## VES010160

. pdfU nited Sta t es Environmental Protection Agen cy Region 5 Air & Radiation Division 77 West Jackson Boulenrd C hicago , Illinoi s 60604 

## AIR POLLUTION CONTROL TITLE V PERMIT TO OPERATE

Permit No.: V-IL-1716300103

-2014

- 10 Issue Date: DRAFT Effective Date: 

### DRAFT Expiration Date: DRAFT
In accordance wi t h the provisions of Title V of the C1eanAir Act and 40 C.P.R
. Part 7 1, 

### Veolia ES T ec hnical Solutions, LL.C. is authorized to operate air emission units and to conduct other air pollutant emitting activities in accordance with the permit conditions listed in this permit. This source is authorized to operate in St. Clair County at the following address: 7 Mobile Avenue , Sauget, IUinois 6220 I Tenns and conditions not othenvise defined in this permit h ave the meaning assigned to them in 40 C.F.R
. Part 71 unless other r egulations or statutes are referenced. All terms and conditions of the permit are enforceable by E PA and citizens under the Clean Air Act. Once effective, this pennit supersedes any other permi t issued to the source pursuant to Title V of the Clean A i r Act and 40 C.F.R
. Part 71.

George Czerniak, Director Air and Radiation Division U.S. EPA- Reg ion 5 Date



### VES010160Veolia ES Technical Solutions, L.L.C. Pennit No.: V

- !L -1 7163 00103-201 4- 10 Issuance Date: DRAFT E

x

piration Date: DRAFT 

### TABLE OF CONTENTS Page 2 of 172

1.0. SOURCE IDENTlFICATION AND UNIT-SPECIFIC INFORMATlON**·~·** .. .**~** ........... 8 1. 1
. GENERAL SOURCE INFORMAT I ON
... . ... . .. . ... .. ................ .. .. ..... .. .. .. . ................... ... .... 8 

### I
.

2. FACILITY DESCRIPTION
. . ............ .. .. . ....... . ................. . .. . .. . ... . .. . ... . ..... . ... .. ..... .. ......... .. . . 

### 8 1
. 3
. EMlSSION UNITS
.. . ............... . .. . ... . ... . .. . .. .. .. . .. .. . .... .. . .. . .. . .. . .. . ........ . ...... .. .. .... . . . ... ............. 8 

### 2.0. UNIT**~PECIFIC** OPERATING REQUIREMENTS
....**~** .........**~** ........**~. ~**  ... . ..... . ..... . ..**~** .. It 2.1. HAZARDOUS WASTE COMBUSTORS, UNITS 2, 3AND4
..... .. ......... . .. . .. . .. . .. . .. .. .. II (A) Emission Limitat i ons and Standards
.... . ............ . .. . .. . .. . ............. .. ......... . ........ .. ....... . I I (B) Nonapplicable Regulations
... . ....... . ..... . ... . .. ... .......... .. . . .. .. .. ..... . . . ... . . . ..................... . .. 14 (C) Work Pract ice and Operational Requirements
. . ..... . ............................................... 15 (D) Monitoring and Testing
.. . ..... . ... . ... . .. . .. . ...... . .... . .. . .. . .... . ...... . . .. .. .. ..... .. ... . .. ..... . . .......... 31 (E) Recordkeeping and Reporting
.. . ... . ...... . .................. .. . . .. . ... .. .... .. .................. . ........ ... 73 

### 2.2
. MATERIAL PROCESSING AREAS
..... . ... . ........ .. ........ . .. . .. . .... .. .... . . ....................... . ..... 

### 90 (A) Emission Limitations and S tandards
............... . .... . ...... . .. . ...... . ... . .. . .................. . ...... 

### 90 ( B ) Nonapplicable Regulations
... . .......... . ... . ........... . ........... . ..................... . . ... ... . ... . . . ...... 

### 91 (C) Work Practice and Operational Requirements . . .. . .... . .. .. ....................... . .. . ..... . .. . ... .. 92 (0) Monitoring and Testing
.. .... .... . . ....... . ............... . ..... . .. . ..... .. ........ . . . .................... . ...... 94 (E) Recordkeeping and Reporting
................. . ....... . .. . .. . .. . .. . .. . . .......... . ........ . ..... . .. .... ... . .. 99 2
. 3
. DRUM CRUSHER
........... . ............ . ... .. ............... . .......... .. ...... . ... . ..... . . ... .. . ........ ............... 99 (A) Emission Limitations a nd Standards
. . ........ . ....... . .. . .. . ..... ... .. . .. . ... . .. . .. . .... . ............. . 100 (B) Nonapplicable Regulations
................... . .. . .. . ....... . ..... . .......... . .. . ...... . ................. ... . . 100 (C) Work Practice and Operational Requirements
... . ....... . ...... . . . .......... . .... .. . .. . . . ...... ... 100 (D) Monitoring and Testing
...................... . ... . .. . .. . .... . ................................... . .. . .. . .. .. .. . . !00 (E) Recordkeeping and Reporting..
. ............... .. . ....... . ...... . ...... . .. . .. . ......... ... ..... . ........... I0 I 2.4. LIQ UID WASTE STORAGE TANKS
. ... .... .. . . ........ ...................... . ........... . ..... . ..... . ..... 102 (A) Emission Limitations and Standards
. ... .. ..... . . . .............. . ...................... . ... . ..... .... ... 102 (B) N onapplicabl e Regulations
. . ... . .... . .... . .... . ............................ . ... . .. .... .. . ... . . ............... 104 (C) Work Practice and Operationa l Requirements
.......... . .. . ... . ..... .. ... . ..... .. .. . .............. 105



### VES010161Voolia ES Technical Solutions, L.L
. C
. Pennit No.: V

-IL-1716300 103 · 2014-10 Issuance Date: DRAFT Expirat ion Date: DRAFT Page 3 of 172

(D) Monitoring and Testing
....................................................................... .. ............... 105 (E) Recordkeeping and Reporting
........................................................... . ... ............... I 06 

### 2.5. BULK SOLID WASTE STORAGE FACILITY
...................................................... .. . 109 (A) Emission Limitations and Standards
.................................................................. .. I 09 (B) Nonapplicable Regulations
...... .. ........ .. .. ........ ..................................... . ...... .. ......... III (C) Work Practice and Operational Requirements
.... .. ............................... .. .............. 112 (D) Monitoring and Testing
................................................ .. .. .. ........ ............ .............. 112 (E) Recordkeeping and Reporting
........................... ................. .. ......... .. ....... .............. 114 2 .6. GASOLINE STORAGE TANK
.................................................................................. 117 (A) Emission Limitations and Standards
.................................................................... 117 (B) Nonapp)jcable R egula tions . .. .. ............ . ... .. ...................... .. .................. . .. ............... 118 (C) Work Practice and Operational Requirements
.. ................ . ...... . .... ...................... . 118 (D) Monitoring and Testing
....... . ... ............. .. .... . .................................. .. ......... .. .......... 

### 119 (E) Recordlceeping and Reporting
............ .. ............................................. ............... .... 

### 119 2.7. BOILER
...... . ................ . .. . ... . ..... . . .................................................................. . .. . ... . ........ 120 (A) Emission Limitations and Standards
.................... . ... . .. ... ... ................................... 120 ( B ) Nonapplicable Regulations
. .................................... . ................ .. ........................... 121 (C) Work Praclice and Operational Requiremen ts ............. .. ...................................... 122 (D) Monitoring and Testing
. .. . ...... . ..... . .... . .. . .... ... ..... .... ... ................... . ...... . .......... . ...... 123 (E) Recordkeeping and Reporting.............................................................................. 124 2.8. EMERGENCY GENERATORS
........ . ........ . ........ .. .. . ..... . ...... . ............................... .. . .... 126 (A) Emission Limitations and Sta ndards
................................ .. .......... .. ...................... 126 (B) Nonapplicable Regulations
................... ..... ...... ................. . .. . .. . ... . ....... .................. 126 (C) Work Practice and Operational Requirements
.................................. .. ................. 126 (D) Monitoring and Testing
..... .. ..... . ... ....... . .................. .. ..... . .......... . .. . ................ ........ 130 (E) Recordkeeping and Reporting
... ... ........................... ........ .. ................................... 130 2 .9. FUGITIVE E MISSIONS
................................... ... ............ ....... ..... .......... ..................... 133 (A) Emission Litnitations and Standards
.... .. ........................................... .. ................. 133 (B) Nonapplicable Regulations
.. .. . .. . .. ........ . ........ .. .. . .. . .. .. .. . .. . ................................. ..... 134



### VES010162Veol ia ES Technical Sol utions, L.L
.C. Pennil No.: Y· IL · 17 16 300 10 3 · 2014 · 10 Issuance Date: DRAFT Expi ration Date: DRAFT Page 4 of 172

(C) Work Practice and Operational Requirements
.......... .. ......... .. .............................. 134 (D) Monitoring and Testing
........................................................................................ 1 43 (E) Record.lceeping and Reporting
.............. . .......................................... . .................... 146 2.10. INSIGNIFICANT EMISSION UNITS AND ACTMTIES
..................................... 148 (A) List oflnsignificant Emission Units and Activities
................ .. . ............ .............. 148 (B) Applicable RequiremeniS
... ..... . ... ........ . ... . .............................. . ............. . ............... 149 (C) Compliance with Applicab l e RequiremeniS
.. .. ................................... ...... : ........ .. . 149 3.0. FACILITY

- WIDE PERMIT REQUIREMENTS
. .......... - ......... -···-·-·· · · -··· · ·· · ·· · ·· · ·· · ··· I SO 3.1. GENERAL PART 71 RECORDKEEPING
............................................. . ........ ........ ... l50 {A) Required Records
..... ... ....... ....... .. .. . .. . ................................................................... 150 (B) Record Retention Schedule
.... .... ........ . .. ......... .... ........ . ..................................... .. .. 150 (C) Emissions Calculation Methodology
............. ........ . ........................................... . .. 1 50 3.2. GENERALPART71 REPORTING
.. ... . ...................................................................... I 5 1 (A) Semi-annual Reports
................................................................. .... ... ..... ............... 151 (B) Deviations
.. ..... . .. . ... . ........ . ............. . .. ............. .. .. ....... ... . ...................... . . .. . .. . .. . ........ 152 3.3. PERFORMANCE TESTING
. . ................ . .......... . ................ ... ... .............. ......... . .. . ........ I 53 3.4. FACILITY

- WIDEAPPU C ABLE REQUIREMENTS
........ .... ... .... ............................ I54 (A) Fugitive Particulate Matter Restrictions
.. .............. . ........ ................................ .. .... 154 (B) Open Burning Prohibitions
......... . ............ . .. . . ... . .. . .. . ................................. . ............ 154 (C) Visib l e E missions
........ . .............. . ............ . ... . ......... .. .... . ...... . ... . ......... . ... . .. .... ......... 154 (D) Recycling and Emissions Reduction
................ ......................... ..................... .. .. .. 154 (E) Risk Managem ent Plan (RMP)
.... ..................................... .. ... . .......................... .. .. !55 (F) Episode Action Plans
.......... . ...... . ...... . .......... . ...................... .. ................... . .. . .. . ...... 155 (G) Annual Benzene Waste Quantity Determination
.......... ....................................... 155 (H) General Prohibition on Air Pollution
. ........ .......................................................... !56 ( I

) Facility-wide Testing
.......... . .. . ....... . .. .. ................................ .. ......... ..... . .... . ..... ....... 156 (J) Facility

- wide Record.lceeping
. ........................... . ...... ...... .. .. . . ........................ . ....... 160
4.0
. GENERAL PART 71 REQUIREMENTS._
.................................................. - ..... . ....... 163



### VES010163Veolia ES Technical Solutions , LL.C. Pennit No.: V

- l l

- 17 163 00 103

- 2014

- 10 Issuance Date: DRAFT Expiration Date: DRAFT PageS of 1 72



### 4.1. DEFINITIONS
.. . .... . .. . ..................................... .............. ... . .. . .................................. .. .... 163 4 .2. ANNUAL FEE PAYMENT
...... .. ... ... ..... ........... . ........... .. .................... . .. . .. .. . .. .. .. .... .. .. .. 163 4 .3
. C O
.

