# A U G1 6 

# 201 3

GWV!RONM£NTA L SERVICE S 

### (Fed-Ex'd )

Augus t 15 , 201 3

Mr
. Davi d Ogule i U S Environmenta l Protectio n Agenc y Regio n 5 7 7 Wes t Jackso n Blv d Mai l Code : AR-18 J Chicago , I L 60604-350 7 Dea rMr
. Ogulei , Enclose d ar e tw o copie s o f th e Addendu m t o Applicatio n fo rRenewa l o f a Majo rSourc e Operatin g Permi t fo rth e Veoli a E S Technica l Solutions , L.L.C
. Sauget , Illinoi s facility
. Th e Addendu m i s comprise d o f th e Veoli a Titl e V permi t renewa l applicatio n submitte d i n Apri l 201 3 an d al l informatio n reference d i n th e Apri l 201 3 submittal
. Previousl y reference d materia l i s include d no wi n expande d form , a s requested , t o ai d th e revie w process . I f yo u hav e an yquestion s o n thi s submitta l o rwoul d lik e t o mee t an d discus s thi s addendum , pleas e cal l Denni s Warcho l o rDou g Harri s a t (618 ) 271-2804
. Sincerely ,
Nanc yL
. Paddoc k Environmenta l Engineerin g Specialis t Att
. C : EP AFil e

# 7 Mobil e Avenue , Sauget , I L 62201 (618 ) 271-280

4 www.veoliaes.co m

# :AU S I 6



# ADDENDU M T O APPLICATIO N FO R RENEWA L O F A MAJO RSOURC E OPERATIN G PERMI T

VeoliaE S Technica

l Solution

s # 7 Mobil e Avenu e Sauget , Illinoi s 6220 1

AUGUS T 201

3

l

## TABL E O F CONTENT S

I . COMPLIANC E CERTIFICATIO N 1 II . INTRODUCTIO N 2 III . FACILIT Y DESCRIPTIO N 3 A . Ai rPermi tHistor y 3 B . Proces s Informatio n 3 1 . Storag e Unit s 4 a . Tank s 4 b . Container s 5 2 . Incineratio n Unit s 6 a . Uni t2 an d Uni t3 6 b . Uni t4 7 c . Ai rPollutio n Contro l Device s - Uni t2 an d Uni t3 9 d . Ai rPollutio n Contro l Device s - Uni t4 1 1 3 . Othe rTreatmen tUnit s 1 5 a . Materia l Processin g Area s 1 5 b . Bul kFee d Buildin g 1 5 c . Glov e Bo x Buildin g 1 5 d . Dru m Crushe r1 6 4 . Ancillar y Processe s 1 6 C . Genera l Ai rEmissio n Informatio n 1 6 IV . REGULATOR Y APPLICABILIT Y AN D PERMI T CONDITION S 1 7 A . Facility-wid e Requirement s 1 7 1 . Fugitiv e Particulat e Matte r[3 5 IA C 212.301 ] 1 7 2 . Ope n Burnin g Prohibition s [3 5 IA C 237.102 ] 1 7 3 . Organi c Emission s fro m Pump s an d Compressor s [3 5 IA C 219.142 ] 1 7 4 . NESHA Pfro m Off-sit e Wast e an d Recover y Operations : Equipmen tLeak s [4 0 CF R63.691(b)(1) ; 40 CF R6 1 Subpar tV ] 1 7 5 . Preventio n o f

Significan tDeterioratio n an d Nonattainmen tNe w Sourc e Revie w 1 7 B . Incinerators : Uni t2 , Uni t3 , an d Uni t4 Emissio n Standar d Requirement s 1 8 1 . Visibl e Emission s 1 8 a . Visibl e Emission s Limitation s [3 5 IA C 212.123(a) ] 1 8 b . Fugitiv e Particulat e Matte r[3 5 IA C 212.30 1 an d 212.314 ] 1 8 2 . Sulfu rDioxid e Emission s 1 9 a . Sulfu rDioxid e Annua l Emissio n Limitatio n 1 9 3 . Carbo n Monoxid e Emission s 1 9 a . NESHA Pfo rHazardou s Wast e Combustor s [4 0 CF R63.1219(a)(5) ] 1 9 b . Carbo n Monoxid e Limitation s fo rIncinerator s [3 5 IA C 216.141 ] 1 9 c . Carbo n Monoxid e Annua l Emissio n Limitatio n 1 9 4 . Particulat e Matte rEmission s 1 9 a . Particulat e Matte rLimitation s fo rIncinerator s [3 5 IA C 212.181(b) ] 1 9 b . NESHA Pfo rHazardou s Wast e Combustor s [4 0 CF R63.1219(a)(7) ] 2 0c . Particulat e Matte rAnnua l Emissio n Limitatio n 20 5 . Volatil e Organi c Materia l Emission s 2 0 a . Us e o f

Organi c Materia l [3 5 IA C 219.30 1 an d 219.302 ] 20 b . Volatil e Organi c Materia l Annua l Emissio n Limitatio n 2 0 6 . Nitroge n Oxid e Emission s 20 a . Nitroge n Oxid e Annua l Emissio n Limitatio n 2 0 7 . Hazardou s Ai rPollutan tEmission s 20 a . NESHA Pfo rHazardou s Wast e Combustor s - Dioxi n an d Fura n Emissio n Limitation s [4

0 CF R63.1219(a)(1) ] 20 b . NESHA Pfo rHazardou s Wast e Combustor s - Mercur y Emissio n Limitation s [4

0 CF R63.1219(a)(2) ] 2 1 c . NESHA Pfo rHazardou s Wast e Combustor s - Semi-volatil e Meta l Emissio n Limitation s [4

0 CF R63.1219(a)(3) ] 2 1 d . NESHA Pfo rHazardou s Wast e Combustor s - Lo w Volatil e Meta l Emissio n Limitation s [4

0 CF R63.1219(a)(4) ] 2 1 e . NESHA Pfo rBenzen e Wast e Operation s [4 0 CF R61.348(a)(l)(iii) ] 2 1 f . NESHA Pfro m Off-sit e Wast e an d Recover y Operation s [4 0 CF R 63.689(c)(2) ] 2 1 8 . Hydroge n Chlorid e Emission s 2 1 a . NESHA Pfo rHazardou s Wast e Combustor s - Hydroge n Chlorid e Emissio n Limitation s [4

