XAD/Cond Sum __, PNR/Filter XAD/Cond Sum PNR/Filter XAD/Cond Sum 

2,3,7,8-TCDD 1 <2.9J <3.6 <6.5 <2.8 <3 <5.8 <4.6 <4.7 <9.3 

1,2,3,7,8-PeCDD 0.5 <1.4 7.2* <8.6 <1.6 6.9* <8.5 <2.1 2 3 * <25.1 

1,2,3,4,7,8-HxCDD 0.1 <1.2 7.3 <8.5 <1.2 5 <6.2 <1.7 20 <21.7 

1,2,3,6,7,8-HxCDD 0.1 <1.2 14 <15.2 <1.2 15 <16.2 <1.6 39 <40.6 

1,2,3,7,8,9-HxCDD 0.1 <1.2 12 <13.2 <1.2 17 <18.2 <1.7 48 <49.7 

1,2,3,4,6,7,8-HpCDD 0.01 3.3 *" 82 85.3* 2.9 94 96.9 <2 250 <252 

OCD D 0.001 9.1 110 119.1 8.1 * 120 128.1 * 7.7 350 357.7 

2,3,7,8-TCDF 0.1 <1,7 9.5 <11.2 <2 9.3 <U.3 <3 49 <52 

1,2,3,7,8-PeCDF 0.05 <1.1 11 * <12.1 <1.1 12* <13.1 <2.1 7 2 * <74.1 

2,3,4,7,8-PeCDF 0.5 <1.2 16 <17.2 <1.1 18 <19.1 <2.1 110* <U2.1 

1,2,3,4,7,8-HxCDF 0.1 <0.69 41 * <41.69 <0.82 4 6 * <46.82 <1.1 190* <191.1 

1,2,3,6,7,8-HxCDF 0.1 <0.61 17* <17.61 <0.73 17* <17.73 <1 130* <131 

1,2,3,7,8,9-HxCDF 0.1 <0.75 2.9 <3.65 <0.89 2.1 <2.99 <1.2 12 <13.2 

2,3,4,6,7,8-HxCDF 0.1 <0.65 13 * <13.65 <0.77 16* < 16.77 <1.1 130 <131.1 

1,2,3,4,6,7,8-HpCDF 0.01 5 * 79 84* 4 89 93 2.4* 780 782.4 * 

1,2,3,4,7,8,9-HpCDF 0.01 <1.7 10 <11.7 <1.8 12 <13.8 <1.7 110 <111.7 

OCD F 0.001 11 * 110 121 * 11 9 8 * 109* 9.7 630* 639.7 * 

Total Toxicity Equivalents 0.00910 14.5 14.5 0.0800 15.9 16.0 0.0174 41.6 41.6 

Concentration (ng TEQ/dscf) 0.000120 0.000134 0.000333 

Concentration (ng TEQ/dscm) 0.00423 0.00472 0.0118 

Concentration (ng TEQ/dscm @ 7% 02) 0.00543 0.00624 0.0157 

Average Concentration (ng TEQ/dscm @ 7% Oi) 0.00912 

1

 Toxic Equivalency Factor (TEF) as developed in: "Interim Procedure for Estimating Risks Associated With Exposures to Mixtures of Chlorinated Dibenzo-p-Dioxin and -Dibenzofurans (CDDs and 

CDFs) and 1989 Update", March 1989; Van den Berg, M„ et a]. "Toxic Equivalency Factors (TEFs) for PCBs, PCDDs, PCDFs for Humans and Wildlife" Environmental Health Perspectives, 

Volume 106, Number 12. December 1998., as directed by the Preamble to the HWC MACT. 

2

 Results followed by an "*" are Estimated Maximum Possible Concentrations (EMPCs). 

3

 In accordance with Section §1208(b)(l)(iii) of the HWC MACT, non-detects of dioxins/furans are assumed to be at zero concentrations. 

In accordance with the USEPA Analytical Services Branch document National Functional Guidelines/or Chlorinated Dibenzo-p-Dioxins and Chlorinated Dibenzofurans Data Review, EMPCs are 

not included in the calculation of TEFs. 

4-35 

VES017764 
Dioxins/Furans HWC MACT Sample Calculation 

ng TEQ/dscm @ 7% O2 (continued) 

Unit 2 - Run 1 

Stack Concentration (ng TEQ/dscf) 

Stack Concentration (ng TEQ/dscf) 

Sum of all TEQ 

Values (pg) 

Sample Volume 

(dscf) 

14.5 pg TEQ 

121.164 dscf 

1 ng 

10 3pg 

1 ng 

103pg 

= 0.0O0120 

Stack Concentration (ng TEQ/dscm) = 

Stack Concentration (ng TEQ/dscm) 

Concentration 

(ng TEQ/dscf) 

0.000120 

35.315 dscf 

1 dscm 

35.315 dscf 

1 dscm 

0.00423 

Stack Concentration (ng TEQ/dscm @ 7% 02) 

Stack Concentration (ng TEQ/dscm @ 7% 02) 

Concentration 

(ng TEQ/dscm) 

0.00423 

(21% -7%) 

(21%-Meas.Oz) 

(21 - 7) = 0.00543 

(21-10.08) 

4-36 

VES017765 
Table 4-27. Unit 3 - Results of Dioxins/Furans in Stack Gas 

Date 

Time 

Run 2 

10-16-13 

14:00-17:20 

Run 3 

10-17-13 

12:30-15:55 

Run 4 

10-18-13 

09:35-12:50 

Volume Collected (dscf) 106.303 102.724 102.624 

Oxygen Concentration (%) 11.19 10.72 10.87 

Analyte Toxicity Equivalent Factor1 Mass Found (pg)2 Analyte Toxicity Equivalent Factor1 

PNR/Filter XAD/Cond Sum PNR/Filter XAD/Cond Sum PNR/Filter XAD/Cond Sum 

2,3,7,8-TCDD 1 <0.14J 1.1 * <1.24 <0.7 3.8* <4.5 <0.29 1.9* <2.19 

1,2,3,7,8-PeCDD 0.5 0.23 4.8* 5.03 * 1.4* 12* 13.4* <0.15 5 * <5.15 

1,2,3,4,7,8-HxCDD 0.1 <0.15 2.6 <2.75 <0.7 4.1 * <4.8 <0.42 3 <3.42 

1,2,3,6,7,8-HxCDD 0.1 0.22 ^ 5.3 5.52* <0.67 11 * <11.67 <0.4 5.1 * <5.5 

1,2,3,7,8,9-HxCDD 0.1 0.41 * 5.6 6.01 * 1.5* 12* 13.5* 1.4* 8.1 9.5 * 

1,2,3,4,6,7,8-HpCDD 0.01 1.5* 29 30.5 * 1.6* 57 58.6* 1.9 29 30.9 

OCD D 0.001 7.7* 37 44.7* 12 40 52 5.6* 28 33.6 * 

2,3,7,8-TCDF 0.1 0.29 6.8* 7.09* <0.47 14 <14.47 <0.29 11 <11.29 

1,2,3,7,8-PeCDF 0.05 <0.11 9.1 * <9.21^ <0.78 2 0 * <20.78 <0.31 12* <12.31 

2,3,4,7,8-PeCDF 0.5 <0.11 19* <19.11 <0.78 36* <36.78 <0.31 27 * <27.31 

1,2,3,4,7,8-HxCDF 0.1 0.48* 2 5 * 25.48 * 2.5* 61 * 63.5* 0.62* 2 6 * 26.62 * 

1,2,3,6,7,8-HxCDF 0.1 0.22 * 11 * 11.22* <0.57 2 3 * <23.57 0.29* 12* 12.29 * 

1,2,3,7,8,9-HxCDF 0.1 0.7 0.9 * 1.6* 1.4* 2.4* 3.8* 0.56* 1.2* 1.76 * 

2,3,4,6,7,8-HxCDF 0.1 0.42* 11 * 11.42* 1.3* 21 * 22.3 * 0.55* 12* 12.55 * 

1,2,3,4,6,7,8-HpCDF 0.01 1.1 * 28 29.1 * <0.63 43 <43.63 0.78* 22 22.78 * 

1,2,3,4,7,8,9-HpCDF 0.01 0.48 * 3.8* 4.28* 1.9* 5 * 6.9* 0.66* 4.4 5.06 * 

OCDF 0.001 3.8 8.5* 12.3* 5.8 9.7 * 15.5* 4.7 5.7* 10.4 * 

Total Toxicity Equivalents 0.218 1.96 2.17 0.0178 2.44 2.46 0.0237 2.79 2.82 

Concentration (ng TEQ/dscf) 0.0000205 0.0000239 0.0000274 

Concentration (ng TEQ/dscm) 0.000722 0.000845 0.000969 

Concentration (ng TEQ/dscm @ 7% O2) 0.00103 0.00115 0.00134 

Average Concentration (ng TEQ/dscm @ 7% O2) 0.00118 

1

 Toxic Equivalency Factor (TEF) as developed in: "Interim Procedure for Estimating Risks Associated With Exposures to Mixtures of Chlorinated Dibenzo-p-Dioxin and -Dibenzofurans (CDDs and 

CDFs) and 1989 Update", March 1989; Van den Berg, M„ et al. "Toxic Equivalency Factors (TEFs) for PCBs, PCDDs, PCDFs for Humans and Wildlife" Environmental Health Perspectives, 

Volume 106, Number 12, December 1998., as directed by the Preamble to the HWC MACT. 

2

 Results followed by an "*" are Estimated Maximum Possible Concentrations (EMPCs). 

3

 In accordance with Section § 1208(b)( 1 )(iii) of the HWC MACT, non-detects of dioxins/furans are assumed to be at zero concentrations. 

4

 In accordance with the USEPA Analytical Services Branch document National Functional Guidelines for Chlorinated Dibenzo-p-Dioxins and Chlorinated Dibenzofurans Data Review, EMPCs are 

not included in the calculation of TEFs. 