MPLIANCESTAT EMENT
........................................... ... .. .. ... ... .... .. ...... .... .. .. .. .. . .. 165 4.4
. COMPLIANCE CERTIFICATI ONS
............ . .. . .................. .. ............. . .. . ..... . ................ 165 4.5
. SCHEDULE OF COMPLIANCE
.. .. ................ . .................... ....................... ............... . 166 4
. 6. DUTY TO PROVIDE AND SUPPLEMENT INFORMATION
...... . ..... .. .. ........ ......... 1 66 4
.7. ENFORCEABILITY
.. ... . .. . . . ....... . ............... . ...... . .. . ....... . .......... .. .. . .. .. ..................... ... .. .. 167 4.8. SUBM1SSIONS
. . ...................... . ...... ... .. . ..... . ... . .. .. ... . .. . .. .. ...... . .......... .. ..... . .. . ... . .. . ........... 167 4.9. SEVERABILITY CLAUSE
.. . .. ... . .. . .................... . .. . ...... . .. .. .. . ... . .. .. .. . .... .. ................. . .. .. 167 4 .10. PERM I T ACTIONS
.................. ...... . ........... ...................... .. ....... .. .... .... ...................... 167 4. 1 1. ADMINISTRATIVE PERMIT AMENDMENTS
. ........ .. .. .. ..................................... . 168 4. 1 2. MIN OR PERMIT MO DIFICATfONS
.................. ..................................... .. .. .. .... .. .. .. 168 4
. 13. S IGNIFICANT PERMIT MODIFICATIONS
.......... .. ................ .... ........................... 168 4.14. REOPENING FOR CAUSE
.. .................. .... . .. ...... ..... .. .... ........................ .. ...... .. ... .. .... 168 4.IS. PROP ERTYRIGHTS
.. .. .... .. .. .... .... ........ .. .. .. .... .... ........................... ........... .... .. . .. ....... I68 4.16.1NSPECTION AND ENTRY
............ . ........................... .. .. ........ ................ .. ..... .. . .... ... 168 4.17. EMERGBNCYPROVISIONS
..... ... ............... .. .. ..... .................................. ............ ..... I69 4 .18. OFF PERMIT CHANGES
.. ........ .. ... ........................................ .. ............................... . 170 4.19
. PERMJT EXPIRATION AND RENEWAL
........ .. ..... .. .. .. ..................................... .. .. 170 4 .20. OPERATIONAL FLEXIBILITY
........ ................... ............................ .. ..... .. . .. .. .... .. .. .. 17 1 4.21. PERMIT SHIELD
........... .... .. ... .......... .... .. .. .......................... .. ....... ............. ....... . ........ 171 4.22. CREDIBLE EVIDENCE
..................................... .... ...... .. ............. .. .............. ............. 172



### VES010164Veol ia ES Teehoieal Sob uion<, LL.C. Pennit No
. : Y· ll.-171 6300 103 · 20 1 4

- 10 Issuance Date: DRAFT Expi ration Date: DRAFT A bbre vi a tion s and Acro n ym s ASTM CAAor Act CEM CEMS C.F.R. CMS 

## co COM CPMS 

## ooc ORE E

PA ESV EU Facility gal g gr

/ scf HAP br HWC lAC IEPA kg kpa lb 

### LVM MACT 11gldscm Mg American Society for Testing and Materials Clean Air Ac t [42 U.S.C. § 740 1 et seq . ] Continuous Emission Moni t or Con tinuou s Emissions Monit oring System Code of Federal Regulations Continuous Mo n itoring System Carbon Monoxide C'.ontinuous Opacity Monitor Continuous Parametric Monitoring System Documentation of Compliance Destruction and removal efficiency United States Environmental Protection Agency Emergency Safety Vent E

mission Unit Veolia ES Teclulical Solutions, LL.C. gallon grams grains per standard cubic foo t ofexhaust gas Hazardous Air Pollutant hour hazardous waste combustor Illinois Administrative Code Illinois Environmental Protection Agency kilogram kilo pascals pound Low Vo latile Metals (Arsenic , Chromium and Beryllium) Maxim um Achiev able Control Technology micrograms per dry standard c u

bic meter of exhau st gas mega gram million British Thermal Units National Emission Standards for Hazardous Air Pol l utants Page 6 o f 172

MMB t u NESHAP ngTEQidscm nanograms toxicity equivalents per dry standard cubic meter of exhaust gas NOC NOx NSPS NSR Operator Permittee PM PM1o ppm Notification of Compliance Nitrogen O"ides New So urce Perfom1ance Standard New Source Review Veolia ES Technical Solution s, L.L.C. Veolia ES Technical Solutions, L
.L.C. Particulate Matter Particulate matter less t h an 10**icrons** in diameter parts per million



### VES010165V eoli a ES T<Ohn ic a l Sol utions , LLC
. P

onn it No .: V

-IL- 1716300103-2 0 14- 10 I ssuance D-Jte : DRAFT E

xpirarion Date : DRA Fli 

### POHC PSD Psi 

### S<h 

### SVM tpy 

### vo c VHAP principle organic hazardous cons tituen t Prevemion of Signi ficant Det eriorat i on Pounds per square inch Sulfur Dioxide Semi v olatile Metals (Lead and Cadmiwn) tons per year Volatile Organic Compounds Volatile Haza rdous Air Pollu tan t Page 7 o fl 72



### VES0 10166Veolia BSTechni cal Sol utions, L. L
.C
. Perm i t No
. : V

-IL- 1 7 16300103 · 2014

- 10 Issuance Date: DRAFT Expiration Date: DRAFT Page 8 of l 72


## 1.0. SO UR C E IDENTIFICATIO N AND UNIT -SP E CIFIC I N FORMATION Lt

. GE NERAL S O URCE IN FORMATIO N P arent Company:
Facility:
County: SlCCode : AFS Plant Identification Number : 1 .2. F ACILITY DES CRIPTION Veolia ES Technical Sol utions, L. L .C. 700 E. Butterfield Road Lombard, Illinois 60 14 g Veolia ES T echnical Solutions , L. L.C. 7 Mobile Avenue Sauget , Illinois 62201 St. Cla ir 4953 I7 1 6300!03

Veolia ES Technical Solutions, L
. L.C. is a treatment, storage, and disposal facility, which accepts offsite waste for further di sposa l through incineration . Containers and bu l k shipments of hazardous and sol i d wastes are receive{!, analyzed, transferred to temporary storage facili t ies , processed, and incinerated in one of three combu stion units. 1. 3
. EMISS ION UNITS The emissions un its located at the fucility at the time of permit issuance are: 

### E mi ssion Manufacture r Date of Emission C ontro l U ni t Desc ri ption /Model Cons truction E quipm en t Incineration Unit #2 T rade Waste October 1 986 Joy-Niro Spray (Incinerator) with a I ncineration, TWI

- Dryer Absorber Maximum Heat 2000, Series 2 (SDA-2), Pulse Flo Hazardous Capaci ty of Fabric Filter (BH

- 2)

Waste 1 6mmBtulh r Combustors



### VESO!Ol67Veolia ES Tecltuical So l utions, L.L.C
. Pennit No.: V

-JL- 17 16300 103-2014-10 I ssuance Date: DRAFT E

x

piration Da t e: DRAFT Emission Unit Description Incineration Unit # 3 (Incinerator) with a Maximum He-at Capacity of 1 6 mmBtulhr Incineration Unit 114 (Rotary Kiln) with a Maximum Heat Capacity of 50mmBtnlhr Waste Processing Matetial Units (Area I and Processing Area 2) Areas Lab Pack Repack Unit Drum Empty dmms are Crusher cru s hed Tanks #2 (4,391 gals), 114 (4,93! gals), 

### #6 (7 ,200 gals), #8 (5,820 gals}, #10 ( 1

2 , 869 gals) , #20 ( 1

2 , 869 gals) , #3 0 ( 1

2,869 gals) , 

### #40 ( 1

2 , 869 gals) , #50 Storage (12,869 gals) , #60 Tanks for (1 2 ,869 gals) , #300 Liquid ( 1 9 , 850 gals) , #3 02 (30,000 gals) , #3 04 Wastes (30 ,000 gals) , # 306 (30,000 gals) , # 308 (30,000 gals) , #310 (30,000 gals) , #3 12 (10,000 gals) and #31411 0,000 2als) Storage tank for 11 2 fuel oil: Tank #390 (30.000 e:als) Bulk Solid Temporary storage of

Waste bulk solid wastes i n p

i ts prior to being fed Ma nufacturer /Model Trade Waste Incineration, TWI2000, Series 2
International Waste Energy, PY*ROX

Modem Welding

Modem Weldi ng Page 9 of 1 72

D ate o f E mi ssion Co ntrol Con s tru ction Eq uln ment November 1987 Joy

-Niro Spray Dryer Absorber (SDA-3) , Pulse Flo Fabric Filter (BH-3) Ju

ne 1988 Tempering Chamber, Activated

Carbon Injection, Spray Dryer Absorber, Fabric Filt er 1988 None 1988 1984 None Apri l 2002 for Acth•ated Carbon #2 and #4; June Absorption Systems

2004 for#lO on each storage tank and #20; March vent.

2009 for #3 0;

1988 for the

others.

1988 None
198 8 Cyclone , Airtol Bagbonse (BF BldgBH- 

## n, Carbon



### VESO!Ol68Veolia ES Techni cal Solu t ions,L..I...C
. Pennit No.: V

- JL

- 1716300103

- 2014

- 10 Issuance Date: DRAFT Expirat ion Date: DRAFT E mission Unit D escripti on Storage to Incineration Unit FacilitY #4 Gasoline 550 gallon tank, Storage Tank equipped with submerged loading pipe Boiler Natural Gas

- Fired Boiler with a Maximum Heat Capacity of I 0
. 6 mmBtulhr (Boiler #I) Emergency 

### l\vo #2 Fuel oil

- tired Generators Eme
. rgency (2) Generators each with Maximum Heat Capacity of 0
.40 mmBtu/hr {<112 kilowatts (kW)) Fugitive Pumps , Valves, Emissions Open-End Lines and Comoressors Page ! Oofl72

Manufacturer Dat e of E mis sion Control /Model Construction E auiDm en t Adsorption Unit (BF Bldg-CA) June 2012 None

Cleaver Brooks, November 1995 None 250



### 1988 None

NI A None



### V ESO!Oi69Veolia ES Technica l Sol utions, l..L.C. Penni ! No.: V

- JL

- 1 7 1

6300 103

- 2

0 14· 10 I ssuance Da l e: DRAFT EKpiral ion Dale: DRAFT 

## 2.0. UNI T-SPECIFIC OP ERATING REQUIREMEN TS 2.1. HAZARDO US WASTE CO MBUST ORS, UNITS 2 , 3 AND 4 (A) E m issi on Limitatio n s a nd S tandards [40 C.F. R. § 7 1 .6(a)(l) ) Page II ofl72