0 CF R63.1219(a)(6) ] 2 1 b . Hydroge n Chlorid e Emissio n Limitatio n 2 1 9 . Destructio n an d Remova l Efficienc y (DRE ) Requiremen t2 2 a . NESHA Pfo rHazardou s Wast e Combustor s - DR E Standar d [4 0 CF R 63.1219(c)(1) ] 2 2 b . NESHA Pfo rHazardou s Wast e Combustor s - DR E Standar d [4 0 CF R 63.1219(c)(2) ] 2 2 c . NESHA Pfo rHazardou s Wast e Combustor s - DR E Standar d [4 0 CF R 63.1219(c)(3) ] 2 2 C . Incinerators : Uni t2 , Uni t3 , an d Uni t4 Wor kPractic e an d Operationa l Requirement s 2 3 1 . Operatin g Paramete rLimit s 23 a . NESHA Pfo rHazardou s Wast e Combustor s [4 0 CF R63.1206(a) , (b ) an d 63.1209)0) throug h (p) ] 2 3 b . NESHA Pfo rHazardou s Wast e Combustor s [4 0 CF R63.1206(c)(1 ) an d 63.1211(c) ] 2 5 c . NESHA Pfo rHazardou s Wast e Combustor s [4 0 CF R63.1206(c)(2 ) an d 63.6(e)(3) ] 25 d . NESHA Pfo rHazardou s Wast e Combustor s [4 0 CF R63.1206(c)(3 ) an d 3 5 IA C 201.149 ] 25 e . NESHA Pfo rHazardou s Wast e Combustor s [4 0 CF R63.1206(c)(4) ] 2 6 f . NESHA Pfo rHazardou s Wast e Combustor s [4 0 CF R63.1206(c)(5) ] 2 6 g . NESHA Pfo rHazardou s Wast e Combustor s [4 0 CF R63.1206(c)(6) ] 2 6 h . NESHA Pfo rHazardou s Wast e Combustor s [4 0 CF R63.1206(c)(7 ) an d 63.6((e) ] 2 7 2 . Wor kPractic e Requirement s 2 7

i iD . Incinerators : Uni t2 , Uni t3 , an d Uni t4 Monitorin g Requirement s 28 1 . Continuou s emission s monitorin g system s (CEMS ) an d continuou s opacit y monitorin g system s (COMS ) [4 0 CF R63.1209(a) ] 2 8 a . NESHA Pfo rHazardou s Wast e Combustor s [4 0 CF R63.1209(a)(l)(i) ] 2 8 b . NESHA Pfo rHazardou s Wast e Combustor s [4 0 CF R63.1209(a)(l)(iii) ] 2 8 c . NESHA Pfo rHazardou s Wast e Combustor s [4 0 CF R63.1209(a)(2) ] 2 8 d . NESHA Pfo rHazardou s Wast e Combustor s [4 0 CF R63.1209(a)(5 ) an d 63.8(f) ] 2 8 e . NESHA Pfo rHazardou s Wast e Combustor s [4 0 CF R63.1209(a)(6) ] 2 8 2 . Othe rcontinuou s monitorin g system s (CMS ) [4 0 CF R63.1209(b) ] 29 a . NESHA Pfo rHazardou s Wast e Combustor s [4 0 CF R63.1209(b)(1 ) an d (2) ] 2 9 b . NESHA Pfo rHazardou s Wast e Combustor s [4 0 CF R63.1209(b)(3) ] 29 c. NESHA Pfo rHazardou s Wast e Combustor s [4 0 CF R63.1209(b)(4) ] 29 d . NESHA Pfo rHazardou s Wast e Combustor s [4 0 CF R63.1209(b)(5) ] 29 3 . Ba g lea k detectio n system s (CMS ) [4 0 CF R63.1206(c)(8) ] 29 4 . Feedstrea m Analysi s [4 0 CF R63.1209(c) ] 3 0 5 . Performanc e Evaluation s [4 0 CF R63.1209(d) , 63.8(d ) an d 63.8(e) ] 30 6 . Conduc to f

Monitorin g [4

0 CF R63.1209(e) an d 63.8(b) ] 3 0 7 . Operatio n an d Maintenanc e o f Continuou s Monitorin g System s [4 0 CF R 63.1209(f

) an d 63.8(c) ] 3 1 8 . Reductio n o f

Monitorin g Dat a[4 0 CF R63.1209(h ) an d 63.8(g) ] 3 1 9 . Operatin g Parameter s fo rMultipl e Standard s [4 0 CF R63.1209(i ) throug h (P) ] 3 1 10 . Operatin g Paramete rLimi tAveragin g Period s [4 0 CF R63.1209(r) ] 3 1 E . Incinerators : Uni t2 , Uni t3 , an d Uni t4 Performanc e Testin g Requirement s 3 1 1 . Change s t

o th e Sourc e [4

0 CF R63.1206(b)(5)(i)(B) ] 3 1 2 . Complianc e wit h C O an d TH C Emissio n Standar d [4 0 CF R63.1206(b)(6) ] 3 2 3 . Type s o f

Performanc e Test s [4 0 CF R63.1207(b) ] 3 2 4 . Frequenc y o f

Performanc e Test s [4 0 CF R63.1207(d) ] 3 2 5 . Conten to f

Performanc e Tes tPlan s [4 0 CF R63.1207(f) ] 3 3 a . NESHA Pfo rHazardou s Wast e Combustor s [4 0 CF R63.1207(f)(1) ] 33 b . NESHA Pfo rHazardou s Wast e Combustor s [4 0 CF R63.1207(f)(2) ] 3 5 6 . Operatin g Condition s Durin g Performanc e Test s [4 0 CF R63.1207(g) ] 36 a . NESHA Pfo rHazardou s Wast e Combustor s [4 0 CF R63.1207(g)(a) ] 36 b . NESHA Pfo rHazardou s Wast e Combustor s [4 0 CF R63.1207(g)(b) ] 37 7 . Operatin g Condition s Durin g Subsequen tPerformanc e Test s [4 0 CF R 63.1207(h) ] 38 8 . Tes tMethod s [4 0 CF R63.1208 ] 38 9 . Failur e o f

Performanc e Tes t[4 0 CF R63.1207(1) ] 3 8 a . NESHA Pfo rHazardou s Wast e Combustor s [4 0 CF R63.1207(1)(1) ] 3 8 b . NESHA Pfo rHazardou s Wast e Combustor s [4 0 CF R63.1207(1)(2) ] 3 9 c . NESHA Pfo rHazardou s Wast e Combustor s [4 0 CF R63.1207(f)(2) ] 39 F . Incinerators : Uni t2 , Uni t3 , an d Uni t4 Recordkeepin g an d Reportin g 39 1 . Summar y o f

Notificatio n Requirement s [4 0 CF R63.1210(a) ] 39 2 . Summar y o f

Reportin g Requirement s [4 0 CF R63.1211(a) ] 4 2 3 . Summar y o f

Recordkeepin g Requirement s [4 0 CF R63.1211(b) ] 4 2

i i iG . Wast e Processin g Uni tRequirement s (MP-1 , MP- 2 an d LPR ) 43 1 . Visibl e Emission s Limitation s [3 5 IA C 212.123 ] 43 2 . Us e o f