4-37 

VES017766 
Table 4-28. Unit 4 - Results of Dioxins/Furans in Stack Gas 

Date 

Time 

Runl 

10-23-13 

12:36-15:50 

Run 2 

10-24-13 

12:35-15:45 

Run 3 

10-25-13 

13:35-16:41 

Volume Collected (dscf) 110.791 112.803 115.284 

Oxygen Concentration (%) 12.27 12.37 12.00 

Analyte Toxicity Equivalent Factor1 Mass Found (pg), Analyte Toxicity Equivalent Factor1 

PNR/Filter XAD/Cond Sum PNR/Filter XAD/Cond Sum PNR/Filter XAD/Cond Sum 

2,3,7,8-TCDD 1 <4.93 7 * <11.9 <4.3 9.5 * <13.8 <2.5 8.2* <10.7 

1,2,3,7,8-PeCDD 0.5 <1.9 120* <121.9 <2.2 120* <122.2 2 120* 122 * 

1,2,3,4,7,8-HxCDD 0.1 <2 230 <232 4.3 230 234.3 3.9* 230 233.9 * 

1,2,3,6,7,8-HxCDD 0.1 13 ** 990 1003* 9.4* 930 939.4 * 16 940 956 

1,2,3,7,8,9-HxCDD 0.1 10 * 640 650* 12* 650 662* 12 630 642 

1,2,3,4,6,7,8-HpCDD 0.01 160 6100 6260 130 5500 5630 160 5900 6060 

OCD D 0.001 170 3600 3770 150 3500 3650 190 4100 4290 

2,3,7,8-TCDF 0.1 3.8* 78 81.8* <2.9 70 <72.9 3.6* 70 73.6 * 

1,2,3,7,8-PeCDF 0.05 <2 130* <132 <2.1 120* <122.1 <1.2 110* <111.2 

2,3,4,7,8-PeCDF 0.5 4.5* 550* 554.5 * <2.2 510* <512.2 4.7* 430* 434.7 * 

1,2,3,4,7,8-HxCDF 0.1 4.7 * 570* 574.7 * 5 510* 515* 3.6* 260 263.6 * 

1,2,3,6,7,8-HxCDF 0.1 2.3 * 310* 312.3 * 2.7* 290* 292.7 * 2.6* 300* J 302.6 * 

1,2,3,7,8,9-HxCDF 0.1 <1.3 3 9 * <40.3 <1.4 38 * <39.4 <0.82 43 * <43.82 

2,3,4,6,7,8-HxCDF 0.1 7.9* 600* 607.9 * 6.9 510* 516.9* 8.4* 560* 568.4 * 

1,2,3,4,6,7,8-HpCDF 0.01 15 760 775 10* 710 720* 17 720 737 

1,2,3,4,7,8,9-HpCDF 0.01 4.1 * 180 184.1 * 3.5* 160 163.5 * 5.9* 200 205.9 * 

OCD F 0.001 12 * 140* 152* 10* 140 150* J 11 * 160* 171 * 

Total Toxicity Equivalents 1.92 268 270 3.07 255 258 5.76 285 291 

Concentration (ng TEQ/dscf) 0.00243 0.00229 0.00252 

Concentration (ng TEQ/dscm) 0.0860 0.0809 0.0892 

Concentration (ng TEQ/dscm @ 7% 0>2) 0.138 0.132 0.139 

Average Concentration (ng TEQ/dscm @ 7% O2) 0.137 

Toxic Equivalency Factor (TEF) as developed in: "Interim Procedure for Estimating Risks Associated With Exposures to Mixtures of Chlorinated Dibenzo-p-Dioxin and -Dibenzofurans (CDDs and 

CDFs) and 1989 Update", March 1989; Van den Berg, M., et al. "Toxic Equivalency Factors (TEFs) for PCBs, PCDDs, PCDFs for Humans and Wildlife" Environmental Health Perspectives, 

Volume 106, Number 12. December 1998., as directed by the Preamble to the HWC MACT. 

2

 Results followed by an "*" are Estimated Maximum Possible Concentiations (EMPCs). 

3

 In accordance with Section §1208(b)(l)(iii) of the HWC MACT, non-detects of dioxins/furans are assumed to be at zero concentrations. 

4

 In accordance with the USEPA Analytical Services Branch document National Functional Guidelines for Chlorinated Dibenzo-p-Dioxins and Chlorinated Dibenzofurans Data Review, EMPCs are 

not included in the calculation of TEFs. 

4-38 

VES017767 
4.2.5 THC in Stack Gas 

Total hydrocarbons (THC) were monitored in the stack gas using EPA Method 25A. 

THC was monitored throughout the second half of each run. Stack gas concentrations of THC 

are presented in Table 4-29 for Unit 2, Table 4-30 for Unit 3, and Table 4-31 for Unit 4. The 

concentration of oxygen measured using CEMS and EPA Method 3A during the second half of 

the run are shown in the tables, and the concentration of THC corrected to 1% O2 is shown. 

Table 4-29. Unit 2 - Results for THC in Stack Gas 

Date 

Time 

Run l 

10-8-13 

15:40 -18:55 

Run 3 

10-10-13 

12:30 -15:40 

Run 5 

10-30-13 

12:45 -16:02 

T HC (ppmv, wet, as propane) 0.68 0.07 0.21 

Moisture (%) 44.7 45.3 42.9 

THC (ppmv, dry, as propane) 1.2 0.13 0.37 

Oxygen Concentration (%) 10.08 10.38 10.50 

T HC (ppmv, dry, as propane, corrected to 7% 02 ) 1.6 0.18 0.49 

Average THC (ppmv, dry, as propane, corrected to 7% 02 ) 0.75 

THC HWC MACT Sample Calculation 

ppmvd @ 7% 02 (continued) 

Unit 2 - Run 5 

THC Concentration

 1 

THC Concentration (ppmvd) = X 

(PP m v ) (l-(% Moisture/100%)) 

THC Concentration (ppmvd) = 0.21 ppmv 

(1-(42.9%/100%)) 

= 0.37 

THC Concentration (21%-7%) 

THC Concentration (ppmvd) = X 

(Ppmvd) (21% - Meas. 02) 

THC Concentration (ppmvd) = 0.37 

(21-7) 

(21-10.50) 

0.49 

4-39 

VES017768 
Table 4-30. Unit 3 - Results for THC in Stack Gas 

Run 2 Run 3 Run 4 

Date 10-16-13 10-17-13 10-18-13 

Time 14:00 -17:20 12:30 -15:55 09:35 -12:50 

T HC (ppmv, wet, as propane) 0.18 0.11 0.23 

Moisture (%) 42.9 44.4 43.7 

T HC (ppmv, dry, as propane) 0.31 0.19 0.41 

Oxygen Concentration (%) 11.19 10.72 10.87 

THC (ppmv, dry, as propane, corrected to 7% 02 ) 0.44 0.26 0.57 

Average THC (ppmv, dry, as propane, corrected to 7% 02 ) 0.43 

Table 4-31. Unit 4 - Results for THC in Stack Gas 

Runl Run 2 Run 3 

Date 10-23-13 10-24-13 10-25-13 

Time 12:36-15:50 12:35 -15:45 13:35 -16:41 

T HC (ppmv, wet, as propane) 0.19 0.23 0.33 

Moisture (%) 39.2 38.3 39.3 

T HC (ppmv, dry, as propane) 0.32 0.37 0.54 

Oxygen Concentration (%) 12.27 12.37 12.00 

T HC (ppmv, dry, as propane, corrected to 7% 02 ) 0.51 0.60 0.85 

Average THC (ppmv, dry, as propane, corrected to 7% 02 ) 0.65 

4-40 

VES017769 
4.3 Chlorine, Ash, and Metals Feedrates 

This section presents calculated values using the analytical results presented previously, 

waste feedrates, and spiking feedrates. Feedrates are calculated for: 

• Total Chlorine/Chloride; 

• Ash; and 

• Metals. 

In those circumstances where a constituent is not detected in a waste feed (i.e., is not 

analyzed above the detection limit), the concentration of that parameter is treated as zero "0" in 

the calculation of the feedrate of that constituent that becomes an OPL for that parameter. 

4.3.1 Chlorine Feedrate 

Feedrate of total chlorine and chloride (i.e., chlorine) is an OPL for the emission 

standards for hydrogen chloride and chlorine gas (HC1/C12) and for SVM and LVM. The feedrate 

of chlorine has been determined during both the HCI/CI2 and metals (i.e., SVM and LVM) stack 

sampling in the second part of each run. Table 4-32 presents the chlorine feedrates calculated 

during both the HCI/CI2 and metals stack sampling for Unit 2. Chlorine feedrates for Unit 3 are 

presented in Table 4-33, and chlorine feedrates for Unit 4 are presented in Table 4-34. 

For the calculation of the chlorine feedrate, the weight of the Containerized Solid Waste 

used to calculate the feedrates of chlorine was reduced by the weight of the box, and the spiking 

materials lead nitrate, hexachloroethane, and the solution of mercuric nitrate to determine the 

feedrate of Containerized Solid Waste that was analyzed for chlorine. 

4.3.2 Ash Feedrate 

Feedrate of ash is an OPL for the emission standard for particulate matter. The feedrate of 

ash has been determined during the particulate matter stack sampling in the first part of each run. 

Table 4-35 presents the ash feedrate calculated during stack sampling for particulate matter for 

Unit 2. Ash feedrates for Unit 3 are presented in Table 4-36, and ash feedrates for Unit 4 are 

presented in Table 4-37. 