The Pennittee shall comply with the following requirements at each individual incinerator unless specified otherwise: L Visible Emission Limitations. (a) The Permittee shall not cause or allow from any emission source the emission into the atmosphere of smoke or o ther particula te matter with an opacity greater than 30 percent, excep t as allowed by 35 lAC 212. I23(b) and212.124. [ 35 IAC212.123(a)J (b) The Perm ittee shall not cause or allow from any process , including any material handling or storage act ivity, the emission of fugitive particulate matter that is visible by an observer looking generally overhead at a point beyond tlte property line ofthe source unless tlte wind s p eed is greater than 40.2 ki l ometers per hour (25 miles per h our)
. (35 lAC 212.301 and 212
. 314) 2. Sulfur Dioxide Limitations. T otal sulfur dioxide em i ssions from the fac il ity shall not exceed 7
.7 tons per year (tpy) from Un it 2, 7
.7 tpy from Unit 3 , and 50.76 tpy from Unit 4. [Construction P

ermits 87 1 00024 and 8801000 1) 3. Carbon Monoxide Limitations. (a) The Permittee shall not allow emissions of carbon monoxide in e x

cess o f I 00 parts per million (ppm) by vol u me, on an hourly rolling average (monitored continuously with a continuous emissions monitoring system), dry basis and coiTected to 7 percent o x ygen . The Pennittee must also document tltat, during the destruction and removal effici e ncy test runs or tlteir equiv alent as provided by 40 C
. F
.R
. § 63
. 1206(b)(7), hydrocar b

ons do not exceed I0 ppm by volume during those runs, on an hourly rolling average (monitored co n tinuous ly with a continuous emissions monitoring syst em), dry basis , corrected to 7 percent oxygen, and reported as propane . [ 40 C
. P.R.§ 63.1219(aX5)] (b) The Permittee shall not allow emissions of carbon monoxide from any i nc inerator in excess of 500 ppm corrected t o 50 percent excess air. (35 lAC 216.141, Con struction Pem1 its 83120053, 87 1 00024 and 880 I 000 I }



### VESOl 0 l70Veolia EST echni cal Solutio ns, L
. L.C. Permir No.: V

- IL

- 17 1 6300 103 -20 14

- 10 Issuance Date: DRAFT Expira tion Dare: DRAFT Page 12 o f 172

(c) The Permittee shall not allow em i ssions of carbon monoxide in ex cess of 6.6 tpy from Unit 2 , 6.6 tpy from Unit 3 and 13.86 tpy from Unit 4
. [Construction Permits 87100024 and 880 1 0001) 4
. Particulate Matter L imitations. (a) The Permittee shall not cause or allow the emission o f partic ulate matter into the atmosphere from any inc inerator burning more than 0.907 m

ega gram pe r hour (Mglhr ; 2 , 000 pounds per hour (lblhr)) but less than 27.2 Mg lh

r (60,000 lblhr ) of refuse to exceed 183 milligrams per standard cubic meter (mg/scm ; 0.08 grain per standard cubic foot (gr / scf)) of effluent gasescorrected to 12 percent carbon dioxide. [35 lAC 212.18l(b), Construct i on Permit 83 120053 ] (b) TI1 e P ermittee shall not allow emi ssion s ofparticulate matter from the facili t y i n excess of 0
.013 gr l dscf, corrected t o 7 percent oxyg en . ( 4 0 C.F.R
. 

### § 63.12 19(a)(7)) (c) The Permittee shall not allow emissions of total suspended particulate matter from the facility in excess of 15
.0 tpy f rom Unit 2 , 15
.0 tpy from Unit 3 , and 16.92 tpy from Unit 4. [Cons truction P ermits 87100024 and 88010001) 5. Volatile Organic Compow1ds Limitations. (a) The Permit t ee shall not cause or allow the discharge of more than 3.6 kg/hr (8 lbs/hr) of organic material into t h

e atmosphere from any emission Wlit, except that , ifno odor nuisance exists , t lus limitation sha ll apply only to photochemically reactive material . Altematively, the Permi t tee may use a control device to reduce such emissions either t o I0 ppm equivalent methane (molecular weight 16) or less, or to convert 85 percent of the hydrocarbons to carbon dioxide and water. [ 351AC 219.301. 219.302) (b) Organic mater ial emissions from the facility s h all not exceed 0.9 tpy from Unit 2 , 0.9 tpy fro m Unit3 , and 3
. 1 tpy from Un it 4. [ Const ruc tion Permits 87 1 00024 and 88010001 ] 6. Nitrogen Oxide Limitat ions . Nitrogen oxide emission s from the facility shall not exceed 4 .0 tpy fro m Uni t 2, 4
.0 tpy from Un it 3, and 61.6 tpy from Unit 4. [ Construction Permits 8710002 4 and 88010001 ) 7
. Hazardous Air Pollutant Limitations.



### VES0101 71Veol ia ES Teclmica l Solu t io n s, LL.C. Pennit No
. : V-ll.ri716J00103

- 2014

- JO Issuance D :uc : DRAFr Expi rotion Da t e: DRAFr Page 1 3of l72

(a) The Permittee shall not allow emissions ofdioxins and furans from the fac il ity in excess of 0
. 20 nanograms toxicity equivalents per dry standard cubic meter (og TEQ/dscm), corrected to 7 percent oxygen. [ 40 C.F .R. § 63.1219(a)( l) ] (b) The Pennittee shall not allow emissions of mercury from the facility in excess of 130 mi crogram s per dry standard cubic meter**~tg dscm)** **,** corrected to 7 percent oxygen. [40 C.P.R.§ 63.1219(a)(2)] (c) The Pennittee shall not allow combined emissions of cadmium and lead from the facility in excess of230 )lg/dscm, corrected to 7 percent oxygen . [ 40 C.P.R. 

### § 63
. 1219(a)(3)] (d) The Permittee shall not allow combined emissions of arsenic , beryllium, and chromium from the facility io excess of92 )lgf dscm, corrected to 7 percent oxygen. [ 40 C.F.R. § 63.1219(a)(4) ] (e) The Permittee shall des ign, i nstall, operat e, and maintain a treatment proces s that destroy s benzen e in the waste stream by inc i nerating the waste in a combustion unit that achieves a destruction efficiency of 99 percen t or greater for benzene. [40 C.P.R
. 

### § 6I.348(a)(I )(iii)] (f) All joints or seams between the pipe sections of any transfer system that consists of cont i nuous bard

- piping shall be permanently or semipermanently sealed {e.g
. , a welded joint berweeo two sections of metal pipe or a bolted and gasketed flange). [ 40 C.F
. R. 

### § 63
. 689(c)(2)] 8. Hydrogen Chloride L imitations. (a) The Pennittee shall not allow combined emissions of hydrogen chloride and chlorine gas (tota l chlorine) from the facility in excess of32 ppm by volume
. • expressed as a chloride 

# ccn equivalent, dry basis and corrected to 7 percent oxygen. [40 C.F.R. § 63.1219(a)(6)] (b) T he Permittee shall not allow hydrogen chloride

-emissions in excess of4.0 pon nds per honr (lbslhr) from either Unit 2 or Unit 3 or the control devices shall demonstrate a mi nimum h ydrogen chloride removal efficiency of99 percent. [Construction Permits 83120053 and 87100024] 9. Destruction and Removal Efficiency (DRE) Standard. (a

) Units 2, 3 an d 4 must each achieve a ORE of99.99 percent for each principle organic hazardous co. nstituent (POHC) specified under condition 2.1 (A)(9)( c)(ii) , below. The Permittee shall calculat e dte DRE for each POHC using the following equation:



### VES010172Veolia ES Techn ical Solutions , L. L .C
. Pennit No.: V

- IIA716300103

- 2014

- 10 Issuance Date: DRAFT Page 14 of l72 Expirntion Date: DRAFT**ORE (I-{Wwr/WiN)]**  x 100"/o Where:
WIN ; mass feedrate ofone POHC in 

### a waste feedstream; and WOUT = mass emission rate ofthe same POHC presen t in exhaust enUssions prior to release to the atmosphere. The Permittee must perfonn intermediate calculations using at least three significant figures, but 

### may round the resultant emission levels to two significant figures to document compliance. (40 C.F.R. § 63.1219(c)(l) and (d)] (b) For dioxin-listed hazardous wastes F020 , F021, F022 , F023 , F026 , or F027 

### (see 40 C.F.R. § 261.31 ), Units 2, 3 and 4 must each achieve a ORE of 99.9999 percent for each POHC specified under condition 2. 1 (A)(9)( c)(ii), below. The Permittee must demonstrate this ORE performance on POHCs that are more difficult to incinerate than tetra-, penta
- , and bexachlorodibenzo-p-dioxins and dibenzofurans. The PernUttee must use the equation in condition 2.1(A)(9)(a), above, to calculate ORE for each POHC. In addition, the PernUttee must notify the Administrator of its intent to inci nerate hazardous wastes F020, F02J, F022, F023 , F026, or F027. (40 C.F.R. 

### § 63.12 1 9(c)(2) ] (c) Principal organic hazardous constituents (40 C.F .R. § 63. 1 219 (c)( 3)] (i) The Permittee mnst treat the POHCs in the waste feed that t h e Permittee specifies under condition 2.l(A)(9)(c)(ii), below , to the exte n t required by 40 C.F.R. § 63
. 1219(c)(l) and (c)(2). (ii) The Permittee mus t specify one or more POHCs that are representative of the most difficult to destroy organic compounds in the hazardous wasie feedstream. The Petmi ttee must base this specification on the degree of difficulty of incineration of the organic constituents in the waste and on their concentratio n or mass in the was t e feed, considering the results of waste analyses or other data and information. (B) Nonapplic ab le Regul ati ons (4 0 C.F.R. 

### § 7 1. 6(1)( 1 ) 1 I. Units 2 , 3 and 4 are not subject to 40 C.F
. R. Part 64, Compliance Assurance Monitoring (CAM) for Major Stat ion ary Sources , because:



### VES010173Vcolia ES Te<:hnical Solution•, LL.C. Pennit No.: V

-IL-17 163 00103-2014-10 Issuance Date: DRAFT Expirot i on Date: DRAFT Page 15 of 172
(a) The affected units are required to comply with a NESHAP proposed after November 15, 1990. Emission limitations or standards proposed by the Administrator after November 15, 1990 pursuant to section I 1 I or 112 of the Act are exempt from CAM. (40 C.f.R. § 64.2(b}(l)(i)] 2. Units 2, 3 and 4 are not subject to 35 lAC Patt 229 ofthe Illinois State Implementation Plan (SIP), "Hospital Medical Infectious Waste Incinerators," because the Permittee is prohibited from accepting or processing hospital medic-.11 infectious waste at the facility. [35 lAC 229.1 1 

## OJ (q Wor k Pr actice and Oper ation al R e quir e m e n ts (40 C.F.R. 

### § 71-6(a)(l)] I. The Permittee s hall not bum hospital medical infectious waste , municipal waste, or waste that is subject to the Beryllium NESHAP
. [ 42 U.S.C. § 7661c(a)] 2. The Pennittee must operate Units 2, 3 and 4 in compliance with the following operating pa rameter limits (OPLs). The Permittee must also comply with the OPLs contained in the Notification ofCompliance (NOC) required pursuant to condition 2.1 (E)(2), below. If any OPL contained in this condition 2.1 (C)(2) differ from the corresponding OPL contained in the Penuittee's most recent NOC, the Permittee may submit an application requesting a revision to th e OPLs in this pemtit, pursuant to 40 C.f.R. § 71. 7( e)(l ). Nothing in this pennit obli gates the Administrator to approve an application to**re\~Se** OPLs in this permit.