Organi c Materia l [3 5 IA C 219.301 ] 44 3 . NESHA Pfo rOff-sit e Wast e an d Recover y Operation s [4 0 CF R6

3 Subpar t DD ] 44 4 . NESHA Pfo rContainer s [4 0 CF R63.922 ] 4 4 5 . NESHA Pfo rContainer s [4 0 CF R63.925 an d 4 0 CF R71.6(a)(3)(i)(A) ] 4 5 6 . NESHA Pfo rContainer s [4 0 CF R71.6(a)(3) ] 45 7 . NESHA Pfo rBenzen e Wast e Operation s [4 0 CF R6 1 Subpar tFF ] 45 8 . Emissio n Calculatio n Requirement s [4 0 CF R71.6(a)(3)(i)(B) ] 45 H . Liqui d Wast e Storag e Tan kRequirement s 4 5 1 . Us e o f

Organi c Materia l [3 5 IA C 219.301 ] 46 2 . Organi c Materia l Emissio n fro m Pump s an d Compressor s [3 5 IA C 219.142 ] 4 6 3 . Standard s o f

Performanc e fo rVolatil e Organi c Liqui d Storag e Vessel s (Includin g Petroleu m Liqui d Storag e Vessels ) fo rWhic h Construction , Reconstruction , o rModificatio n Commence d Afte rJul y 23 , 198 4 [4 0 CF R6

0 Subpar tKb ] 46 4 . Storag e Tank s [3 5 IA C 219.122 an d 129] 4 6 5 . NESHA Pfo rBenzen e Wast e Operation s [4 0 CF R6 1 Subpar tFF ] 4 6 6 . NESHA Pfo rOff-sit e Wast e an d Recover y Operation s [4 0 CF R6

3 Subpar t DD ] 4 6 7 . Monitorin g an d Testin g [4 0 CF R71.6(a)(3)(i)(A ) an d (B) ] 47 8 . Recordkeepin g [4 0 CF R71.6(a)(3) ] 47 9 . Organi c Materia l Emission s [C P#88030001 , Conditio n 3] 47 I . Bul kSoli d Wast e Storag e Facilit y Requirement s 47 1 . Particulat e Emissio n fro m Proces s Unit s fo rWhic h Constructio n o r Modificatio n Commence d O n o rAfte rApri l 14,197 2 [3 5 IA C 212.321 ] 47 2 . Us e o f

Organi c Materia l [3 5 IA C 219.301 ] 4 8 3 . Visibl e Emission s Limitation s [3 5 IA C 212.123 ] 48 4 . NESHA Pfo rBenzen e Wast e Operation s [4 0 CF R6 1 Subpar tFF ] 48 5 . NESHA Pfo rOff-sit e Wast e an d Recover y Operation s [4 0 CF R6

3 Subpar t DD ] 4 8 6 . Wor kPractic e an d Operationa l Requirement s [4 0 CF R71.6(a)(1) ] 4 8 7 . Monitorin g an d Testin g [4 0 CF R71.6(a)(3)(i)(A ) an d (B) ] 4 9 8 . Recordkeepin g an d Reportin g [4 0 CF R71.6(a)(3) ] 4 9 J . Dru m Crushe rRequirement s 50 1 . Us e o f

Organi c Materia l [3 5 IA C 219.301 ] 50 2 . Particulat e Matte rLimitatio n [3 5 IA C 219.321 ] 5 0 3 . Visibl e Emission s Limitation s [3 5 IA C 212.123 ] 50 4 . Monitorin g an d Testin g [4 0 CF R71.6(a)(3)(i)(A ) an d (B) ] 50 5 . Recordkeepin g an d Reportin g [4 0 CF R71.6(a)(3) ] 5 1 K . Boile rRequirement s 5 1 1 . Fue l Combustio n Emissio n Source s ( > 1 0 MMBtu/hr ) [3

5 IA C 216.121 ] 5 1 2 . Standard s o f

Performanc e fo rSmal l Industrial-Commercial-Institutiona l Stea m Generatin g Unit s [4 0 CF R6

0 Subpar tDc ] 5 1 3 . Visibl e Emission s Limitation s [3 5 IA C 212.123 ] 5 1

i v4 . Emissio n an d Operationa l Limitation s [CP #95080025 ] 5 2 5 . Emissio n Limitation s [4 0 CF R63.52 ] 5 2 6 . NESHA PMajo rSources : Industrial , Commercia l an d Institutiona l Boiler s an d Proces s Heater s [4 0 CF R6

3 Subpar tDDDDD ] 5 2 7 . Monitorin g an d Testin g [4 0 CF R71.6(a)(3)(i)(A ) an d (B) ] 5 2 8 . Recordkeepin g an d Reportin g [4 0 CF R71.6(a)(3) ] 5 3 L . Emergenc y Generato rRequirement s 5 3 1 . NESHA Pfo rStationar y Reciprocatin g Interna l Combustio n Engine s [4 0 C F R6 3 Subpar tZZZZ ] 5 3 2 . Wor kPractic e Standard s [4 0 CF R63.6602) ] 5 4 3 . Recordkeepin g an d Reportin g [4 0 CF R63.6655 ] 5 5 M . Gasolin e Storag e Tank s 55 1 . Storag e o f

Gasolin e [3

5 IA C 219.122 ] 5 5 2 . Gasolin e Dispensin g Operation s [3 5 IA C 219.583 ] 55 3 . Recordkeepin g an d Reportin g [4 0 CF R71.6(a)(3) ] 5 5 V . AI REMISSION S INFORMATIO N 56 A . Insignifican tAi rEmissio n Source s 56 B . Lis to f

Ai rEmissio n Source s wit h Regulator y Requirement s 57 C . Emissio n Calculation s 58 1 . Uni t2 Incineratio n 58 2 . Uni t3 Incineratio n 5 9 3 . Uni t4 Incineratio n 5 9 4 . Existin g Boile r6 0 5 . La b Pac k Repac k Buildin g (LPR ) 6 1 6 . Materia l Processin g Are a1 (MP-1 ) 6 1 7 . Materia l Processin g Are a2 (MP-2 ) 6 2 8 . Bul kSolid s Storag e 6 2 9 . Dru m Crushe r6 2 10 . Tank s 6 5 VI . COMPLIANC E METHOD S 6 6 A . Continuou s Emissio n Monitor s 66 ( B . Proces s Paramete rMonitorin g 67 C . Demonstratio n o f Complianc e wit h Applicabl e Requirement s 6 8 VII . RECORDKEEPIN G AN D REPORTIN G 7 4 A . Recordkeepin g 7 4 B . Reportin g Requirement s 78 APPENDICE S APPENDI X A FORM S APPENDI X B NON-APPLICABIL E REGULATION S APPENDI X C FIGURE S APPENDI X D CEM S AN D CM S QUALIT Y ASSURANC E PLAN S APPENDI X E MOS T RECEN T NO C APPENDI X F CONSTRUCTIO N PERMIT S APPENDI X G STARTUP , SHUTDOWN , AN D MALFUNCTIO N PLA N

vAPPENDI X H AUTOMATI C WAST E FEE D CUTOF F PLA N

APPENDI X I ES V OPERATIN G PLA N APPENDI X J FEEDSTREA M ANALYSI S PLA N APPENDI X KTITL E V ITEM S T O B E REMOVE D

v i

## TITL E V PERMI T APPLICATIO N FO RRENEWA L ADDENDU M T O RENEWA L APPLICATIO N

I . COMPLIANC E CERTIFICATIO N I n accordanc e wit h4 0 CF R71.5(c)(9) , th e followin g certificatio n fo r thi s applicatio n documen t

i s provided
.