4-41 

VES017770 
Table 4-32. Unit 2 - Chlorine Feedrate 

HCl/Cb Stack Sampling Metals Stack Sampling 

Runl Run 3 Run 5 Runl Run 3 Run 5 

10-8-13 10-10-13 10-30-13 10-8-13 10-10-13 10-30-13 

15:40 -16:40 12:30 -13:30 12:45 -13:45 15:40 -18:43 12:30 -15:10 12:45 -15:32 

Feedrate (lbs/hr) 1,422.1 1,500.9 1,451.9 1,474.6 1,513.3 1,396.5 

Low-Btu Liquid Waste Chlorine Concentration (mg/kg) 340 404 340 347 364 357 

Chlorine Feedrate (lb/hr) 0.48 0.61 0.49 0.51 0.55 0.50 

Feedrate (lbs/hr) 1,370.8 1,098.7 1,200.0 1,289.1 1,098.9 1,164.6 

High-Btu Liquid Waste Chlorine Concentration (mg/kg) 6.960 3,260 3,500 7,140 3,210 3,580 

Chlorine Feedrate (lb/hr) 9.54 3.58 4.20 9.20 3.53 4.17 

Feedrate (lbs/hr) 485.9 398.2 440.8 432.6 425.4 445.3 

Specialty Liquid Waste Chlorine Concentration (mg/kg) 105 130 106 \ 159 124 92.4 

Chlorine Feedrate (lb/hr) 0.05 0.05 0.05 0.07 0.05 0.04 

Feedrate (lbs/hr) 540.0 534.3 535.7 j 547.0 536.1 542.4 

Containerized Solid Waste1 Chlorine Concentration (mg/kg) 184 345 346 167 499 396 

Chlorine Feedrate (lb/hr) 0.10 0.18 0.19 0.09 0.27 0.21 

Chlorine Spiking Chlorine Feedrate (lb/hr) 197.9 203.1 197.9 | 199.7 j 199.2 200.2 

Total Chlorine Feedrate (lb/hr) 208.0 207.5 202.8 | 209.6 203.6 205.1 

Average Chlorine Feedrate (lb/hr) 206.1 | 206.1 

1

 The weight of the Containerized Solid Waste used to calculate the feedrates of chlorine and metals has been reduced by the weight of the box, and the spiking materials lead nitrate, 

hexachloroethane, and the solution of mercuric nitrate. 

4-42 

VES017771 
Table 4-33. Unit 3 - Chlorine Feedrate 

HCI/CI2 Stack Sampling Metals Stack Sampling 

Run 2 Run 3 Run 4 Run 2 Run 3 Run 4 

10-16-13 10-17-13 10-18-13 10-16-13 10-17-13 10-18-13 

14:00 -15:00 12:30 -13:33 09:35 -10:35 14:00-16:50 12:30 -15:25 09:35 -12:20 

Low-Btu Liquid Waste 

Feedrate (lbs/hr) 1,783.5 1,563.4 1,725.3 1,787.6 1,685.3 1,707.4 

Low-Btu Liquid Waste Chlorine Concentration (mg/kg) 563 409 388 419 429 408 

Chlorine Feedrate (lb/hr) 1.00 0.64 0.67 0.75 0.72 0.70 

High-Btu Liquid Waste 

Feedrate (lbs/hr) 977.2 1,151.9 1,163.5 1,043.9 1,166.5 1,197.7 

High-Bt High-Btu Liquid Waste Chlorine Concentration (mg/kg) 2,460 1,690 1,910 2,720 1,650 1,810 

Chlorine Feedrate (lb/hr) 2.40 1.95 2.22 2.84 1.92 2.17 

Specialty Liquid Waste 

Feedrate (ibs/hr) 177.5 407.7 248.8 202.9 350.0 244.8 

Specialt Specialty Liquid Waste Chlorine Concentration (mg/kg) 1,480 101 113 696 125 127 

Chlorine Feedrate (lb/hr) 0.26 0.04 0.03 0.14 0.04 0.03 

Containerized Solid Waste 1 

Feedrate (Ibs/hr) 550.6 539.6 516.5 541.9 536.5 523.9 

Containerized Solid Waste 1 Containerized Solid Waste Chlorine Concentration (rag/kg) 482 115 382 195 271 255 1 

Chlorine Feedrate (lb/hr) 0.27 0.06 0.20 0.11 0.15 0.13 

Chlorine Spiking Chlorine Feedrate (lb/hr) 203.1 203.3 197.9 200.3 201.7 200.7 

Total Chlorine Feedrate (lb/hr) 207.0 206.0 201.0 204.2 204.6 203.7 

Average Chlorine Feedrate (lb/hr) 204.7 204.2 

' The weight of the Containerized Solid Waste used to calculate the feedrates of chlorine and metals has been reduced by the weight of the box, and the spiking materials lead nitrate, 

hexachloroethane, and the solution of mercuric nitrate. 

4-43 

VES017772 
Table 4-34. Unit 4 - Chlorine Feedrate 

HC1/C1, Stack Sampling Metals Stack Sampling 

Runl 

10-23-13 

12:36 -13:36 

Run 2 

10-24-13 

12:35 -13:35 

Run 3 

10-25-13 

13:35 -14:35 

Runl 

10-23-13 

12:36 -15:20 

Run 2 

10-24-13 

12:35 -15:15 

Run 3 

10-25-13 

13:35 -16:11 

Low-Btu Liquid Waste to Kil n 

Feedrate (lbs/hr) 1,943.7 1,996.5 1,999.6 1,978.5 1,986.6 1,999.0 

Low-Btu Liquid Waste to Kil n Chlorine Concentration (mg/kg) 416 467 486 413 393 532 

Chlorine Feedrate (lb/hr) 0.81 0.93 0.97 0.82 0.78 1.06 

High-Btu Liquid Waste to Kiln 

Feedrate (lbs/hr) 1,167.0 1,205.4 1,201.0 1,189.2 1,201.2 1,201.8 

High-Bt High-Btu Liquid Waste to Kiln Chlorine Concentration (mg/kg) 1,450 1,390 1,360 1,490 1,360 1,350 

Chlorine Feedrate (Ib/hr) 1.69 1.68 1.63 1.77 1.63 1.62 

Liquid Waste to SCC 

Feedrate (lbs/hr) 1165.6 1203.1 1196.3 1186.2 1201.5 1196.2 

Liquid Waste to SCC Chlorine Concentration (mg/kg) 1,230 1,260 1,280 1,250 2,500 1,250 

Chlorine Feedrate (lb/hr) 1.43 1.52 1.53 1.48 3.00 1.50 

Containerized Solid Waste1 

Feedrate (lbs/hr) 515.3 512.3 498.3 514.2 505.4 507.6 

Containerized Solid Waste1 Containerized Solid Waste Chlorine Concentration (mg/kg) 192 205 207 190 201 180 1 

Chlorine Feedrate (lb/hr) 0.10 0.11 0.10 0.10 0.10 0.09 

Bulk Solid Waste 

Feedrate (lbs/hr) 6,093.0 5,448.0 5,739.0 5,251.5 5,598.4 5,345.0 

Bulk Solid Waste Chlorine Concentration (mg/kg) 184 257 191 219 243 173 

Chlorine Feedrate (Ib/hr) 1.12 1.40 1.10 1.15 1.36 0.92 

Chlorine Spiking Chlorine Feedrate (lb/hr) 197.9 197.9 197.9 200.0 197.2 200.3 

Total Chlorine Feedrate (lb/hr) 203.0 203.5 203.2 205.3 204.1 205.5 

Average Chlorine Feedrate (lb/hr) 203.2 205.0 

The weight of the Containerized Solid Waste used to calculate the feedrates of chlorine and metals has been reduced by the weight of the box, and the spiking materials lead nitrate, 

hexachloroethane, and the solution of mercuric nitrate 

4-44 

VES017773 
Table 4-35. Unit 2 - Ash Feedrate During the EPA Method 5 Stack Sampling for PM 

Run l 

10-8-13 

11:50 -13:00 

Run 2 

10-9-13 

09:45 -10:53 

Run 3 

10-10-13 

09:45 -10:53 

Low-Btu Liquid Waste 

Feedrate (lbs/hr) 1,277.2 1,353.3 1,288.3 

Low-Btu Liquid Waste 

Ash Concentration 

(mg/kg) Low-Btu Liquid Waste 3,140 2,960 3,250 

Ash Feedrate (lb/hr) 4.01 4.01 4.19 

High-Btu Liquid Waste 

Feedrate (lbs/hr) 1,000.2 997.7 998.5 

High-Btu Liquid Waste 

Ash Concentration 

(mg/kg) High-Btu Liquid Waste 1,350 1,010 1,180 

Ash Feedrate (lb/hr) 1.35 1.01 1.18 

Specialty Liquid Waste 

Feedrate (lbs/hr) 270.8 256.5 296.7 

Specialty Liquid Waste 

Ash Concentration 

(mg/kg) Specialty Liquid Waste 649 599 598 

Ash Feedrate (lb/hr) 0.18 0.15 0.18 

Containerized Solid Waste 

Feedrate (lbs/hr) 734.9 738.4 746.0 

Containerized Solid Waste 

Ash Concentration 

(mg/kg) Containerized Solid Waste 675,000 688,000 655,000 

Ash Feedrate (lb/hr) 496.1 508.0 488.6 

Total Ash Feedrate (lb/hr) 501.6 513.2 494.2 

Average Ash Feedrate (lb/hr) 503.0 

4-45 

VES017774 
Table 4-36. Unit 3 - Ash Feedrate During the EPA Method 5 Stack Sampling for PM 

Run l 

10-15-13 

13:16 -14:25 

Run 2 

10-16-13 

11:15 -12:25 

Run 3 

10-17-13 

09:50 -10:57 

Low-Btu Liquid Waste 

Feedrate (lbs/hr) 1,292.9 955.4 1,357.6 

Low-Btu Liquid Waste Ash Concentration (mg/kg) 3,090 4,070 3,650 

Ash Feedrate (lb/hr) 4.00 3.89 4.96 

High-Btu Liquid Waste 

Feedrate (lbs/hr) 847.9 818.2 875.3 

High-Bt High-Btu Liquid Waste Ash Concentration (mg/kg) 1,260 937 599 

Ash Feedrate (lb/hr) 1.07 0.77 0.52 

Specialty Liquid Waste 

Feedrate (lbs/hr) 307.9 269.1 457.4 

Specialt Specialty Liquid Waste Ash Concentration (mg/kg) 591 622 588 

Ash Feedrate (lb/hr) 0.18 0.17 0.27 

Containerized Solid Waste 

Feedrate (lbs/hr) 738.3 742.1 720.7 

Containerize Containerized Solid Waste Ash Concentration (mg/kg) 670,000 682,000 778,000 

Ash Feedrate (lb/hr) 494.7 506.1 560.7 

Total Ash Feedrate (lb/hr) 499.9 510.9 566.5 

Average Ash Feedrate (lb/hr) 525.8 

4-46 

VES017775 
Table 4-37. Unit 4 - Ash Feedrate During the EPA Method 5 Stack Sampling for PM 