" 

### O.PL Op erating P ara!lleter Aver aging U nit #2 Unit #3 Unlt#4 Period Minimum primary 1,709 °F 1,709 Of 1,561 Of hourly mlling combustion chamber average temperature (40 C
.f .R. § 63.1209(i)(l), (k)(2)) Minimum secondary 1,885 Of (,850 Of ( , 881 Of hourly rolling combustion chamber average t emperature (40 C.F. R
. § 63.1209(])(1), (k)(2)) Maximum flue gas 15,310 ac £1m in 15,310 acf/min 37,393 ac£1min hourly rolling flowrate or production average rat e (40 C.F.R. § 63.1209GX2)}, (kX3), (m)(2), (n)(S),**(~)(2))** Maximum hazardous 3,107lbslhr 3, I 07 lbslbr 3 , 312 lbs/hr for hourly rolling waste pumpable PCC and 1,203 average feedrate rate for each lbs/hr for 

## sec

VES010174V eol ia ES Tcdwi cal So l ur:ions. LL. C. Penn i t No.: V

-IL

- 17 16300103

- 20 1 4-10 Issuance Date: DRAFT J;xpiration Date: DRAFT


### O

peratlog Parameter U nit #2 combustion chamber (40 C
. P.R. § 63.1209( j )(3) , (k)(4)) Maximwu hazardous 4,017 lbslhr was t e total feedrat e rate for each combustion chamber (40 C.P.R. § 63
. 1209(i)(3), (k)(4)) Operation o f was te Minimum fuing system for each waste location where waste is atomization fed to tl1e incinerator press ure for (40C.F.R. low BTIJ § 63.1209U)(4ll waste
- 15 psi Maximum te mperature 420°F of the gas at t he inlet t o a dry particulate matter control device (i.e. , baghouse i nlet) (40 C.F.R. § 63.1209(kXI)) , (n)(l)) Minimum carbon NI A in

j ection mt e (40 C.P.R. § 63.1209(k)(6)(i)) Minim um carrier fluid N /A (gas or liquid) flowrate or pressure drop for activated carbon in

j ection system (40C.P.R. 

### § 63.1209(k) (6)(ii)) The brand (i.e., NI A manufacturer) and type of carbon used during t he comprebensi ve performance tes t (40 C.P.R. § 63.1209(k)( 6)(i ii)) Page 1 6 o f 172

()PL Averaging Unit #3 U nlt#4 Pe riod

4,01 7 lbslhr l0,6321bslhr hourly rolling forPCCand average I ,203 lbs/hr for 

## sec Minimum Minimum Instantaneous waste waste atomiz ation atomization pressure for pressure for low BTU lowBTIJ waste
- 15 psi waste
- 15 psi 42o•p 399°F hourly rolling average

NI A 6.21bslhr hourly rolling average
N/A 3.10 ga Vl b Cb hourly rolling average

N

/ A NOR IT Amer icas Jnc. DARCO® FGL



### VES010175Veolia ES Technica l Solutions, LL
.C
. Perm i t No.: V

- II. A7 1 6300 103 · 2014 · 10 lsst•1nce Date: DRAFT Expirat ion Date: DRAFT Op e ratin g Paral!l e t e

r Un it # 2 Ma.Wtium total 0.0021 lbs/hr feedrate of mercury ( 40 C.F.R. § 63.1209(1)( l)(i)) Maxim u m ash feedrate 503 lbslhr (40 C.F.R. § 63. 1 209(ni)(3)) Maximum tolal 62 lbslhr feedrate ofsemivolat i le metals (40 C.F.R. § 63. 1 209(n)(2)(ii)) Maximum total 46lbslhr feedrate of low volatile metals (40 C.F.R. § 63. 1 209(n)(2)(ii)) Feedrate limits for low 46lbs/hr volatile metals in pum pable feedstreams (40C.F.R. §

_

63. 1 209(n)(2)(vii)) Feedrate of total 204 lbslhr chlorine and chloride in all feedstreams (40 C.F.R. § 63. 1 209(n)(4) , (o)(l)) Minimum sorbent 2.24 lbllb Ch feedrate (40 C.F.R
. § 63. 1 209(o)(4)(i)) Minimum carrier fluid 1.90 gaVlb Clz flowrate or nozzle pressure drop for the spray dry adsorber (40 C
. F.R. § 63
. 1209(o)(4)(ii)) The brand ( i

. e., Mississippi manufacturer) and 

### type Lime of sorbent used during Company the comprehensive Hydrated Lime perfom1ance t est CodeMR200 (40 C.F.R. 

### § 63.1209 

# i o

)(

4l(iu)(All Page 17 of 172

O PL Averaetn g Unit #3 Per lo!l
. Unit #4 " 0
.002 1 lbslhr 0.040 lbslhr 12-hour rolling average 5031bslhr 4, 777 lbslhr 1 2-bour rolling averal!e 62 lbs/hr 62lbslhr 1 2-bour rolling average 46lbslhr 46 lbslhr 12-hour rolling average 46lbslhr 46lbslhr 12-hour rolling average
2041bs/hr 203 lbs/hr 12-hour rolling average
2.24 lb/lb Cb 2.13lb/lb Ch hourly rolling average 1.90 galllb Ch 3.10 gaVIb Ch hourly rolling average

M

i ssissippi Mississippi Lime Lime Company Company Hydrated Lime Hydrated Lime CodeMR200 CodeMR200



### VES010176Veolia ES Techni<.al Sol utions, LL.
.C
. Pemtit No.: V

-IL

- 17 1 63 00103 · 2014 · 10 Issuance Dat<: DRAFT Page 18 o f 172 Expiration Date : DRAFT OPL Averagln e Op erating P ara meter Peri.od Unit #2 Volt #3 U nl t#4 Maximwn combustion ..0.0 I inch IUO ..0.0 I inch H20 ..0.0 I i nch IUO 

### 5 seconds for chamber pressure Units 2 and 3 (40 C.F.R- § and 63
. 1 209{p)) instantaneous forUnit4 3. Compliance with standards. [40 C.F.R. 

### § 63.1206(bX I)) The**emi~sion** standards and operating requirements derived from 40 C.P.R. Part 63 , Subpart EEE, apply at all times except .: (a) During periods of slartllp , shutdown, and malfunction; and (b) When hazardous waste is not in the eombustion chamber (i.e., the hazardous waste feed to the combustor has been cut off for a period of time not less than the hazardous waste residence time) and the Permittee has documented in the operat ing record compliance with all otherwise

applicable requirements and s tandards promulgated under authority of sections 112 (e.g., 40 C. P. R. Part 63 , S ubparts LLL, DDDDD, and NNNNN ) or 1 29 of the Clean Air Act in lieu of the emission standards under 40 C.F.R. §§ 63.1203,63
. 1204, 63.1205, 63.1215, 63 .1 216, 63.1217 , 63
. 12 18 , 63.1219,63
. 1220, and 63.1221 ; the monitoring and co mpliance standards of40 C.F.R. §§ 63.1206 through 63.1209, except the modes of operation requirements of§ 63.1209{q); and the notification, reporting, and reeordkeeping requirements of§§ 63.1210 through 63.1212
. 4
. Changes in design, operat ion , or maintenance. (40 C.F.R
. 

### § 63
. 1206(b) (5)) (a) Ifthe Pennittee plans to chang e (as def m

ed in 40 C.F.R. § 63.1206(b)(5)(iii)) the design, operation, or maintenance practices of the source in a manne r that may adversely affect co mpHance with any emission standard d1at is not monitored with a CEMS, the Perm ittee must not bum hazardous wast e for more than a total of 720 hours (renewable at the discretion of the Admini strator) and only fo r the purposes of pretesting or comprehensive performance testing. Pretesting is defined at 40 C .F.R. § 63.1207(h ) (2)(i ) and (ii)
. (40 C.F.R. § 63.1206(bX5)(i)(C)(l)] (i) The Permittee may pet ition the Administrator to obtain written approval to burn hazardous waste in the interim prior to submitting a Notification o f Compliance for purposes other than testing or pretesting. The Permittee must specify operat ing requirements,



### VES010177Veolia ES Technical Solutions, LL.C
. Permit No.: V-IL

- 17 1 6300 1 03-20 1 4-10 Issuance Da t e: DRAFT Page 19of l 72 Expirat ion Dote: DRAFT including limits on operating parameters t hat the Pennirtee det ermines will ensure compliance w it h the emission standards of 40 C.F
.R. Part 63, Subpart EEE , based on available information. The Administrator will review, modify as necessary, and approve if warranted t he interim operating requirements. [ 40 C.F.R. § 63.1206{b){5)(i)(C)(2) ) (ii) Nothing in this penn it exempts any changes made u nder this provis i on from any applicable requirements under Title l ofthe CAA. [40 C.F.R. § 71.6(a)(l)) (b) Notification_ [40 C.F. R. § 63.1206(b)(5) ] The Pennirtee must comply with the notificatio n requirements ofconditio n 2.J(E)(9), below. 5
. General Operating Requirements. [ 40 C.P.R.§ 63.1206(c)(l)) (a) The Permittee must operate u nder t he operating requirements specified in the Documentation of Compliance (DOC) u n der40 C.F.R. § 63.121l(c) or the NOC under40 C.P.R.§§ 63.120 7(j) and 63.1210(d), except: (i) Durin g performance tests under approved test plans according to 40 C.F. R
. § 63.1207(e), (f) , and (g); (ii) Under the provisions ofcondition 2.1(C)(3)(a) or (b), above; and (iii) As provided by condition 2.1(C)(2), above. (b) Documentation ofCompliance. (40 C.F.R. § 63.121J(c)) The Permittee's operating record must include a DOC. T he DOC must identify the applicable emission standards under 40 C.F.R. Part 63, Subpart EEE, and the limits on the operating parameters u n der 40 C.P.R. § 63.1209 that will ensure compliance with those em i ssio n standards. (c) Failure to comply with the operating requirements is failure to ensure compliance widt the emission standards of 40 C.F
. R. Part 63, Subpart EEE. 6. Startup, Shutdown , and Malfunction Plan. (40 C.F.R. §§ 63.6(e)(3), 63.1206(c)(2)) (a) The Pennittee is subject to t h e startup, sh u tdown , and malfunction plan requirements of40 C.F.R. § 63.6(e)(3). (4 0 C.F.R. § 63. 1 206(c)(2Xi))



### VES010178Veolia ES TeclUlic.al S o lutions, J..L.C. Penni t No.: V

- fL- 17 1 6300 103

- 201 4

- 10 Issuance Date: DRAFT Page 20 of 172 Expirati on Dat e : DRAFT (i) TI1e Permittee must develop a written startup, shutdown, and malfunction p lan that describes, i n detail , procedures for operating and maintaining the source during periods of startup, shutdown, and malfunction; and a program of corrective action for malfunctioni ng process, air pollution cont rol , and monitoring equipment used to comply with the relevant standard. The startup , shutdown, and ma lftmction plan does not need to address any scenario that would not cause the source to exceed an applicable emission limitation in the relevant standard. The purpose ofthe startup , shutdown, and malfunction plan is to:

A. Ens u re that, at all t imes, the Permittee operates and maintains each affected source, including associated air pollution control and monitoring equip ment, in a manner which satisfies t h

e general duty to minimize e miss i ons establi shed by 40 C.F.R. § 63.6(e) (l )(i); 

### B. Ensure that the Permittee is prepared to correct malfimctions 

### as soon as practica b

le after their occurrence in order to minimize excess emissions of hazardous air pollutants; and C. Reduce the reportin g burden associated with periods 

### of startup, shutdown, and malfunctio n (including corrective action taken to restore malfunct ioning process and air pollution control equi pment to its normal or usual manner of operation). 

