VEOLIA 

ENVIRONMENTAL SERVICES 

March 16, 2010 

Via FedEx 

Attn: Compliance Tracker, AE-17J 

Air Enforcement and Compliance Assurance Branch 

United States Environmental Protection Agency 

Region 5 

77 W. Jackson Blvd., AE-17J 

Chicago, IL 60604 

R E: Veolia ES Technical Solutions, L.L.C. 

163121AAP 

40 CFR Part 63 - Subpart EEE 

National Emission Standards for Hazardous Air Pollutants from Hazardous 

Waste Combustors 

Notification of Compliance (NOC) and Comprehensive Performance Test 

Reports 

Compliance Tracker, 

Pursuant to the requirements of 40 CFR 63.1200, subpart EEE, Veolia ES 

Technical Solutions, L.L.C, hereby submits the Notification of Compliance (NOC) 

and the Performance Test Reports for Incinerators 2, 3 and 4. The NOC 

documents compliance with the emission standards and continuous monitoring 

system requirements, and identifying operating parameters defined in 40 CFR 

63.1209 and 63.1219. Veolia is now complying with all operating requirements 

specified in this NOC. The Performance Test Reports detail compliance with 

these standards. 

I certify under penalty of law that this document and all attachments were 

prepared under my direction or supervision in accordance with a system 

designed to assure that qualified personnel properly gather and evaluate the 

Veolia ES Technical Solutions, L.L.C. 

#7 Mobile Ave, Sauget, IL 62201 

tel: 618 271 2804 - fax: 618 271 2128 

www.VeoliaES.com 
information submitted. Based on my inquiry ofthe person or persons who 

manage the system, or those persons directly responsible for gathering the 

information, the information submitted, is to the best of my knowledge and belief, 

true, accurate, and complete. I am aware that there are significant penalties for 

submitting false information, including the possibility of fine and imprisonment for 

knowing violations. 

Upon review of this submittal, should the Agency have a need for additional 

information or questions, please contact Dennis Warchol at (618) 271 -2804 or via 

e-mail at dwarchol@onyxes.com or myself at (618) 271-2804 or via e-mail at 

dharris@onyxes.com.. 

Sincerely, 

Veolia ES Technical Solutioffs, L.L.C. 

Doug Harris 

General Manager 

Att. 

cc: USEPA File 
Notification of Compliance (NOC) Report EWt 

MAR I t 207 0 

Veolia ES Technical Solutions, L.L.C. hereby submits the Notific£tion_pf 

Compliance (NOC) Report in compliance with 

40 CFR 63.1210(b) and 40 CFR 63.1207(j) 

f AIR ENFORCEMENTS 

U S . EPA. RE ' IUK S 

Applicable Rule: 40 CF R Part 63.1200, Subpart EEE — National Emission Standards for 

Hazardous Air Pollutants for Hazardous Waste Combustors, This NOC 

is being made in accordance with §63.9(h). 

SECTION I 

GENERAL INFORMATION 

A. If you have been issued a Title V permit, do not complete this form. Submit your NOC in 

accordance with your Title V permit. [§63.9(h)(3)] 

B. If you have not been issued a Title V permit, complete the remaining portions of this section 

and also complete Sections ll-IX. [§63.9(h)(2)(i)] 

C. Print or type the following information for each facility for which you are making notification of 

compliance status: 

Operating Permit Number (OPTIONAL) Facility I.D. Number (OPTIONAL) 

V-IL-1716300103-08-01 ILD098642424 

Responsible Official's Name/Title 

Doug Harris 

Street Address 

#7 Mobile Ave. 

City State ZIP Code 

Sauget 62201-1069 

Facility Name (if different from Responsible Official's Name) 

Veolia ES Technical Solutions, L.L.C. 

Facility Street Address (If different than Responsible Official's Street Address) 

Facility Local Contact Name Title Phone (OPTIONAL) 

Doug Harris General Manager 618-271-2804 

City State ZIP Code 

Sauget IL 62201-1069 

D. Indicate the relevant standard or other requirement that is the basis for this notification and 

the source's compliance date: (§63.9(b)(2)(iii)) 

Basis for this notification (relevant standard or other requirement) Compliance Date (mm/dd/yy) 

40 CFR 63.1200 October 14, 2008 

1 
SECTION II 

CERTIFICATION (Note: you may edit the text in this section as deemed appropriate) 

Based upon information and belief formed after a reasonable inquiry, I, as a responsible official of 

the above-mentioned facility, certify the information contained in this report is accurate and true to 

the best of my knowledge. The above-mentioned facility has complied with the relevant standard 

or and other applicable requirements referenced in the relevant standard. [§63.9(h)(2)(i)(G)] 