Runl 

10-23-13 

09:30 -10:42 

Run 3 

10-25-13 

09:35 - 10:40 

Run 4 

10-25-13 

10:50 -11:55 

Low-Btu Liquid Waste 

Feedrate (lbs/hr) 1,899.6 1,901.0 1,896.8 

Low-Btu Liquid Waste Ash Concentration (mg/kg) 2,790 3,320 3,250 

Ash Feedrate (lb/hr) 5.30 6.31 6.16 

High-Btu Liquid Waste 

Feedrate (lbs/hr) 1,101.4 1,098.1 1,108.9 

High-Bt High-Btu Liquid Waste Ash Concentration (mg/kg) 1,610 1,500 989 

Ash Feedrate (lb/hr) 1.77 1.65 1.10 

Liquid Waste to SCC 

Feedrate (lbs/hr) 1,095.6 1,100.7 1,102.8 

Liquid Waste to SCC Ash Concentration (mg/kg) 744 787 743 

Ash Feedrate (lb/hr) 0.82 0.87 0.82 

Containerized Solid Waste 

Feedrate (lbs/hr) 565.8 568.6 553.8 

Containerize Containerized Solid Waste Ash Concentration (mg/kg) 758,000 724,000 771,000 

Ash Feedrate (lb/hr) 428.9 411.7 427.0 

Bulk Solid Waste 

Feedrate (lbs/hr) 6,286.7 6,408.0 5,992.6 

Bulk Solid Waste Ash Concentration (mg/kg) 695,000 689,000 710,000 

Ash Feedrate (lb/hr) 4,369.2 4,415.1 4,254.8 

Total Ash Feedrate (lb/hr) 4,806.0 4,835.6 4,689.9 

Average Ash Feedrate (lb/hr) 4,777.2 

4-47 

VES017776 
4.3.3 Metals Feedrates 

Feedrates ofthe metals regulated by the HWC MACT (As, Be, Cd, Cr, Pb, and Hg) are 

OPLs for the emission standards for SVM, LVM, and mercury. The feedrates of these six metals 

have been determined during the metals stack sampling in the second part of each run. The stack 

gas concentrations of all six of the HWC MACT metals are determined by EPA Method 29. 

Table 4-38 presents the feedrates of these metals calculated during stack sampling for metals for 

Unit 2. Metals feedrates for Unit 3 are presented in Table 4-40, and metals feedrates for Unit 4 

are presented in Table 4-42. 

The OPLs for metals feedrates are total LV M feedrate (i.e., total and pumpable) and 

pumpable LV M for the emission standard for LV M (i.e., arsenic, beryllium, and chromium); 

(Total) SVM feedrate (i.e., total and pumpable) for the emission standard for SVM (i.e., 

cadmium and lead); and (Total) mercury feedrate (i.e., total and pumpable) for the emission 

standard for mercury. Table 4-39 presents the feedrates of total LV M and pumpable LVM, total 

SVM, and mercury calculated during stack sampling for metals for Unit 2. Total LVM and 

pumpable LVM, total SVM, and mercury feedrates for Unit 3 are presented in Table 4-41, and 

total LVM and pumpable LVM, total SVM, and mercury feedrates for Unit 4 are presented in 

Table 4-43. 

For the calculation of the metals feedrates, the weight ofthe containerized solid waste 

used to calculate the feedrates of metals was reduced by the weight of the box, and the spiking 

materials lead nitrate, hexachloroethane, and the solution of mercuric nitrate to determine the 

feedrate of containerized solid waste that was analyzed for the metals As, Be, Cd, Cr, Pb, and 

Hg. 

4-48 

VES017777 
Table 4-38. Unit 2 - Metals Feedrates 

Runl Run 3 Run 5 

10-8-13 10-10-13 10-30-13 

15:40 -18:43 12:30 -15:10 12:45 -15:32 

Feedrate (lbs/hr) 1,475 1,513 1,396 

Arsenic Cone (mg/kg) 2.7 3.2 2.1 

Beryllium Cone (mg/kg) <0.097 <0.096 <0.097 

Cadmium Cone (mg/kg) 7.2 9 7 

Chromium Cone (mg/kg) 0.8 0.88 0.74 

Lead Cone (mg/kg) 1.1 1.7 1.1 

Low-Btu Liquid Waste Mercury Cone (mg/kg 0.021 0.042 0.052 

Arsenic Feedrate (lbs/hr) 0.00398 0.00484 0.00293 

Beryllium Feedrate (lbs/hr) <0.00014 <0.00015 <0.00014 

Cadmium Feedrate (lbs/hr) 0.0106 0.0136 0.00978 

Chromium Feedrate (lbs/hr) 0.00118 0.00133 0.00103 

Lead Feedrate (lbs/hr) 0.00162 0.00257 0.00154 

Mercury Feedrate (lbs/hr) 0.0000310 0.0000636 0.0000726 

High-Btu Liquid Waste 

Feedrate (lbs/hr) 1,289 1,099 1,165 

High-Btu Liquid Waste 

Arsenic Cone (mg/kg) 8.3 2.8 <0.32 

High-Btu Liquid Waste 

Beryllium Cone (mg/kg) <0.096 <0.099 <0.096 

High-Btu Liquid Waste 

Cadmium Cone (mg/kg) <0.076 <0.078 <0.076 

High-Btu Liquid Waste 

Chromium Cone (mg/kg) 0.26 <0.22 <0.21 

High-Btu Liquid Waste 

Lead Cone (mg/kg) 1 0.67 6.7 

High-Bt High-Btu Liquid Waste Mercury Cone (mg/kg 0.026 0.021 0.096 

Arsenic Feedrate (lbs/hr) 0.0107 0.00308 <0.00037 

High-Btu Liquid Waste 

Beryllium Feedrate (lbs/hr) <0.00012 <0.00011 <0.00011 

High-Btu Liquid Waste 

Cadmium Feedrate (lbs/hr) <0.000098 <0.000086 <0.000089 

High-Btu Liquid Waste 

Chromium Feedrate (lbs/hr) 0.000335 <0.00024 <0.00024 

High-Btu Liquid Waste 

Lead Feedrate (lbs/hr) 0.00129 0.000736 0.00780 

High-Btu Liquid Waste 

Mercury Feedrate (lbs/hr) 0.0000335 0.0000231 0.000112 

Specialty Liquid Waste 

Feedrate (lbs/hr) 433 425 445 

Specialty Liquid Waste 

Arsenic Cone (mg/kg) <0.32 <0.3 <0.31 

Specialty Liquid Waste 

Beryllium Cone (mg/kg) <0.096 <0.092 <0.093 

Specialty Liquid Waste 

Cadmium Cone (mg/kg) <0.076 <0.Q73 <0.073 

Specialty Liquid Waste 

Chromium Cone (mg/kg) <0.21 <0.2 <0.2 

Specialty Liquid Waste 

Lead Cone (mg/kg) <0.27 <0.26 <0.26 

Specialt Specialty Liquid Waste Mercury Cone (mg/kg <0.009 <0.0086 <0.0099 

Arsenic Feedrate (lbs/hr) <0.00014 <0.00013 <0.00014 

Specialty Liquid Waste 

Beryllium Feedrate (lbs/hr) <0.000042 <0.000039 <0.000041 

Specialty Liquid Waste 

Cadmium Feedrate (lbs/hr) <0.000033 <0.000031 <0.000033 

Specialty Liquid Waste 

Chromium Feedrate (lbs/hr) <0.000091 <0.000085 <0.000089 

Specialty Liquid Waste 

Lead Feedrate (lbs/hr) <0.00012 <0.00011 <0.00012 

Specialty Liquid Waste 

Mercury Feedrate (lbs/hr) <0.0000039 <0.0000037 <0.0000044 

Containerized Solid Waste1 

Feedrate (lbs/hr) 547 536 542 

Containerized Solid Waste1 

Arsenic Cone (mg/kg) 8.8 7.5 8.8 

Containerized Solid Waste1 

Beryllium Cone (mg/kg) 0.48 0.61 0.73 

Containerized Solid Waste1 

Cadmium Cone (mg/kg) 0.082 <0.077 0.084 

Containerized Solid Waste1 

Chromium Cone (mg/kg) 12.8 19.3 16.7 

Containerized Solid Waste1 

Lead Cone (mg/kg) 11.6 11.7 13.5 

Containerized Solid Waste Containerized Solid Waste1 Mercury Cone (mg/kg 0.045 0.022 0.016 1 

Arsenic Feedrate (lbs/hr) 0.00481 0.00402 0.00477 

Containerized Solid Waste1 

Beryllium Feedrate (lbs/hr) 0.000263 0.000327 0.000396 

Containerized Solid Waste1 

Cadmium Feedrate (lbs/hr) 0.0000449 <0.000041 0.0000456 

Containerized Solid Waste1 

Chromium Feedrate (lbs/hr) 0.00700 0.0103 0.00906 

Containerized Solid Waste1 

Lead Feedrate (lbs/hr) 0.00635 0.00627 0.00732 

Containerized Solid Waste1 

Mercury Feedrate (lbs/hr) 0.0000246 0.0000118 0.00000868 

4-49 

VES017778 
Table 4-38. (continued) Unit 2 - Metals Feedrates 

Runl 

10-8-13 

15:40 -18:43 

Run 3 

10-10-13 

12:30 -15:10 

Run 5 

10-30-13 

12:45 -15:32 

Spiking 

Arsenic Feedrate (lbs/hr) 0 0 0 

Spiking 

Beryllium Feedrate (lbs/hr) 0 0 0 

Spiking 

Cadmium Feedrate (lbs/hr) 0 0 0 Spiking Chromium Feedrate (lbs/hr) 45.8 47.3 45.8 Spiking 

Lead Feedrate (lbs/hr) 61.9 61.7 62.0 

Spiking 

Mercury Feedrate (lbs/hr) 0.00196 0.00196 0.00204 

Pumpable Feedrate2 

Arsenic Feedrate (lbs/hr) 0.0147 0.00792 0.00293 

Pumpable Feedrate2 

Beryllium Feedrate (lbs/hr) 0 0 0 

Pumpable Feedrate2 Cadmium Feedrate (lbs/hr) 0.0106 0.0136 0.00978 Pumpable Feedrate2 

Chromium Feedrate (lbs/hr) 45.8 47.3 45.9 Pumpable Feedrate2 

Lead Feedrate (lbs/hr) 0.00291 0.00331 0.00934 

Pumpable Feedrate2 

Mercury Feedrate (lbs/hr) 0.0000645 0.0000866 0.000184 

Total Feedrate2 

Arsenic Feedrate (lbs/hr) 0.0195 0.0119 0.00771 

Total Feedrate2 

Beryllium Feedrate (lbs/hr) 0.000263 0.000327 0.000396 

Total Feedrate2 Cadmium Feedrate (lbs/hr) 0.0107 0.0136 0.00982 Total Feedrate2 

Chromium Feedrate (lbs/hr) 45.8 47.3 45.9 Total Feedrate2 

Lead Feedrate (lbs/hr) 61.9 61.7 62.0 

Total Feedrate2 

Mercury Feedrate (lbs/hr) 0.00205 0.00206 0.00224 

' The weight ofthe Containerized Solid Waste used to calculate the feedrates of chlorine and metals has been reduced by 

the weight of the box, and the spiking materials lead nitrate, hexachloroethane, and the solution of mercuric nitrate. 