### [ 40 C.P.R.§ 63.6(e)(3)(i) ] (ii) TI1e Permittee must maintain at the affect ed source a current startup, shutdown, and malfunction plan and must make th e plan available upon request for inspection and copying by the Administrat or. In addition, if the startup, shutdown, and malfunction plan is subsequently revised as provided in 40 C.P.R.§ 63.6(e)(3)(viii), the Permittee must maintain at t h e affecte d somce eac h previous (i.e., superseded) version of the startup, shutdown, and malfunction plan, and mus t make each previous version avai !able for in s pection and copying by the Administrator for a period of 5 years after revision of the plan. Ifat any time after adoption ofa statt u p, shutdown , and malfunction plan au affected source**cea~es** oper•tion or is otherwise no longer subject to the provisions of this part, the Permittee must retain a copy of the most recent plan for 5 years from the date the source ceases operation or is no longer subject to 40 C
. F.R. Part 63, and must make the plan avai lable upon request fo r inspection and

. copying by the Administrator. Upon receipt of a writte n requesi

from t he Admini s tl"d tOr that the Permittee submit a copy of a n y



### VES010179Veolia ES Teclmicol Solutions , L.L.C
. Pennit No.: V

- JL.l7 1 6300103 · 2014 · 10 Issuance Date: DRAFT Page2 1 ofl72 Expirat i on Date: DRAFT startup, shutdown and malfunction plan (or pnrtion thereot) whi ch the Permittee maintains at the affected source or which is in the possession of the Permittee, the Permittee must promptly sub m it a copy ofthe requested plan (or a pnrtion thereof) to the Administrator
. The Permittee may elect to s ubmit the required copy of any startup , shutdown, and malfunction plan to the Administra tor in an electronic format. The Permittee may claim that any portion of such a startup, shutdown, and malfunctio n plan is confidential business information (CBI) entitled to protection fro m disclosure under section 1 14(c) ofthe Act or40 C. P .R.§ 2.301. If the Permittee makes a CBJ claim, it must c l early designate in the submission t h

e material which it claims as confident ial. [ 40 C.F.R. 

### § 63.6(e)(3)(v) ] (iii ) To satisfy the req uirements of40 C.F.R
. § 63.6 to dev e lop a startup, shutdown, and malfunction plan, the Permittee may use the affected source' s stan dard operating procedures (SOP) manual , an Occ u pational Safety and Health Administration (OSHA), or other p la n, provided the al ternative plans meet all the requirements of40 C.P. R. § 63
. 6 and the Permittee makes the alternati ve plans available for inspection when requested by the Administrator
. [ 40 C.F.R
. § 63.6(e)( 3 )(vi)] (iv) The Permittee must revise th e start u

p, shutdown and malfun ction plan ifrequired by the Administrator to do so based on the results of a determination made under40 C.F.R. § 63.6(e)(I)(i), or ifthe Administrator finds that the plan:

A. Does not address a startup, shutdown, or malfu n ction even t that has occurred; B. Fails to p rovide for the operat ion ofthe source (including associated air pollution control an d monitoring equipment) during a startu p , shutdown, or malfunction event in a marmer consist ent with the general d ut.y to minimize em i s s ions establ i shed by 40 C
. F
. R. § 63.6(e)( I)(i); C. Does n ot provi d e adequate procedures for correcting malfunction ing process and/or air pnUution con trol and monitoring equipment as q u ick l y as practicable; or D
. Includes an event.that does not meet the defin i tion of startup, shutdown, or malfunction listed in 40 C.P.R. § 63
. 2. ( 40 C.P.R. § 63.6(eX3)(vjj))



### VESOl0180Veolia ES Tocbnical Solutions, L.L
.C. Pem tit No.: V· lL · I7 1 6300 103 · 2014 · 10 Issuance Date: DRAFT Page 22 of 172 Expiration Date: DRAFT (v) The Pennittee may periodical.ly revise the startup, sh utdown, and malfunction plan for the affected source as neeessary to satisfy the requirements of40 C.F
. R. Part 63 or to reflect changes in equipment or procedures at the affected source. The Permittee may make such revisions to the startup, shutdown, and malfunction plan without prior approval by the Administrator or the pennitting authority. However, !he Permittee must report each revisio
. n to the startup ,**shutdov.~t.** and malfunction plan in the semiannual report required by 40 C.F.R. § 63.10(d)(5). If the startup, shutdown, and malfunction plan fails to address or inadequately addresses a n event that meets the characteristics of a malfunction but was not included in the startup, shutdown, and malfunction plan at the time the Permittee developed the plan, the Pennittee must revise the startup, shu tdown, and malfunction plan within 45 days after the event to include detailed procedures for operating and maintaining the source during similar ma lfunction e vents, and a program of corrective action for similar malfunctions of process or air pollution control and monitoring equipment In the event that the Permittee makes any revision to the startup, s hutdown, and malfunction plan which a lters the scope ofthe activities at the source which are deemed to be a startup, shutdown, or malfunction, or otherwise modifies the applicability of any emission limit, work practice requirement, or other requirement in a standard established under 40 C.P.R. Part 63, the revised plan shall not take effect until after the Permittee has provided a wrinen notice describing the revision to the Administrator. (40 C.P.R
. § 63.6(eX3)(viii) ] (vi) Any revisions made to the startup , shutdown, and malfunction plan in accordance with the procedures estab lished by 40 C.F.R. Part 63 shall not be deemed to constitute revisions to this permit , and tlte elements of the Sl<lrtup, shutdown, and malfunction plan s hall not be considered an applicable requirement as defined in 40 C.P.R. §§ 70.2 and 71.2. [40 C.F
. R. § 63.6(e)(3Xix)] (v ii) The procedures specified in the startup , shutdown, and malfunction plan do not fall within the permit shield provided in condition 4.21 ofthis permit. (40 C.F.R. § 63
. 6(e)(3Xix)] (h) The Perm ittee is subject to the following provisions of 40 C.F.R. 

### § 63.1206(c)(2) and (3): (i) The Pennittee must identify in the startup, shutdown, and malfunction plan a projected oxygen correction factor, based on



### VES010181Veolia ES Teclu> i c•l Solutions , LL.C.. Penni t No.: V-IL-17 16300 103-2014-10 Issuance Date: DRAFT Page 23 o f 172 Expiration Date: DRAFT normal operations, to use during pe1iods of startup and shutdown. (40 C.F.R. § 63.1206(c)(2)(iii)] (ii) The Permittee must record the startup, shutdown, and malfunction p lan in the operating record. ( 40 C.P.R.§ 63.1206(c)(2)(iv) J (iii) Operating under the s tartup, shutdown , and malfunction p lan: [40 C .F. R
. § 63 .1 206(c)(2)(v)(A} ] A. Compliance with automatic waste feed cutoff(A\VFCO) requirements during malfunctions:

I. During malfunctions, the A WFCO re quirements of condition 2
. 1 (C)(7) of this f><.'rmit continue to apply , exce p t for condition 2.I(C)(7)(e). lfthere is an exceedance of a 40 C.P.R. Part 63, Su bpart EEE, emission s tandard monitored by a CEMS or COMS or operating limit specified under 40 C.F
.R. § 63.1209 , the automatic waste feed cutoff system must immediately and automatically cutoff the hazardous waste feed, except as provided by condition 2.l(C)(7)(f) of this pem1it. I f the malfunction itself prevents immediate and automatic cutoff of the hazardous waste feed, the Pennittee must cease feeding hazardous wasie as quickly as possible. II
. Although ibe automatic waste feed cutoff requirements continue to apply during a malfunction, an exceedance ofan emission standar d monitored by a CEMS or COMS or operating limit specified u nder 40 C.F.R. 

### § 63.1209 i s not a violation of 40 C.F

. R. Pmt 63 , Subpart EEE, if the source contutues to operate i n accordance w i th 40 C.F
.R. 

### § 63 .6(e)(I)J
. [ 40 C.F.R
. 

### § 63.1206{c)(2)(v)(A)(2)] 

### JJI. Excessive number of exceedances d uring malfunctions. For each s et of I0 exceedances of an emission standard or operating requ i r ement while hazardous waste remains in ibe com b us tion cham be

r (i
.e., when the hazardous waste residence time has not transpired siJ1ce the hazardous waste feed was cutoff) during a 60-day block period, the Pennittee must

(aa) Within45 days of the lOth exceedance, complete an investigation of the cause of each exceedance



### VES010182Voolia EST eel

uoi cal Solutions, LLC. Permit No.: V-lL-1716300103 -2014- 10 Issuance Date: DRAFT Expirat i on Dille: DRAFT Pa go24of l 72

and evaluation ofapproaches to minimize the frequency, d uration. and severity o f each exceedllnce, and revise the s tartup, shutdown. and malfunction plan as warranted b y the evaluation to minimize the frequency, duration, and severity of each exceedance; and (bb) Record the results of the investigation and evaluation in the operating recor d , and i nclude a swrunary of the investigation and evaluation. and any changes to the start up, s hutdown, and malfunction p l an, in the excess emissions report required under condition 2.1(0} ofthis pertnit and 40 C. F. R. § 63.10(e)(3 ). ( 40 C.F
. R. § 63.1206(c)(2)(v)(A)] B. Comp liance with A WFCO requirements when burning hazardous waste during startup and shutdown: [40 C.F.R
. § 63.1206(c){2)(v)(B)]

I. Ifthe Pennittee feed s hazardous waste during startup or shutdown, the Penni ttee must include was te feed restricti ons (e.g., typ e and quantity) , and other appropriate operating conditions and limi ts in the startup , s hutdown , and malfunction plan. [40 C.F.R. § 63 .1 206(c){2)(v)(B}(l} ] II. The Pennittee must interlock the operating limits established under condition 2 .1(C }(6)(iii){B){I ), above, with the automa tic waste feed cutoffsystem required under condition 2
. 1 (C){7) , except for condition 2.1(C){ 7){e). [40 C.P
. R.§ 63.1206(c)(2)(v)(B)(2)) Ill. When feeding hazardous waste during startup or shutdown , the automatic waste feed cutoff s y s tem must immediately and automatically cutoffthe h azardous waste feed i.f the Permittee exceeds the operating limits established under condition 2.l(C )(

6)(b)(iii)(B)( l ) of this permit, except as prov i ded by condition 2. 1(C)(7)
. [ 40 C.F.R. § 63.1206(c)( 2)(v){B)(3)] IV
. Although th e a u tomatic waste feed cuto ff requirements of 40 C.F
. R
. 

### § 63 .1206 (c)(2)(v){B)(4) 

### apply during startup and shutdown, an exceedance ofan e mis sion standard or operdting limit is not a violation of Subpart



### VES0 1 0183Veol ia ES Techni cal Solut ions, L.L.C. Penni t No.: V

-IL-1716300103

- 2014·10 I ssuance Date: DRAFT Page25 ofl72. Expira tion Date: DRAFT E EE if t he Pennittee operates in accordance with 40 C.F.R. § 63.6(eXl)
. [40 C.F.R
. 