Name of Responsible Official (Print or Type) Title Date (mm/dd/yy) 

Doug Harris General Manager 03/16/2010 

Signature^ Responsible Official 

U 

SECTION III 

Describe the methods you used to determine compliance. [§63.9(h)(2)(i)(A)] 

RCR A Trial Burn Data from EPA approved testing as required by the RCR A Part B permit and using all 

approved EPA methods were used to demonstrate compliance with all applicable emission standards 

defined in 40 CF R 63.1219. In addition, Comprehensive Performance Testing approved by USEPA, Region 

5 on August 8, 2008 and conducted in August and September of 2008 and Comprehensive Performance 

Testing approved by USEPA, Region 5 on November 25, 2009 and conducted in December, 2009. See the 

attached Operating Parameters Tables and HWC MAC T Emission Standards table for Units 2/3 and Unit 4, 

that define the operating parameters established during testing that ensures compliance with the 

performance standards. • 

SECTION IV 

Describe the results of any performance tests, opacity or visible emission observations, 

continuous monitoring system (CMS) performance evaluations, and/or other monitoring 

procedures or methods that were conducted. [§63.9(h)(2)(i)(B)] 

See attached test results that were used to develop the limits defined in the Operating Parameter Tables 

referenced in Section III of this report. These results also include CM S Performance evaluations and 

monitoring methods. 

SECTION V 

Describe the methods you will use to determine continuous compliance, including a description of 

monitoring and reporting requirements and test methods. [§63.9(h)(2)(i)(C)] 

Continuous compliance is based on the operating parameter limits established from compliance testing, 

defined in the attached Operating Parameters Table referenced in Section III of this report. These 

incinerator operating parameters are monitored continuously to verify compliance by a process 

monitoring and control system. The details of these systems are defined in detail in Section 2.0, 

Incinerator Process description referenced in Section VIII of this report and attached. 
SECTION VI 

Describe the type and quantity of hazardous air pollutants (HAP) emitted by the source (or 

surrogate pollutants if specified in the relevant standard), reported in units and averaging times 

and in accordance with the test methods specified in the relevant standard. [§63.9(h)(2)(i)(D)] 

See attached test results from compliance testing that was conducted to demonstrate compliance with 

the HAP's and other pollutants defined in Subpart EEE. 

SECTION Vll 

If the relevant standard applies to both major and area sources, present an analysis 

demonstrating whether the affected source is a major source (using the emissions data 

generated for this notification. [§63.9(h)(2)(i)(E)] 

This facility is a major source due to its applicability to the NESHA P regulations, specifically Subpart EEE 

and Subpart DD. Regardless of the facility's emission concentrations, this facility is a major source by 

definition. 

SECTION VIII 

Describe the air pollution control equipment (or method) for each emission point, including each 

control device (or method) for each hazardous air pollutant and the control efficiency (percent) for 

each control device (or method). [§63.9(h)(2)(i)(F)j 

See attached Section 2.0, Incinerator Process Description from 2009 Performance Test Plans for 

Incinerators 2, 3 and 4 that describes the air pollution control equipment for each emission point. Also, 

see attached the compliance testing data defined in Section IV of this report that details the control 

efficiency for each control device. 

SECTION IX 

A. Did you submit an application for construction or reconstruction under §63.5(d) that contained 

preliminary or estimated data? [§63.9(h)(5)] 

Yes • . . . No • . . . Not applicable • . (did not submit an application for construction or 

reconstruction). 

B. If you answered yes, provide actual emission data or other corrected information below. 

END OF FORM. A Responsible Official must sign this form - See Section II. 

3 
HWC MACT Emission Standards 

Parameter 

Dioxin/Furan (D/F) 

Mercury (Hg) 

Semivolatile Metals (SVM) 

Cadmium, Lead 

Low Volatile Metals (LVM) 

Arsenic, Beryllium, Chromium 

Carbon Monoxide (CO) 

Hydrogen Chloride/Chlorine 

(HC1/C12) 

Particulate 

Units Standard ((3)7% 02) 

ng/dscm TEQ 0.20 (>400 deg F) 

0.40 (<400 deg F) 

ug/dscm 

ug/dscm 

ug/dscm 

ppmv 

ppmv 

gr/dscf 

130 

230 

92 

100 

32 

0.013 

Method of Compliance 

Operating Parameter 

Limits 

Operating Parameter 

Limits 

Operating Parameter 

Limits 

Operating Parameter 

Limits 

Continuous Emissions 

Monitor 

Operating Parameter 

Limits 

Operating Parameter 

Limits 
UNITS 2/3 OPERATING PARAMETER LIMITS

 1 

Operating Parameter Units Limits Test Date 

Performance 

Standards 

Maximum Total Pumpable Lb/hr 3107 

Waste (Hourly Rolling Total) 