2

 Non-detects treated as a zero "0". 

4-50 

VES017779 
Table 4-39. Unit 2 - HWC MACT Metals Feedrates 

Units 

Runl 

10-8-13 

15:40 -18:43 

Run 3 

10-10-13 

12:30 -15:10 

Run 5 

10-30-13 

12:45 -15:32 

Average 

Arsenic (Total) lb/hr 0.0195 0.0119 0.0077 0.0130 

Beryllium (Total) lb/hr 0.00026 0.00033 0.00040 0.00033 

Chromium (Total) lb/hr 45.8 47.3 45.9 46.3 

Total LVM (Arsenic, Beryllium, 

Chromium) lb/hr 45.9 473 45.9 46.3 

Arsenic (Pumpable) lb/hr 0.0147 0.0079 0.0029 0.0085 

Beryllium (Pumpable) lb/hr 0.0000 0.0000 0.0000 0.0000 

Chromium (Pumpable) lb/hr 45.8 47.3 45.9 46.3 

Pumpable LVM (Arsemc, Beryllium, 

Chromium) lb/hr 45.9 47.3 45.9 46.3 

Cadmium lb/hr 0.0107 0.0136 0.0098 0.0114 

Lead lb/hr 61.9 61.7 62.0 61.9 

Total SVM (Cadmium, Lead) lb/hr 61.9 61.7 62.0 61.9 

Mercury lb/hr 0.00205 0.00206 0.00224 0.00212 

4-51 

VES017780 
Table 4-40. Unit 3 - Metals Feedrates 

Run 2 Run 3 Run 4 

10-16-13 10-17-13 10-18-13 

14:00 -16:50 12:30 -15:25 09:35 -12:20 

Feedrate (lbs/hr) 1,788 1,685 1,707 

Arsenic Cone (mg/kg) 4.8 3.2 3.3 

Beryllium Cone (mg/kg) <0.096 <0.097 <0.096 

Low-Btu Liquid Waste 

Cadmium Cone (mg/kg) 15.2 9.4 11.3 

Low-Btu Liquid Waste 

Chromium Cone (mg/kg) 1.3 0.87 0.97 

Low-Btu Liquid Waste 

Lead Cone (mg/kg) 3.1 1.9 1.9 

Low-Btu Liquid Waste Mercury Cone (mg/kg 0.065 0.049 0.08 

Arsenic Feedrate (lbs/hr) 0.00858 0.00539 0.00563 

Low-Btu Liquid Waste 

Beryllium Feedrate (Ibs/hr) <0.00017 <0.00016 <0.00016 

Low-Btu Liquid Waste 

Cadmium Feedrate (lbs/hr) 0.0272 0.0158 0.0193 

Low-Btu Liquid Waste 

Chromium Feedrate (lbs/hr) 0.00232 0.00147 0.00166 

Low-Btu Liquid Waste 

Lead Feedrate (lbs/hr) 0.00554 0.00320 0.00324 

Low-Btu Liquid Waste 

Mercury Feedrate (lbs/hr) 0.000116 0.0000826 0.000137 

High-Btu Liquid Waste 

Feedrate (lbs/hr) 1,044 1,167 1,198 

High-Btu Liquid Waste 

Arsemc Cone (mg/kg) 12.4 1.7 2.4 

High-Btu Liquid Waste 

Beryllium Cone (mg/kg) <0.095 <0.1 <0.096 

High-Btu Liquid Waste 

Cadmium Cone (mg/kg) <0.075 <0.079 <0.076 

High-Btu Liquid Waste 

Chromium Cone (mg/kg) <0.21 <0.22 <0.21 

High-Btu Liquid Waste 

Lead Cone (mg/kg) 1.8 1 1.3 

High-Bt High-Btu Liquid Waste Mercury Cone (mg/kg 0.027 0.029 0.022 

Arsenic Feedrate (lbs/hr) 0.0129 0.00198 0.00287 

High-Btu Liquid Waste 

Beryllium Feedrate (lbs/hr) <0.000099 <0.00012 <0.00011 

High-Btu Liquid Waste 

Cadmium Feedrate (lbs/hr) <0.000078 <0.000092 <0.000091 

High-Btu Liquid Waste 

Chromium Feedrate (lbs/hr) <0.00022 <0.00026 <0.00025 

High-Btu Liquid Waste 

Lead Feedrate (lbs/hr) 0.00188 0.00117 0.00156 

High-Btu Liquid Waste 

Mercury Feedrate (lbs/hr) 0.0000282 0.0000338 0.0000263 

Specialty Liquid Waste 

Feedrate (lbs/hr) 203 350 245 

Specialty Liquid Waste 

Arsenic Cone (mg/kg) <0.32 <0.32 <0.33 

Specialty Liquid Waste 

Beryllium Cone (mg/kg) <0.098 <0.096 <0.099 

Specialty Liquid Waste 

Cadmium Cone (mg/kg) <0.077 <0.076 <0.078 

Specialty Liquid Waste 

Chromium Cone (mg/kg) <0.22 <0.21 <0.22 

Specialty Liquid Waste 

. Lead Cone (mg/kg) <0.27 <0.27 <0.28 

Specialt Specialty Liquid Waste Mercury Cone (mg/kg <0.0088 <0.0094 <0.0099 

Arsenic Feedrate (lbs/hr) <0.000065 <0.00011 <0.000081 

Specialty Liquid Waste 

Beryllium Feedrate (lbs/hr) <0.000020 <0.000034 <0.000024 

Specialty Liquid Waste 

Cadmium Feedrate (lbs/hr) <0.000016 <0.000027 <0.000019 

Specialty Liquid Waste 

Chromium Feedrate (lbs/hr) <0.000045 <0.000073 <0.000054 

Specialty Liquid Waste 

Lead Feedrate (lbs/hr) <0.000055 <0.000094 <0.000069 

Specialty Liquid Waste 

Mercury Feedrate (lbs/hr) <0.0000018 <0.0000033 •cO.0000024 

Containerized Solid Waste1 

Feedrate (lbs/hr) 542 537 524 

Containerized Solid Waste1 

Arsenic Cone (mg/kg) 7.5 6.4 8.4 

Containerized Solid Waste1 

Beryllium Cone (mg/kg) 0.58 0.55 0.79 

Containerized Solid Waste1 

Cadmium Cone (mg/kg) <0.071 <0.076 <0.071 

Containerized Solid Waste1 

Chromium Cone (mg/kg) 13.6 13.7 18.9 

Containerized Solid Waste1 

Lead Cone (mg/kg) 11.1 10.7 14.1 

Containerized Solid Waste Containerized Solid Waste1 Mercury Cone (mg/kg 0.028 0.028 0.026 1 

Arsenic Feedrate (lbs/hr) 0.00406 0.00343 0.00440 

Containerized Solid Waste1 

Beryllium Feedrate (lbs/hr) 0.000314 0.000295 0.000414 

Containerized Solid Waste1 

Cadmium Feedrate (lbs/hr) <0.000038 <0.000041 <0.000037 

Containerized Solid Waste1 

Chromium Feedrate (lbs/hr) 0.00737 0.00735 0.00990 

Containerized Solid Waste1 

Lead Feedrate (lbs/hr) 0.00601 0.00574 0.007393 

Containerized Solid Waste1 

Mercury Feedrate (lbs/hr) 0.0000152 0.0000150 0.0000136 

4-52 

VES017781 
Table 4-40. (continued) Unit 3 - Metais Feedrates 

Run 2 

10-16-13 

14:00 -16:50 

Run 3 

10-17-13 

12:30 -15:25 

Run 4 

10-18-13 

09:35 -12:20 

Spiking 

Arsenic Feedrate (lbs/hr) 0 0 0 

Spiking 

Beryllium Feedrate (lbs/hr) 0 0 0 

Spiking 

Cadmium Feedrate (lbs/hr) 0 0 0 Spiking Chromium Feedrate (lbs/hr) 46.3 46.1 45.7 Spiking 

Lead Feedrate (lbs/hr) 62.1 62.5 62.2 

Spiking 

Mercury Feedrate (lbs/hr) 0.00204 0.00200 0.00209 

Pumpable Feedrate2 

Arsenic Feedrate (lbs/hr) 0.0215 0.00738 0.00851 

Pumpable Feedrate2 

Beryllium Feedrate (lbs/hr) 0 0 0 

Pumpable Feedrate2 Cadmium Feedrate (lbs/hr) 0.0272 0.0158 0.0193 Pumpable Feedrate2 

Chromium Feedrate (lbs/hr) 46.3 46.1 45.7 Pumpable Feedrate2 

Lead Feedrate (lbs/hr) 0.00742 0.00437 0.00480 

Pumpable Feedrate2 

Mercury Feedrate (lbs/hr) 0.000144 0.000116 0.000163 

Total Feedrate2 

Arsemc Feedrate (lbs/hr) 0.0256 0.0108 0.0129 

Total Feedrate2 

Beryllium Feedrate (lbs/hr) 0.000314 0.000295 0.000414 

Total Feedrate2 Cadmium Feedrate (lbs/hr) 0.0272 0.0158 0.0193 Total Feedrate2 

Chromium Feedrate (lbs/hr) 46.3 46.1 45.7 Total Feedrate2 

Lead Feedrate (lbs/hr) 62.1 62.5 62.2 

Total Feedrate2 

Mercury Feedrate (lbs/hr) 0.00220 0.00213 0.00226 

1

 The weight of the Containerized Solid Waste used to calculate the feedrates of chlorine and metals has been reduced by the 

weight of the box, and the spiking materials lead nitrate, hexachloroethane, and the solution of mercuric nitrate. 