### § 63.1206(cX2)(v)(B)(4)) (c) The Permittee shall not cause or allow the continued operation of an emission source during malfunction or bre akdown oft h e emission source or related air pollution con . trol equ i pmen t if such operation woul d cause a violation ofthe stan dards or limitations set forth in the lllinois Administ rative Code, Subchapter c: Emission Standards and Limitations for Stationary Sou rces. Tite Permittee shaH not cause or allow violat io n of the standards or limitations set forth in Subch apter c: Emission Standards a

n

d Limitations for Stat ionary Sources during sta rtu p. ( 35 lAC 201.149] 7. A u

tomat ic waste feed cutoff(A WFCO). [ 40 C.F.R. § 63.1 2 06(c)(3)) (a) The Permittee must operat e the hazardous waste combustor with a functioning A WFCO system that inu n ediately and automatically cuts off the hazardous waste feed, except as provided by condition 2. 1 (CX7)(f): (i) When any of the following are exceeded: Opera t ing paramet er limits specified under condition 2
. 1 (C) ofihi s permit and 40 C.F.R. § 63. 1 209 ; an emission standard monitored by a CEMS ; and t he allowabl e combustio n chamber pressure; (ii) When the s pan va. lue of any CM S de tector, ex c ept a CEMS , is met or exceeded; (iii) Upon malfunction of a CMS monitoring an operating parameter limit specified under condit ion 2
. 1 (C) of this pennit a n

d 40 C
.F
.R
. § 63.120 9 or an e m ission level; or (i v) When any component of the AWFCO syst em fails. [ 40 C
. F.R
. § 63.1206(c)3)(i)) (b) Dueling of combustion gases . Du ring an A WFCO, t h

e Pennittee mus t continue to duct combustion gasse s t o t he air pollut ion control system wh ile hazardous was te remains i n the combu stion chamber (i.e., if the hazardous waste residence time bas not transpired since the hazardous waste feed cutoffsy.'tem was act ivated). [ 40 C.F.R. § 63.1206(c)(3)(ii)] (c) Restarting waste feed. The Permittee mus t con t i n

ue to mon itor d u

ring the cutoff t h e operating parameters for which limits are established under condit ion 2.1(C) of thi s perm it and 40 C. P .R. § 63.1209 and the emissions required under dtat section to be monitored by a CEMS , a n

d must not r e

start the hazardous waste feed u ntil the operating parameters an d



### VE S010184Veolia ES Technical Solutions, L
. L.C. Pennit No.: V-IL

- 17 16300103-201 4- 10 Issuance Date: DRAFT Page 26 of 172 E.'piration Dale: DRAFT emission levels are within the specified limits. [40 C.F.R. § 63.1206(c)(3)(ii i)) (d) Failure of the AWFCO system. Ifthe AWFCO system fai l s to automatically and immediately cut offthe flow ofhazardous waste upon exceedance of a parameter required to be int erlocked with t h e A WFCO system u nder condit i on 2.1 (C)(7)(a) , the Pennittee has failed to com ply with the A WFCO requirements of condition 2.1 (C)(7). If an equipment or other failure prevents immediate and automatic cutoff ofthe hazardous waste feed, however, the Permittee must cease feeding hazardous waste as quickly as possible. (40 C.F.R. 

### § 63.1206(c)(3)(iv)] (e) COrrective measures. If, after any A WFCO, there is an exceedance ofan emission standard or operating requirement, irrespective of whether the exceedance occurred while hazardous waste remained in the combustion chamber (i.e., whether the hazardous waste residence time has transpired since the hazardous waste feed cutoff system was activated), the Permittee must investigat e the cause oft he AWFCO , take appropriate corrective measures to minimize future A WFCOs, and record the findings and corrective measures in the operating record. [ 40 C .F.R. § 63.1206(c)(3)(v)] (f) Ramping down waste feed. [40 C.F.R. § 63.1206(c)(3)(viii)) (i ) Tite Pennittee may ramp down dte waste feedrate of pumpable hazardous waste over a period not to exceed I minute, except as provided by co ndition 2 .l(C)(7)(f)(ii) of this permit, below. Ifthe Permittee elects to rantp down the waste feed, the Permittee must document ramp down procedures in the operating and maintenance plan
. The procedures must specify that the ramp down begins immediately upon initiation of A WFCO and the procedures must prescribe a bona fid e ramping down. If an emission standard or operating limit is exceeded during the ramp down , the Permittee has failed to comply with the emission standards or operating requirements of40 C.F.R. Part 63, Subpart BEE. (ii) If the AWFCO is triggered by an exceedance of any of the following operating limits, the Permitt e

e may not ramp down the waste feed cutoff: minimum combustion chamber temperature, maximum haza rdous waste feedrdte, or any hazardous waste firing system operating limits that may be established for its combustor. (g) Compliance with the A WFCO requirements in 40 C.F.R. Part 63, Subpart EEE, 

### will assume compliance with the requirements for a waste 

### feed cutoff interlock system and sensors required by construction permits 87100024, 88010001, and 83120053. [40 C.F. R. § 71 .6(a)(3)(i)(A) ]



### VES010185Vcolia ES Te<:hni cal Solutions, L .L. C
. Pennit No.: V· IL · 17 16300103 · 2014 · 10 I ssuance Date: DRAFT Expiration Dille: DRAFT Page 27 of 172

8. Emergency safety vent (ESV) openings. (40 C.F.R. § 63. 1 206(c)(4)] (a) Failure to meet standards. If an ESV opens when hazardous waste remains in the combustion chamber (i.e. , when the hazardous waste residence time has not expired) during an event other than a malfunction as defined in the startup , shutdown, and malfunction plan such that combustion gases are not treated as during the most recent comprehensive performance test (e.g., if the combustion gas by-passes any emission control device that was operating during the performance test) , the Peanittee must document in the operating record whether the source remained in compliance with the emission standards of40 C.F.R. Part 63 , Subpart EEE, considering emissions during the ESV opening event. (40 C.F.R. § 63.1206(c)(4)(i)) (h) ESV operating plan. [40 C.P.R.§ 63.1206(c)(c)(4)(ii)] (i) The Pemuttee must develop an ESV operating plan, comply with the operating plan, and keep the plan in the operating record. (ii ) The ESV operating plan must provide detailed procedures for rapidly stopping the waste feed, shutting down the combustor , and, if feasible , maintaining temperature and negative pressure in the combustion chamber during the hazardous waste residence time. The plan must include calculations, information and data documenting the effect iveness ofthe plan's procedures for ensu ring that combustion chamber temperature and negative pressure are maintained as is reasonably feasible. (c) Corrective measures . Afte r any ESV opening that res u lts in a failure to meet the emission standards as defined in condi t ion 2. J(C)(8)(a) of t his permit, the Permittee must investigate the cause of the ESV opening, take appropriate corrective measures to min imize such future ESV openings, and record the findings and corrective measures in the operating record. (40 C.F.R. 

### § 63.1206(c)(4)(iii)] 9. Combustion syst em leaks. (40 C.P.R.§ 63.1206(c)(5)) (a) The Permittee must control combustion system lea ks of hazardous air pollutants by maintaining the maximum combustion zone pressure lower than ambient pressure using an i nstantaneous monitor ; and [ 40 C.F.R. § 63.1206(c)(5)(i)(B)J (b) The Permittee must specify in the performance test work plan a n

d NOC the method that it 

### will use to control combustion system l eaks
. Because the Permittee controls combu•1ion system leaks by maintaining t he



### VES010186Veolia ES Technical Solutions, L.LC. Pennit No.: V-llr17 1 6300103

- 2014

- IO Issuance Date: DRAFT Pase 28 of 172 Expiration Date: DRAFT combustion zone pressure lower than ambient pressure using an instantaneous monitor, the Permittee must also specify in the performance test work plan and NOC the monitoring and recording frequency of the pressure monitor, and specify bow the monitoring approach is integrated into the automatic waste feed cutoff system. [40 C.F.R. § 63.1206(c)(5)(ii)] I 0. Operator training and certification. (40 C.P.R
. § 63
. 1206(c)(6)J (a) The Permittee must establish training programs for all categories of personnel whose activities may reasonably be expected to directly affect emissions of hazardous air pollutants 

### from the source. Such persons include, but are not limited to, chief facility operators, control room operators, continuous monitoring system operators, persons that sample and analyze feedstreams, persons that manage and charge feedstreams to the combustor, persons that operate emission control devices, and ash and waste handlers. Each training program shall be of a t echnical level commensurate with the person's job duties specified in the training manual. Each commensurate training program shall require an examination to be admini stered by the instructor at the end of the training course. Passing ofthis te st shall be deemed the "certificat ion" for personnel , except that, for control room operators, the training and certification program shall be as specified in conditions 2.l((;)(IO)(c) through (e) of this permit [40 C.P.R.§ 63.1206(c)(6)(i)] (b) The Permittee must ensure that the source is operated and maintained at all times by persons who are trained and certified to perform these and any other duties that may affect emissions of hazardous air pollutants. A certified control room operator must be on duty a t the site at all times the source is in operation. [40 C
. F
. R
. § 63.1206(c)(6)(ii)] (c) Hazardous waste incinerator control room operators must: [40 C.P.R. § 63.1206(c)(6)(iii)) (i) Be trained and certified under a site-specific, sou rce - developed and implemented program that meets the requirements of**c~ndition** 2
. 1(C)(IO)(d), below; or (ii) Be trained under the requirements of, and certified under, one ofthe following American Society of Mechanical Engineers (ASME ) standards: QH0- 1 -1994, QH0

- 1 a-1996 , or QH0-1-2004 (Standard for tl1e Qualification and Certification of Hazardous Waste Incinerator Operators). If the Pennittee elects to 

### use the 

### ASME program:



### VESO!Ol87Voolia ES Technical Solut ion•, LL
.C. Pllge 29 o f 172 Permit No.: V

- I L

- 1716 3 00 103

- 2014-10 Issuance Date: DRAFT Expirat i on Date: DRAfT A
. Control room operators mus t, prior to the compliance date, achieve provisional certification , and must subm it an applicat ion t o ASME and be scheduled for the full certification exam. Within I year of the compliance date , control room operators must achieve full certification; B. New operators a nd operators o f new sources must, before assuming their duties, achieve provisiona l cert i fication , and must submit an applica tion to ASME, and be scheduled fo r th e full certification exam. Within I year of assuming their duties, these operators must ach ieve full certification; or (iii) Be trained and certified under a S tate program. ( d) Site-specific, source developed and implemented training programs for conrro l room operators must include the follow i ng elements: (i) Training on the following subjects: A. Envirorunental concerns, including types ofemissions ; B. Basic combust i on principl es, including products of c ombustion; C. Operation of the specific iype of combustor used by the operator, including proper startup , waste 

### firing, and shutdown procedures ; D. Combu s tion controls and continuous monitoring systems ; E
. Operation of air pollution control equipment and factors affecting perf ormance ; F. I ns pect ion a nd maintenance of dte com b ustor, continuous monitoring systems , and air pollution control devices; G. Actions to correct malfunctions or conditions that may lead to malfunction; H
. Residue c haracterist ics a nd handling procedures ; an d l. Applicable federal , state, and local regulations , inclu ding Occupational Saf ety and Health Adm i nistration workplace standards
. ; and



### VES010l88Veolia ESTechoical Solutions, L.L
.C. Permit No.: V -IL-171 6300 103-2014

- 10 Issuance Date: DRAFT Page 30 of 172 Expira tion Date: DRAFT (ii) An examination designed and administered by the instructor; and (iii) Written material covering the traioing course topics that may serve as reference material following completion ofthe course. [40 C.F.R. § 63. 1 206(c)(6)(v)] (e) To maintain control room operator qualification under a site-specific, source developed and implemented training program as provided by condition 2.i(C)(!O}(d), above, control room operators m us t complete an annual review or refresher course covering, a t a minimum, the follow ing topics: (i) Update of regulations ; (ii) Combustor operation, including startup and shutdown procedures, waste firing, and residue handling; (iii) Inspection and maintenance; (iv) Responses to malfunctions or conditions that may lead to malfunction; and (v) Operating problems encountered by the operator. [40 C.F.R. § 63.1206(cX6Xvi)) (t) The Permittee must record the operator training and certification program in the operating record. [40 C.F.R. 