I certif y unde r

penalt y o f

la w that , base do n informatio n an dbelie f forme dafte r

reasonabl e inquiry , th e statement s an dinformatio n containe di n thi s applicatio n ar e true , accurate , an d complete
. Authorize dSignature : Genera l Manage r Responsibl e Officia l Titl e Dongla s Harri s % / / Type do r

Printe dNam e o f

Signator y Dat e

Acomplianc e certificatio n wil l b e submitte dannuall y t o the appropriat e agencies
. I n addition , adescriptio n o f al l monitoring , recordkeeping , an dreportin g requirement s an dth e method s use dt o demonstrat e complianc e i s include di n subsequen t section s o f

thi s document
. Th e facilit y an dal l emissio n unit s ar e i n complianc e wit hth e enhance d monitorin g an dcomplianc e certificatio n requirement s o f th e Clea n Ai r

Act
.

1

## II . INTRODUCTIO N Veoli aE S Technica l Solutions , L.L.C
. (Veolia ) i s submittin g thi s addendu mt o th e Titl e V permi t renewa l application , submitte dt o USEP A Apri l 9 , 2013 , i n accordanc e wit hth e federa l operatin g permit s progra mi n 4 0 CF RPar t 71
. Th e applicatio n an dth e addendu mar e fo r renewa l o f

Veolia' s Titl e V Permi t t o Operat e No
. V-IL-12716300103-08-01 , whic h expire s Octobe r

12 , 2013
. Th e permi t i s fo r th e operatio n o f

Veolia' s hazardou s wast e storag e an dtreatmen t facilit y i n Sauget , Illinois
. USEP A Par t 7 1 applicatio n form s ar e provide di n Sectio n I X o f thi s document
. Th e additiona l narrativ e tha t follow s i s als o include dt o supplemen t th e informatio n o n th e form s an dt o presen t relevan t

informatio n abou t th e facilit y an dit s operations
.

2

## III . FACILIT Y DESCRIPTIO N

Veoli aE S Technica l Solutions , L.L.C
. (Veolia ) operate s acommercia l hazardou s wast e facilit y i n Sauget , Illinois
. Th e facilit y receive s avariet y o f liquid , solid , an dgaseou s wast e fo r treatmen t

i n incineratio n systems . Th e facilit y include s wast e receivin g areas ; wast e stagin g an dstorag e fo r smal l an dlarg e containers , drums , bul k solids , tan k

trucks , an d cylinders ; thre e incinerator s an dthei r associate dequipment ; alaboratory ; an dothe r sit e infrastructur e an dfacilitie s necessar y t o suppor t th e operations
. Figure s l a- I dprovid e facilit y sit e layou t

information
. (Figure s ar e provide di n Appendi x C. ) A . Ai rPermi tHistor y Veoli aha s receive dth e constructio n permit s fro mth e Illinoi s Environmenta l Protectio n Agenc y (IEPA ) liste dbelo w fo r th e emissio n unit s a t th e Sauge t

facility
. A previousl y permitte demissio n unit , incineratio n Uni t 1 , covere dunde r

permi t #8308007 2 ha s bee n dismantle dan dremove dfro msite
. Uni t 1 (remove dfro mservice ) #8308007 2 Shredde r

syste m #8406006 3 8/8/8 4 Uni t 2 & 3 Constructio n & Tan k Far m# 1 Permi t #8312005 3 9/2/8 6 an drevision s Pneumati c Conveyo r #8711005 2 2/11/8 8 Residu e Fee dSyste mfo r Uni t 1 #8712006 9 4/13/8 8 Uni t 3 Constructio n Permi t #8710002 4 8/19/8 8 an drevision s Uni t 4 Constructio n Permi t #8801000 1 8/3/8 8 an drevision s Tan k Far m# 3 Permi t #8803000 1 6/27/8 8 Specialt y Feede r

fo r Uni t 3 #9303010 7 6/7/9 3 Cleave r Brook s Boile r

1 #9508002 5 Activate dCarbo n Injectio n Uni t 4 #0011003 0 Copie s o f

th e constructio n permit s fo r th e activ e emissio n unit s ar e provide di n Appendi x F
. B . Proces s Informatio n Liqui dwaste s ar e receive da t th e facilit y i n tan k

truck s an ddrums
. Gaseou s (an dsom e liquid ) waste s arriv e i n variou s size dcylinders
. Bul k solid s ar e receive da t th e sit e primaril y i n20

- t o 40-yar droll-of f container s o r

othe r simila r bul k transpor t

vehicles
. Soli dwaste s ar e als o receive di n container s suc ha s drums , totes , an dGaylor dboxes
. Waste s ar e store dprio r t o incineratio n an deithe r fe ddirectl y t o a n incinerator , repackage dint o smalle r charg e container s fo r

incineration , o r

sen t off-sit e fo r

treatmen t

a t othe r locations
. Fixed-heart hincinerator s Uni t 2 an dUni t

3 are designe dt o receiv e containerize dwastes , aqueou s liqui dwastes , organi c liqui dwastes , specialt y liqui dwastes , an dsludg e wastes . Th e aqueou s an dorgani c liqui dwaste s are fe dthroug hair-atomizin g nozzles
. Th e specialt y liqui d feed s an ddirect-injec t liquid s ar e fe dthroug hthe aqueou s o r organi c liqui dfee dsystems . Eac h incinerato r

ca n receiv e an y combinatio n o f liquid , semi-solid , o r soli dwastes . Uni t

2 ca n als o
3receiv e wast e gase s throug hseparat e fee dnozzles
. Th e rotar y kil nincinerato r Uni t 4 ca n incinerat e container , aqueou s liquid , organi c liquid , specialt y liquid , an dsludg e wastes . Liqui d waste s ar e fe dint o eithe r th e kil no r