Maximum Total Hazardous Lb/hr 4017 

Waste (Hourly Rolling Total) 

Maximum Stack Gas Flow Acfm 15,147 

Rate (Hourly Rolling Average) 

Minimum Primary Combustion Deg F 1686 

Chamber Temperature (Hourly 

Rolling Average) 

Minimum Secondary Combustion DegF 1877 

Chamber Temperature (Hourly 

Rolling Average) 

Maximum Baghouse Inlet Deg F 420 

Temperature (Hourly Rolling 

-Average) 

Max. Pump. Low Volatile Metals Lb/hr 46 

Feedrate (12 Hour Rolling Total) 

Max. Total Low Volatile Metals Lb/hr 47 

Feedrate (12 Hour Rolling Total) 

Maximum Semi Volatile Metals Lb/hr 63 

Feedrate (12 Hour Rolling Total) 

Maximum Mercury Feedrate Lb/hr 0.0019 

(12 Hour Rolling Total) 

Maximum Chlorine Feedrate Lb/hr 218 

(12 Hour Rolling Total) 

Maximum Ash Feedrate (12 Lb/hr 617 

Hour Rolling Total) 

Minimum Sorbent Feedrate Lb/lb Cl 2 1.57 

(Hourly Rolling Average) 

Minimum Carrier Fluid Flowrate Gal/lb Cl 2 1.46 

(Hourly Rolling Average) 

Jan, 1993 

Jan, 1993 

Jan, 1993 

Dec, 2009 

Dec, 2009 

Dec, 2009 

Sep, 2008 

Sep, 2008 

Sep, 2008 

Aug, 2008 

Aug, 2008 

Dec, 2009 

Dec, 2009 

Dec, 2009 

DRE, D/F 

DRE, D/F 

DRE, D/F, 

Part, SVM , 

L V M 

DRE, D/F 

DRE, D/F 

D/F, SVM , 

L V M 

L V M 

L V M 

S V M 

Hg 

SVM, LV M 

HC1/C12 

Part. 

HC1/G12 

HC1/C12 

l Operating parameter limits in table reflect more conservative value between Unit 2 and Unit 3 test data. 
UNIT 4 OPERATING PARAMETER LIMITS 

Operating Parameter Units Limits Test Date 

Performance 

Standards 

Maximum Total Pumpable Lb/hr 

Waste (Hourly Rolling Total) 

Maximum Total Hazardous Lb/hr 

Waste (Hourly Rolling Total) 

Maximum Stack Gas Flow Acfm 

Rate (Hourly Rolling Average) 

Minimum Primary Combustion Deg F 

Chamber Temperature (Hourly 

Rolling Average) 

Minimum Secondary Combustion Deg F 

Chamber Temperature (Hourly 

Rolling Average) 

Maximum Baghouse Inlet Deg F 

Temperature (Hourly Rolling 

Average) 

Max. Pump. Low Volatile Metals Lb/hr 

' ^eedrate (12 Hour Rolling Total) 

Max. Total Low Volatile Metals Lb/hr 

Feedrate (12 Hour Rolling Total) 

Maximum Semi Volatile Metals Lb/hr 

Feedrate (12 Hour Rolling Total) 

Maximum Mercury Feed rate Lb/hr 

(12 Hour Rolling Total) 

Maximum Chlorine Feed rate Lb/hr 

(12 Hour Rolling Total) 

Maximum Ash Feed Rate (12 Lb/hr 

Hour Rolling Total) 

Carbon Injection Feedrate Lb/hr 

(Hourly Rolling Average) 

PCC-3291 

SCC - 1176 

PCC-12,897 

SCC - 1176 

37,432 

1499 

400 

47 

50 

64 

0.026 

229 

6444 

6.2 

Dec, 2009 

Dec, 2009 

Dec, 2009 

Dec, 2009 

Dec, 2009 

Dec, 2009 

Aug,2008 

Aug,2008 

Aug,2008 

Aug , 2008 

Dec, 2009 

Dec, 2009 

Dec, 2009 

DRE, D/F 

DRE, D/F 

DRE, D/F, 

Part, SVM , 

L V M 

DRE, D/F 

DRE, D/F 

D/F, SVM , 

L V M 

L V M 

L V M 

S V M 

Hg 

SVM , LVM , 

HC1/C12 

Part. 

D/F, Hg 

Minimum Sorbent Feedrate Lb/lb Cl 2 2.25 

(Hourly Rolling Average) 

Minimum Carrier Fluid Flowrate Gal/lb Cl 2 3.10 

(Hourly Rolling Average) 

Dec, 2009 

Dec, 2009 

HC1/C12 

HC1/C12