### § 63.1206(c)(6)(vii)] 11. Operation and maintenance plan. [40 C.F .R. § 63. 1206(c)(7)] (a) The Permittee must prepare and at aU times operate according 10 an operation and maintenan ce (O&M) plan that describes in detail procedures for operation, inspection, maintenance, and corrective measures for all components ofthe combustor, including associated pollution control equipment, that could affect emissions ofregulated hazardous air pollutants. [ 40 C.F.R. 

### § 63.1206(c)(7Xi)J (b) Tite plan m ust prescribe how the Permittee will operate and maintain the combustor in a manner consistent with good air pollution control practices for minimizing emissions at least to the levels achieved during the comprehensive performance test. [40 C.F
. R. 

### § 63.1206(cX7)(ii))



### VESOlOI89Veolia ES Technical Solu1ions, LL.C. Penni< No.: V- f L- 1716300103-2014

- 10 Issuance Dale: DRAFT Expiration Da<e: DRAFT Page31 ofl72
(c) This plan ensures compliance with the operation and maint enance requirements of40 C.F.R § 63.6(e) and mirumizes emissions of pollutants, automatic waste feed cutoffs, and malfunctions. [40 C.F.R. § 63.1206(c )(7)(iii)

## l (d) T he Perm ittee must record t he plan in t he operating record. [40 C.F.R. § 63.1206(c)(7)(iv)) (D ) Monitoring and Testing [40 C.F.R. 

### § 71.6(a)(3)(1)(A)) I
. Con tinuous emissions monitoring systems (CEMS) and continuous opacity monitoring systems (COMS). (40 C.F.R. § 63.1209(a)]: (a) The Permittee must use either a carbon monoxide or hydrocarbon CEMS to demonstrate and monitor compliance with the carbon monoxide or hydrocarbon standard
. The Permittee must also use an oxygen CEMS to continuously correct the carbon monoxide measurements to 7 percent oxygen . (b) After such time as the EPA promulgates all performance specifications and operational requirements applicable to PM CEMS, the Permittee must install, calibrate, maintain, and operate a PM CEMS to demonstrate and monitor compliance with the particulate matter standards under this penn it. (c) Performance s pecifications. The Permittee must install, calibrate, maintain, and continuously operate all CEMS and COMS in compliance with the quality assurance procedures provided in the appendix to 40 C.F.R. Part 63, Subpart BEE, and Performance Specifications I (opacity), 4B (carbon monoxide and oxygen), and 8A (hydrocarbons) in Appendix B to 40 C.F.R. Part 60. (d) Carbon monoxide readings exceeding the span should be recorded in accordance with the following requirements of40 C.P.R.§ 63.1209(a)(3): (i) Except as provided b y 40 C.F
. R_ § 63
. 1209(a)(3Xii), if a carbon mo. noxide CEMS detects a response that res ults in a 1-min ute average at or above the 3,000 ppmv span level required by Performance Specification 4B in Appendix B t o 40 C
.F.R. Part 60, the Permittee must record the )

- minut e average as 10,000 ppmv. The Permittee must use the 1-minute I0 ,000 ppmv val ue for calculating the hourly rolling average carbon monoxide level. (ii) Carbon monoxide CEMS that use a span value of I 0,000 ppmv when !-minute carbo n monoxide levels are equal to or exceed 3 ,000 ppmv



### VES01019 0Veol ia BS Technical Solutions, L. LC. Pennit No.: V

-IL- 17 16300 103

- 2014

- 10 Issuance Date: DRAFT Page 32 of 172 Expiration Date : DRAFT
are not subject to 40 C.F.R. § 63.1209(a)(3)(i). Carbon monoxide CEMS that use a span value of 10,000 are su bject to the same CEMS performance and equipment specifications when operating in the range of3,000 ppmv to 10,000 ppmv that are provided by Performance Specification 4B for other carbon monoxide CEMS , except: A. Ca li bration drift must be Jess than 300 ppmv; and B. Ca li bration error must be less than 500 ppmv. (e) Hydrocarbon readings exceeding the span. (i) Except as provided by 40 C.P.R.§ 63.1209(aX4Xii), ifa hydrocarbon CEMS detects a response that results in a !-minute average at or above the I 00 ppmv span level required by Performance Specification SA in Appendix B to 40 C.F .R. Part 60, the Permittee must record the )-minute average**a~** 500 ppmv. The Permittee must use the !

- minute 500 ppmv value for calculating the hourly rolling average hydrocarbon level. (ii) Hydrocarbon CEMS that use a span value of 500 ppmv when !-minute hydrocarbon levels are equal to or exceed I 00 ppmv are not subject to 40 C.F.R. § 63.1209(a)(4)(i). Hydrocarbon CEMS that use a span value of 500 ppmv are subject to the same CEMS performance and equipment specifications when operating in the range of I 00 ppmv to 500 ppmv that are provided by Pe
. rformance Specification 8A in Appendix B to 40 C.P.R. Part 60 for other hydrocarbon CEMS, except:

A
. The zero and high-level calibration gas must have a hydrocarbon lev el of bet ween 0 and 100 ppmv, and between 250 and 450 ppmv, respectively ; B. The strip chart recorder, computer, or digital recorder must be capable of recording all readings within the CEM m easuremen t ran ge and must have a resolution of2.5 ppmv; C. The CEMS calibration must not differ by more than ± 15 ppmv after each 24-hour period ofthe seven day test at both zero and high levels; D. The calibration enur must be no greater than 25 ppmv; and



### VES01019lVoolia ES Tetboic al Soluti ons. L. l
. C. Pennit No.: V

-IL

- 171 6300 103

- 2014

- 10 I ssuance Dat e: DRAFT E

xpirat i on Date: DRAFT Page 33 o f 1 72

E. The zero level , mid-level, and high level calibration gas used to determine calibrat ion error mus t have a hydrocarbon level of 0

- 200 ppmv , 150-200 ppmv , and 350-400 ppmv, respectively . (f) Petitions to use CEMS for other standards. T he P ermittee may petition EPA to use C E MS for compliance monitoring for particu late matter, m

ercury, semivolatile metals , low volatile metals, and hydrogen chloride and ch lorine gas under 40 C.F.R. 

### § 63.8(1), in lieu of compliance with t he corresponding operating parameter limits . (g) Calculation ofrolling averages. The Permittee shall calcula t e rolling averages in accordance w i th t he following requirements of40 C.P
. R. § 63
. 1209(a)(6): (i) Calculation of rolling averages upon intem1ittent operations. The Permittee must ignore per iods of time when 1 -minute values are not avail.able fo r calculating the hourly rolling average. When 1-minute values become available again , the first 1-minute value is added to the previous 59 values to calculate the hourly rolling average. [40 C.P
.R. 

### § 63
. 1209(a)(6)(ii)) (ii) Calculation of rolling averages when the hazardous waste feed is cut off. (40 C.F.R. § 63.1209(a)(6)(iii)] A. Except as prov i ded by con dition 2.1(D)(l)(g)(i i )(B), below , the Permittee must continue m onitoring carbon monoxide when the hazardous waste feed i s c u t off if the source is operating
. The Permittee must not res u

me feeding hazardous waste if the emission levels exceed the standard. B. The Permittee is n ot subject t o the CEMS requirements of 40 C.P.R. Part 63, Subpart EEE, during periods of time the Permittee meets the requirements of40 C.F.R. § 63
. 1206(b)(t)(ii) (com pliance with emissions standards for nonhazardous waste burning sources when t he Permittee is not burning h azardous waste). (b) Operating paramet er limits for hydrocarbons. If the Permittee elects to comply with tbe carbon monoxide and hydrocarbon emission standard by continuously m onitoring carbon monoxide with a CEMS , t h

e Permittee must demonstrate that hydrocarbon emissions during the comprehensive performance test do not exceed the hydrocarbon em i ssions standard. In addition, the limits the Permittee establishes o n t he ORE operating parameters required under 4 0 C.F
. R. § 63.1209(j) also must ensure that the Permittee maintains compl iance with the hydrocarbon emission standard.



### VESOIOI92Veolia EST ccboical Solvtions. 1-.L.C. Perm it No.: V

-IL

- 1716300103

- 2014- 10 Issuance Date: DRAFT Page 34 of 172 Expiration Date: DRAFT If the Permittee does not conduct the hydrocarbon demonstration and ORE tests concurrently, the Permittee mus t establish separate operating parameter limits under 40 C.F.R. § 63.1209(j) based on each tes t, and the more restrictive of the operating parameter limits applies. (i) Multi

- metals CEMS. [40 C.F.R. § 63. 1209(g)(2)] The Permittee shall install, calibrate, maintain and operate an x-ray fluorescence multi-metals CEMS for use as a con tin uous parametric monitoring system (CPMS) on Units 2, 3 and 4 within 12 months (365 days) after this permit becomes effec
. tive , unless the Administrat or determines that a time extension is warranted based on the Permittee's documentation in writing of factors beyond its control that prevent the Pennittee from meeting the 12

- montb deadline. The Permittee must also install and operate an oxygen CEMS on each unit to continuously correct the multi-metals CEMS data to 7 percent oxygen . (i) Each multi

- metals CEMS must meet the installation requirements in Other Test Method (OTM) 16, Performance Specification YY (Specifications and Test Procedures for X-ray Fluorescence Based Multi-Metals Continuous Emission Monitoring Systems at Stationary Sources) and the on- going quality control and quality assurance procedures set forth in OTM 20, Procedure Z (Quality Assurance Requirements for X

- Ray

- Fluorescence Based MultiMetals Continuous Emission Monitoring Systems at Stationary Sources) and subsequent revisions. (ii) At a mitumum, each multi

- metals CEMS shall measure and report the total concentrations (regardless of speciation) of the following metals in both their vapor and sol id forms in the exhaust stream: arsenic, beryllium, cadmium, chromium, lead and mercury. If the Permittee installs a multi-metals CEMS that is incapable of me-asuring any ofthe specified metals, the Permittee must quantify that metal's emissions using that metal's feedrate as determined according to cond
. ition 2. I(D)(4)(d) for the most recent 12-hour period for which feedstream analysis data for that metal is available and the system removal efficiency and exhaust parameters used by the Permittee to estimate emissions of ti1a t metal for that 12

- hour period. For this purpose , un l ess otherwise approved in writing by EPA, the Permittee shall base its calculations on the affected metal's feedrate as determined according to condition 2.l(D)(4)(d) , system removal efficiency from the last comprehensive performance test required by conditions 2.1(0)(8) and (10), and continuous flow and temperature data as measured by CMS required under con dition 2.1(0)(2).