Secondar y Combustio n Chambe r (SCC)
. Bul k

soli dwaste s ar e fe dint o th e kil nthroug heithe r the ra mfeede r

o r th e scre w auger . Containerize dwaste s ar e fe dint o th e kil nthroug hth e ra mfeede r o r th e auxiliar y ra mfeeder
. Uni t 4 ca n als o accep t liqui dwaste s injecte ddirectl y fro mthe deliver y vehicle
. Th e incinerator s produc e ash , whic henter s th e As hHandlin g System
. As hfro mUnit s 2 an d 3 i s stage di n roll-of f container s temporaril y a t th e As hStorag e Building
. Fro mher e i t i s transporte dt o th e Bul k Fee dBuilding
. As hfro mUni t 4 i s collecte di n roll-of f container s an d transporte dt o Storag e Buildin g #7
. Emission s o f particulat e matte r

ar e minimize dthroug h wor k practice s suc ha s we t handling , coverin g wit hatarp , an dhandlin g insid e enclose d structures . Th e section s belo w provid e detaile dinformatio n fo r th e processin g operation s at th e facility
. 1 . Storag e Unit s Upo n arrival , waste s ar e sample daccordin g t o th e facility' s Wast e Analysi s Pla n an d Fee dStrea mAnalysi s Pla n an danalyze da t Veolia' s on-sit e laboratory
. Bul k liqui d waste s ma y b e transferre dt o Tan k Far m# 1 o r

Tan k Far m#

3 fo r bul k storag e an d blendin g o r

directl y int o Uni t

2 , 3 , o r

4 fo r incineration
. Containerize dliqui dwaste s (drums ) ma y b e transferre dvi adru mpump s t o Tan k Far m# 1 fo r

bul k storag e o r

directl y int o Uni t

2 o r 3 fo r incineration
.
a . Tank s Bul k liquid s are store da

t Tan k Far m# 1 an dTan k

Far m#3
. Al l bul k

liqui dtank s ar e vertical , fixed-roo f

tank s equippe dwit hcarbo n canister s fo r contro l o f

volatil e organics
. Se e Figure s 2 an d3 fo r tan k far mproces s flo w diagrams
. Figur e 4 depict s atypica l tank-to-carbon-caniste r flo w diagram
. (Figure s ar e provide da t th e en do f thi s section. ) Tan k

Far m# 1 include s te n bul k liqui dwast e tank s (2 , 4 , 6 , 8 , 10 , 20 , 30 , 40 , 50 , an d60 ) an dsupplie s bul k liqui dwast e t o Unit s 2 an d3
. Tan k Far m# 3 include s eigh t

bul k liqui dwast e tank s (300 , 302 , 304 , 306 , 308 , 310 , 312 , an d314 ) an dsupplie s bul k liqui dwast e t o Uni t

4
. Tan k

Far m#3 als o include s a vertical , fixed-roo f

tan k tha t store s No
. 2 fue l oi l (Tan k 390)
. Othe r fue l tank s o n sit e includ e ahorizonta l kerosen e tank , tw o horizonta l diese l fue l tanks , an dahorizonta l gasolin e tank
. Thes e fue l tank s ar e use dt o suppl y fue l t o on sit e compan y vehicle s an dfo r fir e suppressio n syste mpump .

4Tabl e 1 . Wast e Storag e Tank s an d Carbo n Canister s Contro l - Carbo n Capacit y Caniste r Locatio n Numbe r (gallons ) Numbe r Tan k Far m# 1 2 4,93 1 2 Tan k Far m# 1 4 4,93 1 4 Tan k Far m# 1 6 7,20 0 6 Tan k Far m# 1 8 5,28 0 8 Tan k Far m# 1 1 0 12,86 9 1 0 Tan k Far m# 1 2 0 12,86 9 2 0 Tan k Far m# 1 3 0 12,86 9 3 0 Tan k Far m# 1 4 0 12,86 9 4 0 Tan k Far m# 1 5 0 12,86 9 5 0 Tan k Far m# 1 6 0 12,86 9 6 0 Tan k Far m# 3 30 0 30,00 0 30 0 Tan k Far m# 3 30 2 30,00 0 30 2 Tan k Far m# 3 30 4 30,00 0 30 4 Tan k Far m# 3 30 6 30,00 0 30 6 Tan k Far m# 3 30 8 30,00 0 30 8 Tan k Far m# 3 31 0 30,00 0 31 0 Tan k Far m# 3 31 2 10,00 0 31 2 Tan k Far m# 3 31 4 10,00 0 31 4
Tabl e 2 . Othe rStorag e Tank s Locatio n Numbe r Capacit y (gallons ) Materia l Store d Tan k Far m# 3 39 0 30,00 0 No
. 2 Fue l Oi l Sout ho f

Parkin g Lo t Non e 55 0 Kerosen e Sout ho f

Parkin g Lo t Non e 55 0 No
. 2 Fue l Oi l Sout ho f

Parkin g Lo t Non e 55 0 Gasolin e Fir e Pum p Hous e Non e 55 0 No
. 2 Fue l Oi l b . Container s Soli dwaste s ar e als o receive di n containers , including , bu t no t limite dto , drums , totes , cartons , boxes , o r pails
. Drum s an dothe r container s receive do n site , dependin g o n compatibility , mayb e store di n building s 1A , IB , 1C , 2A , 2B , 2C , 3 , 3A , 3B , an d6
.

52 . Incineratio n Unit s Thre e separat e incinerato r system s consis t

o f tw o fixed-hearth , dual-chambere dunit s rate dat 1 6 millio nBtu/h r

eac h(Unit s 2 an d3)
. Unit s 2 an d3 ar e mirro r image s o f

eac h other
. Th e onl y differenc e betwee n th e unit s i s Uni t 2 ha s fou r

baghous e modules , whil e Uni t 3 ha s thre e baghous e modules
. Th e thir dincinerato r (Uni t 4 ) i s arotar y kil nrate da t 5 0 millio nBtu/hr
. Eac huni t include s it s ow n feed , ai r pollutio n control , proces s instrumentatio n an dcontrols , an dcontinuou s emissio n monitorin g systems .
a . Uni t2 an d Uni t3 Unit s 2 an d3 ar e fixed-heart hincinerator s wit hatwo-stag e combustio n process . Se e Figur e 5 fo r

th e Unit s 2 an d3 proces s flow diagram
. (Figure s ar e a t th e en do f

thi s section. ) Ignitio n o f wast e materia l take s plac e i n th e primar y (lower ) combustio n chambe r

a t temperature s i n exces s o f 1,70 0 degree s F
. A secondar y (upper ) combustio n chambe r serve s a s a n "after-burner " fo r proces s gases . Th e secondar y combustio n chambe r temperatur e i s maintaine da t aminimu mtemperatur e o f 1,80 0 degree s F
. Waste s ar e no t injecte dint o th e secondar y combustio n chamber
. Th e thermocoupl e tha t

monitor s temperatur e i n th e lowe r combustio n chambe r i s locate d o n to p o f

th e chambe r

approximatel y 5 fee t fro mth e transition
. Th e thermocoupl e tha t monitor s temperatur e i n th e uppe r combustio n chambe r i s locate do n to p o f th e chambe r

abov e th e transition
. Eac hincinerato r

ha s tw o burners
. Th e burne r i n th e lowe r

chambe r

i s aNort h America n burne r

rate da t 1 2 millio nBtu/hr
. Thi s burne r onl y burn s natura l ga s an di s use dt o maintai n minimu mchambe r temperatures . Liqui do r gaseou s (Uni t