2

 Non-detects treated as a zero "0". 

/ 

Table 4-41. Unit 3 - HWC MACT Metals Feedrates 

Units 

Run2 

10-16-13 

14:00 -16:50 

Run 3 

10-17-13 

12:30-15:25 

Run 4 

10-18-13 

09:35 -12:20 

Average 

Arsenic (Total) lb/hr 0.0256 0.0108 0.0129 0.0164 

Beryllium (Total) lb/hr 0.00031 0.00030 0.00041 0.00034 

Chromium (Total) lb/hr 46.3 46.1 45.7 46.0 

Total LVM (Arsenic, Beryllium, Chromium) lb/hr 46.3 46.1 45.8 46.1 

Arsenic (Pumpable) lb/hr 0.02152 0.00738 0.00851 0.01247 

Beryllium (Pumpable) lb/hr 0.00000 0.00000 0.00000 0.000000 

Chromium (Pumpable) Ib/hr 46.3 46.1 45.7 46.0 

Pumpable LVM (Arsenic, Beryllium, Chromium) Ib/hr 46.3 46.1 45.7 46.0 

Cadmium lb/hr 0.02717 0.01584 0.01929 0.02077 

Lead lb/hr 62.1 62.5 62.2 62.3 

Total SVM (Cadmium, Lead) lb/hr 62.1 62.5 62.2 62.3 

Mercury lb/hr 0.00220 0.00213 0.00226 0.00220 

4-53 

VES017782 
Table 4-42. Unit 4 - Metals Feedrates 

Runl Run 2 Run 3 

10-23-13 10-24-13 10-25-13 

12:36 -15:20 12:35 -15:15 13:35 -16:11 

Feedrate (lbs/hr) 1,979 1,987 1,999 

Arsenic Cone (mg/kg) 5.5 4.9 2.9 

Beryllium Cone (mg/kg) <0.094 <0.098 <0.096 

Cadmium Cone (mg/kg) 13.6 12.1 9.4 

Chromium Cone (mg/kg) 1.3 1.2 0.84 

Lead Cone (mg/kg) 3.3 2.9 1.6 

Low-Btu Liquid Waste to Kiln Mercury Cone (mg/kg 0.11 0.14 0.11 

Arsenic Feedrate (lbs/hr) 0.0109 0.00973 0.00580 

Beryllium Feedrate (lbs/hr) <0.00019 <0.00019 <0.00019 

Cadmium Feedrate (lbs/hr) 0.0269 0.0240 0.0188 

Chromium Feedrate (lbs/hr) 0.00257 0.00238 0.00168 

Lead Feedrate (lbs/hr) 0.00653 0.00576 0.00320 

Mercury Feedrate (lbs/hr) 0.000218 0.000278 0.000220 

High-Btu Liquid Waste to Kiln 

Feedrate (lbs/hr) 1,189 1,201 1,202 

High-Btu Liquid Waste to Kiln 

Arsenic Cone (mg/kg) 1.4 0.37 <0.32 

High-Btu Liquid Waste to Kiln 

Beryllium Cone (mg/kg) <0.099 <0.093 <0.097 

High-Btu Liquid Waste to Kiln 

Cadmium Cone (mg/kg) 0.12 <0.073 <0.077 

High-Btu Liquid Waste to Kiln 

Chromium Cone (mg/kg) 0.24 <0.2 <0.21 

High-Btu Liquid Waste to Kiln 

Lead Cone (mg/kg) 1.1 0.4 <0.27 

High-Bt High-Btu Liquid Waste to Kiln Mercury Cone (mg/kg 0.048 0.021 0.018 

Arsenic Feedrate (lbs/hr) 0.00166 0.000444 <0.00038 

High-Btu Liquid Waste to Kiln 

Beryllium Feedrate (lbs/hr) <0.00012 <0.00011 <0.00012 

High-Btu Liquid Waste to Kiln 

Cadmium Feedrate (lbs/hr) 0.000143 <0.000088 <0.000093 

High-Btu Liquid Waste to Kiln 

Chromium Feedrate (lbs/hr) 0.000285 <0.00024 <0.00025 

High-Btu Liquid Waste to Kiln 

Lead Feedrate (lbs/hr) 0.00131 0.000480 <0.00032 

High-Btu Liquid Waste to Kiln 

Mercury Feedrate (lbs/hr) 0.0000571 0.0000252 0.0000216 

Liquid Waste to SCC 

Feedrate (lbs/hr) 1,186 1,202 1,196 

Liquid Waste to SCC 

Arsenic Cone (mg/kg) <0.3 <0.32 <0.31 

Liquid Waste to SCC 

Beryllium Cone (mg/kg) <0.092 <0.098 <0.094 

Liquid Waste to SCC 

Cadmium Cone (mg/kg) <0.073 <0.077 <0.074 

Liquid Waste to SCC 

Chromium Cone (mg/kg) <0.2 <0.22 <0.21 

Liquid Waste to SCC 

Lead Cone (mg/kg) 0.26 <0.27 <0.26 

Liquid Waste to SCC Mercury Cone (mg/kg 0.017 0.019 0.017 

Arsenic Feedrate (lbs/hr) <0.00036 <0.00038 <0.00037 

Liquid Waste to SCC 

Beryllium Feedrate (lbs/hr) <0.00011 <0.00012 <0.00011 

Liquid Waste to SCC 

Cadmium Feedrate (lbs/hr) <0.000087 <0.000093 <0.000089 

Liquid Waste to SCC 

Chromium Feedrate (lbs/hr) <0.00024 <0.00026 <0.00025 

Liquid Waste to SCC 

Lead Feedrate (lbs/hr) 0.000308 <0.00032 <0.00031 

Liquid Waste to SCC 

Mercury Feedrate (lbs/hr) 0.0000202 0.0000228 0.0000203 

Containerized Sohd Waste1 

Feedrate (lbs/hr) 514 505 508 

Containerized Sohd Waste1 

Arsenic Cone (mg/kg) 2.4 2 2.1 

Containerized Sohd Waste1 

Beryllium Cone (mg/kg) 0.13 0.16 <0.1 

Containerized Sohd Waste1 

Cadmium Cone (mg/kg) 0.46 0.43 0.45 

Containerized Sohd Waste1 

Chromium Cone (mg/kg) 45.2 58.9 35.1 

Containerized Sohd Waste1 

Lead Cone (mg/kg) 35.9 212 25.4 

Containerized Sohd Waste Containerized Sohd Waste1 Mercury Cone (mg/kg 0.18 0.24 0.26 1 

Arsenic Feedrate (lbs/hr) 0.00123 0.00101 0.00107 

Containerized Sohd Waste1 

Beryllium Feedrate (lbs/hr) 0.0000668 0.0000809 <0.000051 

Containerized Sohd Waste1 

Cadmium Feedrate (lbs/hr) 0.000237 0.000217 0.000228 

Containerized Sohd Waste1 

Chromium Feedrate (lbs/hr) 0.0232 0.0298 0.0178 

Containerized Sohd Waste1 

Lead Feedrate (lbs/hr) 0.0185 0.107 0.0129 

Containerized Sohd Waste1 

Mercury Feedrate (lbs/hr) 0.0000926 0.000121 0.000132 

4-54 

VES017783 
Table 4-42. (continued) Unit 4 - Metals Feedrates 

Runl 

10-23-13 

12:36 -15:20 

Run 2 

10-24-13 

12:35 -15:15 

Run 3 

10-25-13 

13:35 -16:11 

Bulk Solid Waste 

Feedrate (lbs/hr) 5251 5598 5345 

Bulk Solid Waste 

Arsenic Cone (mg/kg) 2.2 3 2.2 

Bulk Solid Waste 

Beryllium Cone (mg/kg) 0.21 0.28 0.26 

Bulk Solid Waste 

Cadmium Cone (mg/kg) 0.28 0.37 0.3 

Bulk Solid Waste 

Chromium Cone (mg/kg) 35.6 37.9 29.8 

Bulk Solid Waste 

Lead Cone (mg/kg) 41 58.1 26.6 

Bulk Solid Waste Mercury Cone (mg/kg 0.082 0.12 0.077 

Arsenic Feedrate (lbs/hr) 0.0116 0.0168 0.0118 

Bulk Solid Waste 

Beryllium Feedrate (lbs/hr) 0.00110 0.00157 0.00139 

Bulk Solid Waste 

Cadmium Feedrate (lbs/hr) 0.00147 0.00207 0.00160 

Bulk Solid Waste 

Chromium Feedrate (lbs/hr) 0.187 0.212 0.159 

Bulk Solid Waste 

Lead Feedrate (lbs/hr) 0.215 0.325 0.142 

Bulk Solid Waste 

Mercury Feedrate (lbs/hr) 0.000431 0.000672 0.000412 

Spiking 

Arsenic Feedrate (lbs/hr) 0 0 0 

Spiking 

Beryllium Feedrate (lbs/hr) 0 0 0 

Spiking 

Cadmium Feedrate (lbs/hr) 0 0 0 

Spiking Chromium Feedrate (lbs/hr) 46.0 46.0 45.8 Spiking 

Lead Feedrate (lbs/hr) 62.0 61.1 62.0 

Spiking 

Mercury Feedrate (lbs/hr) 0.0393 0.0388 0.0394 

Pumpable Feedrate2 

Arsenic Feedrate (lbs/hr) 0.0125 0.0102 0.00580 

Pumpable Feedrate2 

Beryllium Feedrate (lbs/hr) 0 0 0 

Pumpable Feedrate2 Cadmium Feedrate (lbs/hr) 0.0271 0.0240 0.0188 Pumpable Feedrate2 

Chromium Feedrate (lbs/hr) 46.0 46.0 45.8 Pumpable Feedrate2 

Lead Feedrate (lbs/hr) 0.00815 0.00624 0.00320 

Pumpable Feedrate2 

Mercury Feedrate (lbs/hr) 0.000295 0.000326 0.000262 

Total Feedrate2 

Arsenic Feedrate (lbs/hr) 0.0253 0.0280 0.0186 

Total Feedrate2 

Beryllium Feedrate (lbs/hr) 0.00117 0.00165 0.00139 

Total Feedrate2 Cadmium Feedrate (lbs/hr) 0.0288 0.0263 0.0206 Total Feedrate2 

Chromium Feedrate (lbs/hr) 46.2 46.3 46.0 Total Feedrate2 

Lead Feedrate (lbs/hr) 62.2 61.5 62.2 

Total Feedrate2 

Mercury Feedrate (lbs/hr) 0.0402 0.0399 0.0402 

1

 The weight of the Containerized Solid Waste used to calculate the feedrates of chlorine and metals has been reduced by 

the weight of the box, and fhe spiking materials lead nitrate, hexachloroethane, and the solution of mercuric nitrate. 