### VES010193Yeolia ES Techni cal Solutions, L.l.C. Pennit No.: V-IL

- 1716300103-20 1 4

- 10 Issuance Dote: DRAFT Page 35 of 172 Expiration Date: DRAFT (iii) The parametric range for each metal or class ofmetals measured by the multi-metals CEMS is equal to the emission limit for that metal or class of metals specified in condition 2.l(AX7) ofthis permit. (iv) For a period of no le ss than 12 consecuth • e months, the Permittee shall operate each multi-metals CEMS a t all times except during periods ofmonitor downtime due to calibratioo, quality assurance checks or scheduled maintenance. Operation "at all times" is defined as the collection ofat least one measurement for each successive 15-m inu te period. In order to calculate a valid one-hour b

lock average, valid results must be available for at least three of the four 15

- minute cycles in each hour. (v) Outing the period when each multi-metals CEMS is installed and operating, the Permittee shall calculate and record l -hour rolling average emissions from the raw data obtained by each CEMS. l11e Permittee shall also calculate a 12-bour rolling average ofdata for each CEMS, calculated each hour as the average of data collected over the previous 12 operating hours. The Permittee shall maintain for five years all data used in all calculations. (vi) The Permittee shall report to EPA in accordance with condition 2.l(DXl)(i)(x) for every 12

- hour averaging period during which the 12-hour average emissions from any incinerator were higher d1an the l imits in condition 2
. l(A)(7) whether or not the levels of metals in the feedstream complied with the OPLs in the permit. (vii) During periods when any multi

- metals CEMS is malfunctioning, or during periods of mouitor downtime due to calibration, quality assurance checks or scheduled maintenance, the Permittee shall use data from feedstream analysis, performance tests and/or other CMSs, as provided in this permit, to demonstrate compliance at the respective incinerator with the applicable emissions limits provided that the monitor d owntime lasts at least three of the four 15

- minute cycles in each hour needed to calculate a valid one-h.our block average . (viii) During th e period when any multi

- metals CEMS is being operated, the Permittee must continue to operate other CMS required u nder c

ondition 2.1 (DX2) for the respective incinera tor , and must monitor feedrates for the incinerator using the procedures contained in the feedstream analysis plan required under condition 2.l(D)(4){b), and the supplemental procedures contained in condition 2.l(D){4){d)(2). ( ix ) At the end o f the 12-month period during which each multi-metals CEMS was cont inuously operated, the Permittee may petition the



### VES010194Veolia ES TeclUlical Solutions, LLC. Penni t No.: V

-JL- 17 16300 103

- 2014-10 Issuance Date: DRAFT Page36 of 172
E

xpirat ion Date: DRAFT Administrator, in accordance with 40 C.F.R. § 63.1209(a)(5) , to contin ue to use any or all of the multi-metals CEMS for compliance monitoring for mercury , L VM and SVM under 40 C.F.R. § 63 .8(1) in lieu ofcompliance with the correspond i ng operating parameter limits for the respective incinerators. (x) An y CEMS reading above any parametric range, as defined in conc:lition 2.1 (D)( I)(i)(iii), is a deviation. (xi) Ifthe data from any multi

- metals CEMS show a deviation, the Permittee must analyze the feedstream analysis data for the waste burned at the t ime of the deviation and the combustion conditio ns that existed at the time ofthe deviation to determine why the deviation occurred. The Permittee 

### will send to the Administrator within 30 days ofthe deviation all feedstream analysis data for the period ofthe deviation and its analysis of the cause ofthe deviation, and actions taken to address the deviation. (xii) From the time t hat a CEMS records a deviation, the Permittee must immediately stop feeding t he batch of waste burned when the deviation occurred, and is prohibited from burning the remainder of the batch or any component that comprised the batch at that unit until such time th at the Permittee demonstrates to the Administrator, and the Administrato r indicat es in writ ing that EPA accepts t he demonstration, that a reduction in the feedrate for that affected class of metals is not necessary to assure compliance with the emi s sions limits in this permit. (xiii) If operation ofthe multi -m etals CEMS during the 12-mon th period, in conjunction with feedstream analysis or other relev ant data, reveals that any of the feedrate limits included in this permit mus t be made more stringent in order to assure complian ce with the applicable emission s limi ts, EPA 

### will reopen this permit, pursuant to 40 C.F.R. § 71.7(1) , to either revise the affected feedrate limits or require operation of the multi-metals CEMS for a longer period of time o r permanently
. (xiv) Ifoperation of the multi

-metals CEMS during t he 12

- mon th period, i n conjunction with feedstream analysis or other relevant data, reveals that any of the feedrate limits included in this permit are more stringent than necessary to assure compliance with the applicable emissions limits, th e Pennittee may petition the Administrator to use the results of historical comprehensive performance tests, feedstream analysis , and CEMS data to establish higher feedrate limits for the affected incinerators provided the CEMS data demonstrate that compliance would be assured at the



### VES010195Veolia ES Technical Solutions, L L C. Penni t No.: V-1 L-1 716300 103 -2014-I O Issuance Date: DRAFT Page 37 o fl72 Expiration Date: DRAFT higher feedrate 

### limits regardless of t he waste burned. Nothing in tbis permit or 40 C .F.Jt Part 6 3 , Subpart EEE, obligates tbe Administrator to approve a petition for revised feedrate limits. (xv) Notwithstanding the specific recordkeeping and reporting requirements conta i ned in condition 2
. 1 (E) of Ib is permit , tbe Pemtittee shall, on a quarterly basis, submit to EPA a suuunary of emissions data recorded by each multi-metals CEMS and the !

- hour and 12

- hou r rolling average mercury , SVM and L VM feedrates recorded during the same period. The emissions data summary shall inc lude: A. The !

- hour and 12

- h our rolling average concentrations of mercury, L VM and SVM as recorded by tbe multi-metals CEMS , i n the units of the applicable MACT standards (Jlg/dscm, correc t ed to 7 percent oxygen); B. The 12-hour rolling averag e feedrates, as determined through tbe required feedstream analyses conducted during tbe same period ; C. Sample calculations, equations or other data used by the Permittee to convert CEMS and feedrate data; D. T he total duration in m i nutes ofany excess emissions during the reporting p eriod, the 1-hour and 12-hour rolling average concentrations recorded during each period of excess eotissions, tbe t otal duration of excess emissions expressed as a percent of the toml sour ce operating time during that reporting period, and a breakdown of the total dw-ation of excess emissions during the reporting period into those that are due t o startup/shutdown, control equipment problems , process problems, other known causes, and otber unknown causes; and E. All deviations that occurred during the reporting period and corrective actions taken. 2. Other continuous monitoring s ystems (CMS). [ 40 C.F.R. § 63.1209(b)) (a) The Permittee must use CMS (e.g. , thermocouples, pressure transducers , flow meters ) to document com p liance with the applicab l e opera t ing parameter limits under 40 C
.F
.R. § 63
. 1209
. (b) Except as specifi ed in conditions 2
. l(D)(2)( b )(i) and (ii), below , the Petmittee must install and operate continuous monitoring systems otl1 er than CEMS in conformance with 40 C.F
. R
. § 63
. 8 ( c)(3) that requires, at a



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minim u m, to comply with the manufacturer's written specifications or recommendations for in stallation, operation , a nd calibration of the system: (i) Calibration of thermocouples and pyrometers. The calibration of thermocouples must be verified at a frequency and in a manner consisten t with manufacturer specifications, but no less frequent than once per year. The Permittee must operate and maintain optical pyrometers in accordance with manufacturer specifications unless otherwise approved by the Administrator. The P enninee must calibra te optical pyrometers in accordance with t he frequency and procedures recommended by the manufacturer, but no less frequent than once per year, un le ss otherwise approved by the Administrator. (ii) Ac c u

racy and calibration of weigh t measuremen t devices for activated carbon injection systems. Ifthe Pen:nittee operates a carbon injection system, the accuracy of the weight measurement device must be :1: I percent of the weight being measured. The cal ibration of the device must be verifie<l at least once eac. h calendar quarter at a frequency of approximately 1 2 0 days. (c) A CMS must sample the regula t ed paramet er without int erruption. evalu ate the detector r esponse at least once each 15 seconds, and compute and record the average values at leas t every 60 seconds
. (d) The span of the non-CEMS CMS detector must not be exceeded. The Permittee mu s t interlock the span limits into t he automatic was te feed c u toff system r eq uired by 40 C.F.R. 

### § 63.1206(c)(3). (e) Calculation of rolling averages. (i) Calculation of rolli n g averages upon intermittent operations. The Permittee must ignore periods of time when !-minute val u es are not available when calculating rolling averages . When !-minute values become availab le again, the firs t !-minute value is added to the previous !·minute v alues to calculate rolling average s . (ii) Ca lculation of rolling averages w hen the hazardous waste feed is cutoff
. A
. Except as provided by con dition 2.l(DX2XeXiiXB), below, the Pennittee must continu e monitoring operat ing parameter limits with a CM S when the hazardous**wa~te** feed is cut off if the source is operating. The Permittee must not resume feeding hazardous waste if an operating parameter exceeds its limit.



### VES010197Veol ia ES Technical Solut ions, L
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B. The Pennittee is not subject to the CMS requirements during periods of t ime t he Permittee meets the requireme nts of 40 C.P.R.§ 63.1206(bXl)(ii) (compliance with emissions standards for nonhazardous waste burning sources when the Permittee is not burning hazardous waste). 3. Bag leak detection system requirements. (40 C.F.R. § 63.1206(c)(8)) The Permittee must continuously operate a bag leak detection system under the following requ i rements: (a) A bag leak detection system that meets the specifications and requirements of condition 2.l(D)(3Xb), be low, and the Permittee must compl y with the corrective measures and notification requirements of conditions 2J(DX3)(c) and 2.l(EX5). (b) Bag l eak detection system specification and requirements: (i) The bag leak de tection system mus t be certified by the manufacturer to be capable of continuously detecting and recording patticulate matter emissions at concentrations of 1.0 milligram 

### per actual cubic meter unless the Permittee demonstrates, under 40 C.F.R. § 63.1209(gXI ), that a higher detection limit wou l d routinely detect pa rticulate matter l oadings during n ormal operations; (ii) The bag leak detection system shall provide outp ut of relative or absolute particulate matter loadings ; (i ii ) The bag leak detection system shall be equipped with an alarm system that will sound an audible alarm when an increase in relative particulate loadings is detected over a preset level; (iv) The bag leak detection system shall be installed and operated in a manner consistent with available written guidance from EPA or, in the absence of such written g uidance, the manufacturer's written specifications and recommendations for installation, operation, and adjustment of the system; (v) The initial adjustment of the system shall , at a minimum, consist of establishin g tbe base line output by adjust i ng the sensit ivity (ran ge) and the averaging period of the device, and establishing the alarm set points and the alarm de l ay time; (v i ) Following ini tial adjustment, the Permittee must not adjust the s e nsitivity or range, avemging period, alanu set points , or alarm



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delay time , except as detailed in the operation and maintenance plan required under 40 

### C.F.lt § 63.1206(c)(7). The Permittee must not increase the sensitivity by more than I 00 percent or decrease the sensitivity by more thao 

### 50 percen t over a 365-day period unless such adjustment follows a complet e bagbous e inspection whic
. h demonstrates the baghouse is in good operating condition; and (vii) The bag leak detector shall be installed downstream o f the baghouse and upstream of any wet acid gas scrubber. Where multiple detectors are required, the system's instrumentation and alann system may be shared among the detectors. (c) Bag leak detection system corrective measures requirements. The opera t ing and maintenance plan required by 40 C.F.R. 

### § 63.1206(cX7 ) must include a corrective measures plan that specifies the procedures the Permittee will fo ll ow in the case of a bag leak detection system alanu or malfunction. The corrective measures plan must include , a t a minimum , the procedures used to determine and record the time and cause of t he alanu as well as the corrective measures taken to correct the control device malfunction or minimize emissions as specified below. Failure to initiate the correct ive measures required by this condition 2
. 1(D)(3)(c) is failure to ensure compliance with the emission standards in 40 C.F.R. Pan 63, Subpart BEE. (i) The Permittee must initiate the procedures used to determine th
. e cause of the alrum within 30 minutes ofthe time the alarm first sounds; and (ii) The Permittee must alleviate the cause of the alanu by taking the necessary corrective measure(s) which may include, but are not to he limited to, the following: A. Inspecting the baghouse for air leaks, tom or broken filter elements, or any other malfunction that may cause an increase in emissions ; B. Sealing offde f ecti ve bags or filter media; C. Re pla cing defective bags or filter media, or otherwise repairing the control device; D. Sealing off a defective baghouse compartment; E. Cleaning the bag leak detection system probe , or otherwise repairing th e bag leak detection sys te m; or



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