2 only ) waste s ar e injecte dthroug hseparat e fee dnozzles
. Th e burne r i n th e uppe r

chambe r

i s aNort hAmerica n burne r rate da t 6 millio nBtu/h r

use dt o suppl y additiona l hea t t o th e chambe r

whe n necessary . Thi s burne r onl y burn s natura l gas . Th e primar y an dsecondar y chamber s o f Unit s 2 an d3 eac hhav e a n externa l diamete r o f 9 fee t an dar e 17. 5 fee t

long
. Th e interio r

wall s o f

bot hchamber s ar e line dwit h approximatel y 1 0 inche s o f bric k refractor y an dinsulatin g backing
. Th e interna l operatin g diamete r

i s 7 fee t

2 inches
. Th e cross-sectiona l are ao f th e chamber s i s 40. 3 squar e feet
. Combustio n ai r i s controlle dseparatel y i n th e uppe r an dlowe r

chambers
. Se e Tabl e 3 fo r

asummar y o f

Unit s 2 an d3 desig n specifications
. Tabl e 3 . Unit s 2 an d 3 Desig n Specification s Mode l TWI-2000 , Serie s 2 Manufacture r Trad e Wast e Incineratio n Typ e Fixe dHearth , Dua l Chambe r Fee d Solids , Organi c Liquids , Aqueou s Liquids , Sludges , Gase s (Uni t

2 only ) Hea t Releas e Ratin g 1 6 M [MBtu/h r Primar y Chambe r Secondar y Chambe r Externa l Lengt h 17. 5 f t 17. 5 f t
6Tabl e 3 . Unit s 2 an d 3 Desig n Specification s Externa l Diamete r 9 f t 9 ft Interna l Diamete r 7 f t 2 i n 7 f t 2 i n Cross-sectiona l Are a 40. 3 s qf t 40. 3 s qf t Burne r Manf
. Nort hAmerica n Nort hAmerica n Burne r Siz e 1 2 MMBtu/h r 6 MMBtu/h r Burne r Fue l Natura l Ga s Natura l Ga s Liqui dWast e Injector s 0-42 5 gp h Prim e Move r Induce ddraft fan , 15,00 0 acf m@ 400°F , 2 2 inche s wate r colum n Afte r ignitio n o f

wast e materia l unde r controlle dcondition s i n th e lowe r chamber , gase s trave l throug harefractory-line dflu e ga s passag e int o th e uppe r chamber , whic h act s a s a n afterburner
. Turbulenc e i s achieve db y th e tangentia l introductio n o f ai r an dadditiona l fue l i n th e uppe r chamber
. Afte r passin g throug hth e uppe r chamber , th e ho t

ga s strea mtravel s throug h2 8 fee t o f refractory-line dstac k section s befor e reachin g th e star t o f th e ga s scrubbin g system . Th e combine dvolum e o f th e uppe r

an dlowe r

chambers , th e flu e ga s passage , an dth e ho t

crossove r

sectio n i s approximatel y 1,56 7 cubi c feet
. Th e tota l retentio n tim e o f

combustio n gase s withi n th e syste mi s approximatel y 5 seconds
. Th e incinerato r

i s rate da

t 1 6 millio nBtu/h r

an dha s adesig n uni t hea t releas e o f approximatel y 10,00 0 Bt u pe r cubi c foot
. Maximu mga s volum e whe n firin g ahea t releas e o f

1 6 millio nBtu/h r

i s 15,00 0 acf ma

t 40 0 degree s F
. b . Uni t4 Bul k soli dwaste s ar e fe dint o th e Uni t 4 incinerato r

throug heithe r

th e ra mfeede r

o r a scre w auger . Containerize dwaste s ar e fe dint o th e kil nthroug hth e ra mfeede r o r th e auxiliar y ra mfeeder
. Uni t 4 i s supporte db y storage/blen dtank s locate di n Tan k Far m#3
. Rate s o f

waste s fe dfro mth e tan k far mar e controlle da t th e incinerator
. Th e materia l i s transferre dthroug habove-groun dpipeline s fro mth e tan k far mt o th e Uni t 4 system . Uni t 4 incinerato r

ha s atwo-stag e combustio n proces s consistin g o f akil nan d Secondar y Combustio n Chambe r (SCC)
. Se e Figur e 6 fo r th e Uni t

4 proces s flo w diagram
. (Figure s ar e a t th e en do f

thi s section. ) Ignitio n o f wast e materia l take s plac e i n th e primar y kil na t temperature s i n exces s o f 1,50 0 degree s F
. Th e SC C temperatur e i s maintaine dabov e 1,88 0 degree s F
. Hig hBt u liqui dwaste s ca n b e injecte ddirectl y int o th e SCC
. Th e pyromete r tha t monitor s temperatur e i n th e rotar y kil ni s locate dtop-cente r i n th e transitio n sectio n betwee n the rotar y kil nan dth e SCC , approximatel y 2 fee t downstrea mfro mth e exi t o f th e kiln
. Th e thermocoupl e tha t monitor s temperatur e i n th e SC C i s locate do n th e wes t sid e o f th e chambe r

nea r th e SC C exi t

duct
.

7Th e rotar y kil ni s fabricate do f carbo n steel
. I t

ha s approximat e dimension s o f 8 fee t 8 inche s outsid e diamete r b y 3 5 fee t

long
. I t

i s supporte do n aone-degre e slop e b y tw o stee l tire s o r

ridin g rings
. Eac hridin g rin g ride s o n tw o pair s o f stee l trunnion s an dha s a n approximat e outsid e diamete r o f 9 fee t 5 inches
. Th e thicknes s an dfac e widt ho f

th e trunnion s ar e approximatel y 6 inche s an d9 inches , respectively
. Th e kil ni s line dwit happroximatel y 7. 5 inche s o f dense , abrasion-resistant , high-alumin a firebric k

refractory
. Wit hthi s refractor y system , th e kil nha s a n insid e diamete r o f approximatel y 7 feet , alengt ho f approximatel y 3 5 feet , a n integra l cross-sectio n are a o f approximatel y 38 squar e feet , an da n interna l volum e o f approximatel y 1,34 6 cubi c feet
. A l l kil nfeed s ente r

throug hth e uppe r

kil nfac e plat e locate do n th e fee den do f th e kiln
. Th e plat e contain s aprimar y burner , thre e liqui dfee dnozzle s (fo r direc t injectio n o f

liqui dwaste , aqueou s waste , an dhig hBt u liqui dwaste) , a n ai r turbulenc e nozzle , ara mfeeder , an dasurg e vent . Th e primar y burne r

i s equivalen t

t o aNort hAmerica n 'Fue l Directed ' burne r o f 2 5 MMBtu/h r

an dburn s natura l gas . Th e burne r syste mi s supplie dwit happroximatel y 4,00 0 acf mcombustio n ai r a t astati c pressur e o f