Non-detects treated as a zero "0". 

4-55 

VES017784 
Table 4-43. Unit 4 - HWC MACT Metals Feedrates 

Units 

Runl Run 3 Run 5 

Units 10-8-13 Average 

15:40 -18:43 

10-10-13 

12:30 -15:10 

10-30-13 

12:45 -15:32 

Average 

Arsenic (Total) lb/hr 0.0253 0.0280 0.0186 0.0240 

Beryllium (Total) lb/hr 0.00117 0.00165 0.00139 0.00140 

Chromium (Total) lb/hr 46.2 46.3 46.0 46.1 

Total LVM (Arsenic, Beryllium, Chromium) lb/hr 46.2 46.3 46.0 46.2 

Arsenic (Pumpable) lb/hr 0.0125 0.0102 0.0058 0.0095 

Beryllium (Pumpable) Ib/hr 0.00000 0.00000 0.00000 0.000000 

Chromium (Pumpable) lb/hr 46.0 46.0 45.8 45.9 

Pumpable LVM (Arsenic, Beryllium, Chromium) lb/hr 46.0 46.0 45.8 45.9 

Cadmium lb/hr 0.0288 0.0263 0.0206 0.0252 

Lead lb/hr 62.2 61.5 62.2 62.0 

Total SVM (Cadmium, Lead) lb/hr 62.2 61.6 62.2 62.0 

Mercury lb/hr 0.0402 0.0399 0.0402 0.O401 

4-56 

VES017785 
5.0 Quality Assurance/Quality Control 

As part of the comprehensive performance test, a project-specific quality 

assurance/quality control (QA/QC) effort was developed and implemented. This QA/QC effort 

was documented in the QAPjP, and was tailored to meet the specific needs of this test effort. 

The results ofthe QA/QC activities demonstrate that the quality of project 

measurement data is well documented and that the data are reliable, defensible, and 

meet project objectives. 

The primary objectives of the QA/QC effort were to control, assess, and document data 

quality. To accomplish these objectives, the QA/QC approach consisted of the following key 

elements: 

• Definition of quality assurance objectives that reflect the overall technical objectives 

of the measurement program; 

• Design of a sampling, analytical, QA/QC and data analysis system to meet those 

objectives; 

• Evaluation of the performance of the measurement system; and 

• Initiation of corrective action when measurement system performance does not meet 

the specifications 

The CPT of the incinerators at Veolia Sauget was conducted in accordance with the QA 

procedures described in the Quality Assurance Project Plan for the Comprehensive Performance 

Test ofthe Units 2 and 3 Fixed Hearth Incinerators and the Unit 4 Rotary Kiln Incinerator, 

September 25, 2013. These QA procedures include sampling and analytical procedures, along 

with specified calibration requirements, QC checks, data reduction and validation procedures, 

and sample tracking. A review of analytical results for QA/QC samples and assessment of 

overall data quality is presented in this section. Detailed QC information is presented in the 

appendices to this report. 

The sections below present discussions of the QA/QC activities associated with the 

overall quality ofthe data associated with the CPT. Although several minor issues are identified 

and discussed in the following sections, the overall conclusion of the QA/QC assessment is that 

the results of the testing are of high quality, and are appropriate for their intended use. 

A few minor issues were identified during the QA/QC assessment. These issues and their 

impact on data usability are discussed in greater detail in following sections. 

5-1 
5.1 Audit Samples 

Audit samples were acquired from a Sigma-Aldrich RTC for metals and hydrogen 

chloride. These samples were submitted to the analytical laboratory along with the samples 

collected during the CPT. These results are included on the laboratory reports generated by Test 

America. The evaluation of the results by Sigma Aldrich RTC is presented in Appendix G6. 

The results ofthe audit samples are summarized in Table 5-1. Laboratory analysis of each audit 

sample was rated as "Acceptable". 

Table 5-1. Results of Analysis of Audit Samples 

Result 

Assigned 

Value 

Evaluation 

Metals on Filter 

Arsenic (ug/filter) 20.31 21.0 Acceptable 

Beryllium (pig/filter) 12.16 11.3 Acceptable 

Cadmium (ug/filter) 11.72 11.2 Acceptable 

Chromium (u.g/filter) 17.67 16.1 Acceptable 

Lead (u.g/filter) 21.60 21.0 Acceptable 

Metals in Impinger Solution 

Arsenic (ug/ml) 0.1884 0.201 Acceptable 

Beryllium (|ig/ml) 0.0576 0.0530 Acceptable 

Cadmium (ug/ml) 0.1053 0.105 Acceptable 

Chromium (ug/ml) 0.2017 0.202 Acceptable 

Lead (ug/ml) 0.2102 0.202 Acceptable 

Mercury (ng/ml) 13.9 15.0 Acceptable 

Hydrogen Chloride in Impinger Solution (mg/L) 30.4 27.6 Acceptable 

5.2 Analysis of Waste Feeds 

5.2.1 Analysis of Waste Feeds for Metals 

Samples of waste feed materials were analyzed for mercury using CVAA, according to 

SW-846 Method 7470A. These same samples were also analyzed for arsenic, beryllium, 

cadmium, chromium, and lead using ICPES, according to SW-846 Method 6010B. These 

samples were prepared for analysis using appropriate extraction or dilution techniques. Quality 

assurance and quality control activities associated with these analyses included: 

• Sample handling and preservation; 

• Preparation and analysis of samples within specified holding times; 

• Preparation and analysis of laboratory blanks; 

5-2 

VES017787 
• Preparation and analysis of laboratory control samples; 

• Duplicate preparation and analysis of received samples; 

• Analysis of duplicate samples; and 

• Preparation and analysis of matrix spike (MS) and matrix spike duplicate (MSD) 

samples. 

Review of these QA/QC activities indicates that these data are supportable, and useable. 

Seethe detailed data quality assessment in Appendix H. The following issues were identified as 

part of this data quality assessment: 

• The QAPjP specifies the performance of matrix spike/matrix spike duplicates with 

75-125% recovery, 0-20% RPD for mercury and 70-130% recovery, 0-20% RPD for 

other metals. One hundred eighty-seven of 204 MS or MSD met the specifications for 

recovery. One hundred of 102 MS/MSD pairs met the specification for RPD. The 

following samples were outside the specification: 

— VS2-CS-11B-COMP2B: Arsenic recovery 67% in MS, arsenic RPD 23%, 

chromium recovery 149% and 172% in MS/MSD; 

— VS2-CS-15B-COMP2B: chromium recovery 150% in MSD; 

— VS3-CS-12B-COMP2B: chromium recovery 131 and 145% in MS/MSD; 

— VS4-BS-13B-COMP2B: chromium recovery 132 and 134% in MS/MSD, lead 

recovery 208% in MSD; 

— VS4-CS-13B-COMP2B: chromium recovery 164 and 186% in MS/MSD, lead 

recovery 406% in MS, lead RPD 49%, mercury recovery 61 and 45% in 

MS/MSD; and 

— VS4-LBW-12B-COMP2B: cadmium recovery 145% in MSD, mercury recovery 

71 and 66% in MS/MSD. 

Metals feedrates are developed as a sum of totals fed to the system as LVM (arsenic, 

beryllium and chromium); SVM (cadmium and lead) and mercury. The MS/MSD 

outliers detailed above indicate increased uncertainty in the concentrations of the 

metals in those streams. The contribution of these streams to the total feedrates of 

LVM, SVM and mercury are negligible, and the increased uncertainty in these 

concentrations has no impact on the conclusions of the report. No data are qualified 

or invalidated based on MS/MSD results. 

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5.2.2 Analysis of Waste Feeds for Physical and Chemical Parameters 

Samples of liquid and solid waste feed materials were analyzed for ash content, total 

chlorine, density, gross calorific value, kinematic viscosity, and percent moisture, using the 

following methods: 

• Ash Content: ASTMD482; 

• Total Chlorine: KNOXWC-0016; 

• Density: ASTM D1963; 

• Gross Calorific Value: ASTM D240, ASTM D5865; 

• Kinematic Viscosity: ASTM D 445; and 

• Percent Moisture: Method 160.3, ASTM D017. 

Quality assurance and quality control activities associated with these analyses included: 

• Sample handling and preservation; 

• Preparation and analysis of samples within specified holding times; 

• Preparation and analysis of laboratory blanks; 

• Preparation and analysis of laboratory control samples; 

• Preparation and analysis of matrix spike and matrix spike duplicate samples; 

• Collection and analysis of duplicate samples; and 

• Preparation and analysis of selected samples in duplicate. 

Review of these QA/QC activities indicates that data are supportable, and usable for the purpose 

of demonstrating regulatory compliance. See the detailed data quality assessment in Appendix H. 

The following issues were identified during the course of the QA/QC assessment: 

• Selected samples were analyzed in duplicate. Ninety of 96 duplicate analyses met the 

QAPP specifications (see table below). The outliers are: 

- Ash in VS2-HBW-13B-COMP2B; results of 582 and 646 mg/kg; RPD of 10.4%; 

- Gross Calorific Value in VS2-LBW-15B-COMP2B; results of 178 and 152 

Btu/lb; RPD of 15.8%; 

- Chlorine in VS3-CS-11A-COMP 1; results of 253 and 325 mg/kg; RPD of 24.9%; 

- Chlorine in VS4-BS-11A-COMP1; results of 171 and 221 mg/kg; RPD of 25.5%; 

- Ash in VS4-HBW-12B-COMP2B-DUP; results of 943 and 1050 mg/kg; RPD of 

10.7%; and 

- Ash VS4-HBW-13A-COMP1; results of 1,500 and 928 mg/kg; RPD of 47.1%. 