2 0 inche s wate r

column
. Th e pilo t fo r th e primar y burne r

burn s natura l gas . Th e fue l syste mfo r th e kil nan dSC C i s controlle db y aFactor y Mutua l approve dburne r managemen t

syste mcomplet e wit h interlock s an dsafet y valves
. Th e SC C i s avertical , cylindrica l chambe r havin g approximat e dimension s o f 1 0 fee t 6 inche s outsid e diamete r b y 7 1 fee t

high
. I t

i s fabricate do f

carbo n stee l an dline d wit ha n inne r

cours e (ho t

face ) o f

approximatel y 6 inche s o f high-alumin arefractor y an da n oute r

cours e o f

approximatel y 2 inche s o f insulatin g refractory
. Wit hthi s installe drefractory , th e SC C ha s a n insid e diamete r o f approximatel y 9 feet
. Th e effectiv e lengt h(ga s retentio n length ) o f th e chambe r

i s approximatel y 4 8 fee t 6 inches
. Consequently , th e SC C ha s across-sectio n are ao f 6 4 squar e fee t

an da n effectiv e volum e o f

approximatel y 3,08 4 cubi c feet
. A t maximu mcombustio n ga s flows , th e combustio n ga s residenc e tim e i s greate r tha n 2 seconds
. Hig hBt u liquid s ca nb e fe ddirectl y int o th e SCC
. Combustio n gase s fro mth e kil nente r th e botto mo f

th e SC C throug harefractory

line dsid e duc t

an dexi t

fro mth e to p o f

th e SC C throug harefractory-line dduc t t o th e temperin g chamber
. Th e floo r o f th e chambe r

i s slope dt o facilitat e the remova l o f as han dsolid s throug hasla g tap . Th e SC C i s equippe dwit hon e burne r mounte do n th e sidewal l o f

th e chambe r

nea r th e bottom
. Th e burne r i s aTran e Therma l Mode l o r equivalent , wit hadesig n hea t releas e o f

approximatel y 3 0 millio nBtu/hr
. Thi s burne r i s supplie dwit hnatura l ga s an dcombustio n air
. A s wit hth e kil nburner , th e S C C burne r

i s supplie dwit hatomizin g ai r an di s equippe dwit haburne r managemen t system . Thi s syste mcontrol s th e ignitio n an dinitiate s a n automati c shutof f whe n ther e i s alos s o f

flame , combustio n ai r supply , fue l pressure , atomizin g ai r pressure , pilo t burner , o r

induced-draft

fan
.

8Th e SC C burne r i s ahigh-intensity , vorte x typ e uni t wit haspi n van e assembly , locate dwithi n th e windbo x t o impar t a n intens e rotar y motio n t o th e combustio n air
. Thi s rotar y motio n an dth e burne r desig n provid e complet e mixin g o f ai r an dfuel , an drecirculatio n o f th e gase s withi n th e combustio n chambe r promote s rapi d combustio n an dhig hhea t intensity
. Se e Tabl e 4 fo r asummar y o f

Uni t 4 desig n specifications
. Tabl e 4 . Uni t4 Desig n Specification s

Mode l PY*RO X Manufacture r Internationa l Wast e Energ y System s Typ e Transportabl e Rotar y Kil n Fee d Solids , Organi c Liquids , Aqueou s Liquids , Sludge s Hea t Ratin g 5 0 MMBtu/h r

Kil n Secondar y Chambe r Externa l Lengt h 3 5 f t 7 1 f t Externa l Diamete r 8 f t 10. 5 f t Interna l Diamete r 7 f t 9 f t Burne r Mfg
. Nort hAmerica n T-Therma l Burne r Siz e 2 5 MMBtu/h r 2 5 MMBtu/h r Burne r Fue l Natura l Ga s Natura l Ga s Liqui dWast e Injector s 0-75 0 gp h Prim e Move r Induce ddraft fan , 53,00 0 acf m

c. Ai rPollutio n Contro l Device s - Uni t2 an d Uni t3 Th e ai r pollutio n contro l syste mconsist s o f aspra y drye r

absorbe r

an dfabri c filte r baghouse
. Th e ai r pollutio n contro l syste mneutralize s acidi c compound s an d remove s particulat e fro mth e exhaus t gas . Tw o subsystems , th e spra y drye r absorbe r an dth e fabri c filter , carr y ou t th e chemica l neutralizatio n an dparticulat e remova l functions , respectively
. A thir dsubsystem , th e lim e system , i s use dt o prepar e an d provid e lim e slurr y t o th e spra y drye r absorbe r

fo r us e i n th e chemica l neutralizatio n process . Th e induce ddraft fa n an dstac k

provid e th e mechanica l energ y require dt o transpor t

th e flu e ga s throug hth e interconnectin g ductwor k t o it s eventua l discharg e poin t t o atmosphere
. Lime System Th e lim e syste mprepare s lim e slurr y fo r us e i n th e chemica l neutralizatio n proces s i n sufficien t suppl y an dconcentratio n t o maintai n continuou s flu e ga s treatmen t

i n th e spra y drye r

absorber
. Th e syste mha s bee n designe dfo r batc h mixin g t o provid e thi s service
. Hydrate dlim e i s store di n astorag e bi n abov e th e lim e preparatio n area . Th e storag e bi n i s size dt o hol denoug hhydrate dlim e t o maintai n severa l day s o f syste moperatio n a

t th e maximu mcombustio n rat e o f th e incinerator
. Lim e i s discharge dthroug hth e conica l storag e bi n bottom
. Th e flo w
9o f th e materia l fro mth e bi n i s aide db y avibratin g "liv e bottom " o r bi n activator
. Avariabl e spee drotar y feede r i s use dt o mete r

th e hydrate dlim e i n th e proportion s require dfo r batc hmixin g lim e slurry
. Th e lim e i s mixe dwit hwate r i natan k

beneat hth e lim e storag e bin
. Th e rotar y feede r spee dan dth e rat e tha t wate r i s adde dt o th e lim e slurr y tan k ar e variabl e s o tha t

th e desire d20 % lim e solid s concentratio n ca n b e achieve di n th e tank
. Th e variabl e fee dadjustment s allo w wate r

an dlim e t o b e adde dt o th e lim e slurr y tan k a t arat e tha t

wil l allo w a batc hmod e o f

mixing
. A n agitato r

i s provide di n th e slurr y tan k t o mi x th e wate r an dlim e an dt o maintai n th e suspensio n o f lim e solids
. Th e mixe dlim e slurr y i s pumpe da