The outliers for duplicate analysis have a negligible impact on the usability of the 

data. The chlorine carried in containerized solids and bulk sohds is negligible (<1%) 

compared to the chlorine provided by the spiking material. The ash carried in highBtu waste is negligible (<1%) compared to the ash provided by the bulk or 

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VES017789 
containerized solids. The heat input results in low-Btu waste are near the detection 

limit. Increased uncertainty is expected close to the detection limit. No data are 

qualified or invalidated based on the results of duplicate analysis. 

• No duplicate analysis was performed for moisture in solid waste streams. This 

duplicate analysis was specified in the QAPjP. This has no impact on the usability of 

the data. Moisture results are used only to characterize the waste feed materials, and 

are not used in any demonstration of compliance. No data are qualified or invalidated 

based on this omission. 

5.3 Stack Gas 

5.3.1 Isokinetic Sample Collection 

Isokinetic sampling trains were used for the collection of samples for the determination 

of: 

• Particulate matter according to EPA Method 5; 

• Hydrogen chloride and chlorine according to Modified EPA Method 26A; 

• Metals according to EPA Method 29; and Polychlorinated dibenzodioxins and 

polychlorinated dibenzofurans according to SW-846 Method 0023A. 

Quality assurance and quality control activities associated with the collection of these samples 

included: 

• Collection of the specified volumes of stack gas over the specified duration; 

• Collection of stack gas within 90-110% of isokinetic; 

• Maintaining the probe, filter and (on applicable trains) heated transfer line at the 

specified temperatures; 

• Maintaining the impinger exit and (on applicable trains) the condenser exit at the 

specified temperature; 

• Performing sampling train leak checks before sample collection, at port changes, and 

after sample collection; 

• Performing pitot tube leak checks before and after sample collection; and 

• Recording all data on pre-printed data sheets. 

Review of these QA/QC activities indicates that sampling was performed according to the 

methods and the QAPjP. See the detailed data quality assessment in Appendix H. Samphng data 

sheets are presented in Appendix F. Calibration documentation for all field equipment is 

presented in Appendix I. No issues were identified as part of the data quality assessment. 

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5.3.2 Analysis of Stack Gas Samples for Determination of PM 

Samples of stack gas for determination of particulate matter (PM) were collected in a 

sampling train meeting the requirements EPA Method 5. 

Quality assurance and quality control activities associated with this analysis included: 

• Sample handling and preservation; 

• Preparation and analysis of samples within specified holding times; 

• Preparation and analysis of laboratory blanks; 

• Collection and analysis of field blanks; 

• Repeatability of sequential weighings; and 

• Daily balance cahbration. 

Review of these QA/QC activities indicates that these data are supportable, and useable. See the 

detailed data quality assessment in Appendix H. The following issue was identified during the 

QA/QC review: 

• The field blank probe and nozzle rinse had observable levels near the detection limit. 

The levels of particulate material observed in the PNR samples were very low, and 

near the detection limit. Levels in the field samples were similar to these results, and 

may have a positive bias. As a positive bias is conservative relative to the estimation 

of emissions, no data are qualified or invalidated based on field blank results. 

5.3.3 Analysis of Stack Gas Samples for Determination of HCI/CI2 

Samples of stack gas for determination of hydrogen chloride and chlorine (HCI/CI2) were 

collected in a Modified EPA Method 26A sampling train. Samples recovered from this sampling 

train were analyzed for hydrogen chloride and chlorine using ion chromatography, according to 

EPA Method 26A. 

Quality assurance and quality control activities associated with these analyses included: 

• Sample handling and preservation; 

• Preparation and analysis of samples within specified holding times; 

• Preparation and analysis of laboratory blanks; 

• Collection and analysis of field blanks; 

• Preparation and analysis of laboratory control samples; 

• Preparation and analysis of matrix spike and matrix spike duplicate samples; and 

• Preparation and analysis of all samples in duplicate. 

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Review of these QA/QC activities indicates that these data are supportable, and useable. See the 

detailed data quality assessment in Appendix H. The following issue was identified during the 

QA/QC review: 

• Hydrogen chloride was consistently detected in the field blank samples. The levels of 

hydrogen chloride observed (approximately 60 u,g per sample) are well below the 

levels observed in the field samples (all greater than 1,800 u,g per sample). These 

levels are negligible and have no impact on the data. No data are qualified or 

invalidated based on blank results. 

5.3.4 Analysis of Stack Gas Samples for Determination of Metals 

Samples for determination of metals in stack gas were collected according to EPA 

Method 29. The filters, impinger solutions and rinses were analyzed for mercury by CVAA 

according to SW-846 Method 7470A and for arsenic, beryllium, cadmium, chromium, and lead 

by ICPES, according to SW-846 Method 6010B. 

Quality assurance and quality control activities associated with these analyses included: 

• Sample handling and preservation; 

• Preparation and analysis of samples within specified holding times; 

• Preparation and analysis of laboratory blanks; 

• Collection and analysis of field blanks; 

• Preparation and analysis of media check samples; 

• Preparation and analysis of laboratory control samples (LCS) and laboratory check 

sample duplicates (LCSD); 

• Preparation and analysis of matrix spike and matrix spike duplicate samples; and 

• Preparation and analysis of post digestion spike (PDS) and post digestion spike 

duplicate (PDSD) samples. 

Review of these QA/QC activities indicates that these data are supportable, and useable. See the 

detailed data quality assessment in Appendix H. The following issues were identified during the 

QA/QC review: 

• Arsenic was found above the detection limit in laboratory blank samples associated 

with analysis of PNR/filter samples. The blank results for arsenic in the laboratory 

blanks are near the detection limit, and similar to or below the results for the field 

samples. This may indicate a slight positive bias in the field results. Samples were not 

corrected for field blank results. No results are invalidated or qualified based on 

blank results. 

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• Cadmium and mercury were each found in one field blank sample. The single 

positive result for cadmium in one field blank is similar in magnitude to the field 

results. The single positive result for mercury in one field blank is near the detection 

limit, and well below many of the field results. These may indicate a slight positive 

bias in the field samples. Samples were not corrected for field blank results. No 

results are invalidated or qualified based on blank results. 

• Chromium was consistently observed in field blanks and media check samples. The 

consistent observation of chromium in field blank and media check samples is at a 

lower level than the field samples. This may indicate a slight positive bias in the 

results for the field samples. Samples were not corrected for field blank results. No 

results are invalidated or qualified based on blank results. 

5.3.5 Analysis of Stack Gas Samples for Determination of Dioxins/Furans 

Samples for determination of the polychlorinated dibenzodioxins and dibenzofurans 

(dioxins/furans) were collected according to the methodology described in SW-846 

Method 0023A. The filters, sorbent traps, and rinses from these samples were prepared for 

analysis according to SW-846 Method 0023A, and the resulting extracts analyzed for 

dioxins/furans by high-resolution GCMS, according to SW-846 Method 8290. 

Quality assurance and quality control activities associated with these analyses included: 

• Sample handhng and preservation; 

• Preparation and analysis of samples within specified holding times; 

• Preparation and analysis of laboratory blanks; 

• Collection and analysis of field blanks; 

• Preparation and analysis of media check samples; 

• Preparation and analysis of laboratory control samples and laboratory check sample 

duplicates; and 

• Addition of surrogate compounds to each sample. 

Review of these QA/QC activities indicates that these data are supportable, and useable. See the 

detailed data quality assessment in Appendix H. The following issue was identified during the 

QA/QC review of these data: 

• All target analytes except 2,3,7,8-TCDD were observed in a media check sample, 

laboratory blank or field blank. The levels observed in the blank samples are very 

low, typically near the detection limit. Typically these levels are below the levels 

observed in the field samples. This indicates a potential positive bias in the field 

samples, which is conservative relative to the determination of emission rate. No data 

are qualified or invalidated based on blank results. 

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VES017793 
5.3.6 Monitoring of Stack Gas for 02

, C02 , and THC 

The stack gas was monitored for oxygen (02), carbon dioxide (CO2), and total 

hydrocarbons (THC) according to EPA Methods 3A and 25A, respectively. 

Quality assurance and quality control activities associated with continuous emission 

monitoring include: 

• Use of calibration gas standards of known and acceptable quality; 

• Use of calibration gas standards in the specified ranges, 

• Performance of system bias checks, 

• Performance of calibration error tests; and 

• Performance of zero and span drift checks. 

Review of these QA/QC activities indicates that these data are supportable and usable. See the 

data quality assessment in Appendix H. Copies of certifications of calibration gas standards are 

presented in Appendix L Raw data for continuous emission monitors are presented in Appendix 

F. The following issue was identified during the QA/QC review of this data: 

• Seventy of 72 drift checks for total hydrocarbons met method specifications. The two 

outliers were both during Unit 2 Run IB. A drift of 8.0% was seen at 1800, and a drift 

of 8.3% was observed at 1909. In accordance with EPA Method 25A, the total 

hydrocarbon analyzer was immediately re-calibrated following each of the drift 

excursions. The data from the run was then recalculated using both calibration curves 

and the higher (more conservative) result reported. As the average THC was well 

below the standard, and that the conservative recalculation approach specified in the 

method was implemented, any uncertainty in these data has no impact on the 

conclusion of the report and the demonstration of compliance. No data are flagged or 

invalidated based on the calibration drift results. 

5.4- Process Data 

In accordance with the MACT requirements, all process instrumentation was calibrated. 

A Continuous Monitoring System Performance Evaluation Test Plan (CMSPETP) was prepared 

and defines the calibration procedures and acceptance criteria. The testing specified in the 

CMSPETP was performed prior to the CPT. Data from the CMSPET is presented in Appendix 

D. 

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VES017794 
5.5 Spiking 

As detailed in Sections 1.3 and 2.3 and Appendix B, during the CPT, liquids and solids 

were spiked into the incinerator feed. QA/QC activities associated with the spiking included: 

• Use of spiking materials of known and acceptable quahty; 

• Collection of data on data sheets and appropriate data acquisition systems; 

• Calibration of pumps; and 

• Documentation of preparation of spiking packets. 

Review of these QA/QC activities indicates that the spiking data are supportable and useable. 

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VES017795 
VES017798-018278.pd f