t acontinuou s rat e o f

flo w throug harecirculatio n loo p t o th e atomizer
. Spray DryerAbsorber Slurr y flo w t o th e spra y drye r absorbe r

i s metere db y aflo w contro l valv e t o obtai n th e prope r

fee dconcentratio n t o th e spra y drye r absorbe r

atomizer
. Automati c (o r

manual ) adjustmen t

t o th e flo w i s mad e a s afunctio n o f th e outpu t fro mahydrochlori c aci d(HC1 ) analyze r i n th e ga s duc t

downstrea mo f

th e fabri c filter
. Th e amoun t

o f slurr y metere di s proportiona l t o th e amoun t o f HC 1 monitored
. Th e slurr y passe s throug hastationar y swirl-typ e liqui ddistributo r int o th e atomize r

whee l wher e induce dcentrifuga l forc e fro mth e rapidl y spinnin g whee l discharge s the slurr y throug hth e whee l nozzle s a t hig hvelocity
. Th e desig n o f

th e atomize r

wheel , it s rat e o f

spin , an dth e discharg e velocit y o f th e slurry , creat e aclou do f finel y divide ddroplet s aroun dth e peripher y o f th e atomize r

wheel
. A feedbac k

signa l fro mth e atomize r powe r transmitte r

provide s verificatio n that

wate r flo w t o th e atomize r increase s o r

decrease s i n proportio n t o th e spra y drye r

absorbe r

outle t temperature . Flu e ga s enter s fro mth e botto mo f th e spra y drye r

absorbe r

throug havertical , centrall y locate ddisperser
. Th e disperse r direct s th e flu e ga s throug hth e zon e fille db y th e atomize dslurr y clou dwher e th e flu e ga s an dslurr y mix , an dmos t o f th e absorptio n occur . Th e spra y drye r absorbe r

feature s atwo-poin t produc t discharge
. A portio n o f th e drie dspen t

chemical s an das hsettl e t o th e botto mo f th e chamber
. Thi s materia l i s discharge da t th e bas e o f

th e powde r

discharg e cone . I t the n passe s throug halum p breake r tha t reduce s larg e agglomeration s o f materia l t o amanageabl e size
. Finally , i t i s discharge dthroug harotar y valv e t o th e conveyin g system . Th e remainde r o f th e spen t

chemical s i s carrie dfro mth e modul e entraine di n th e flu e gas . Fabric Filter Ga s exhauste dfro mth e spra y drye r absorbe r

i s distribute db y manifol dduct s t o fou r fabri c filte r

module s a

t Uni t 2 an dthre e fabri c filte r module s a

t Uni t 3
. Withi n eac hfilte r

module , th e ga s i s passe dthroug hTeflon-coate dfiberglas s clot hbags
. Th e ga s passe s fro mth e outsid e t o th e insid e o f th e filte r

bags
. Particulate , entraine di n th e ga s stream , i s mechanicall y deposite do n th e outsid e o f th e filte r

bag s a s th e ga s passe s throug hth e cloth
.
1 0Th e fabri c filte r cleanin g mechanis mutilize s jet s o f ai r t o clea n th e filte r

bags
. Periodically , th e cleanin g sequenc e wil l b e initiated
. Th e sequenc e i s eithe r starte da

t th e en do f

atime dcycl e o r

whe n th e differentia l pressur e acros s th e filte r reache s apredetermine dsetpoin t o f approximatel y 7.0 " w.c . Th e controlle r the n sequence s t o eac hro w o f filte r bag s i n eac hmodule , releasin g aburs t o f ai r opposit e t o th e directio n o f ga s flow
. Th e quickl y release dburs t o f ai r dislodge s dus t cak e o n th e exterio r

o f eac hba g a s i t

travel s fro mth e to p t o th e botto mo f th e bag
. Release dfro mth e bag , th e dus t cak e fall s b y gravit y int o th e hoppe r a t th e botto mo f

th e module
. Th e dus t cleane dfro mth e filte r bag s i s remove da

t th e bas e o f th e hoppe r

throug harotar y valv e fo r discharg e t o th e conveyin g system . Treate db y th e spra y drye r absorbe r

an dfiltere db y th e fabri c filter , th e cleane d flu e ga s exit s th e fabri c filte r module s t o a n outle t manifol dfo r

exhaust
. Induced Draft Fan and

Stack Th e induce ddraft

fa n an dstac k

ar e locate ddownstrea mo f th e fabri c filter. Combustio n gase s ar e draw n throug hth e syste mb y a7 5 h p induce ddraft fan , rate dat 15,00 0 acf ma

t 40 0 degre s Fsaturated , an d22 " wate r colum n pressure . Th e induce ddraf

t fa n provide s th e mechanis mfo r transportin g th e incinerato r flu e ga s throug hth e spra y drye r absorber , fabri c filter, an dal l interconnectin g ducts
. Th e velocit y o f

th e ga s withi n th e ductin g an dtreatmen t device s i s regulate db y th e dampe r

associate dwit hth e fan
. Treate dgase s ar e exhauste dfro mth e induce d draft fa n t o th e atmospher e throug ha90-foo t hig hstack
. Th e stac k diamete r

fo r Unit s 2 an d3 ar e bot h3 9 inche s insid e diameter
. Eac hstac k i s equippe dwit h instrumen t

samplin g port s an dasamplin g platfor mfo r emission s testing
. d . Ai rPollutio n Contro l Device s - Uni t4

a . Tempering Chamber Th e temperin g chambe r i s avertical , cylindrica l uni t designe dt o coo l th e combustio n gase s usin g aserie s o f interna l dual-flui d(wate r an dair ) spra y nozzles
. Th e combustio n gase s ente r th e to p o f

th e chamber , flo w downwar d throug hth e spra y patter n an dexi t fro mth e botto mo f th e chamber
. Th e spra y patter n i s designe dt o eliminat e direc t contac t o f wate r wit hrefractory , an dth e chambe r i s designe dt o maintai n adr y botto munde r al l operatin g conditions
. Tha t is , th e injectio n rat e o f spra y wate r

i s controlled , s o tha t i t i s completel y vaporize dan dcarrie dou t o f th e chambe r

i n th e combustio n gases . Th e temperin g chambe r i s approximatel y 4 9 fee t hig hwit ha n 11-foo t insid e diameter , i s fabricate do f l A inc hnomina l plat e thicknes s carbo n stee l (AST M A36) , an di s line dwit hrefractory
. Th e spra y nozzle s an dextension s are fabricate do f 30 4 S S material
. Th e temperin g chambe r i s size ds o tha t

acombustio n ga s retentio n tim e o f greate r tha n on e secon dwil l b e maintaine da t al l ga s flows
. Becaus e som e molte n
1 1particulat e material s i n th e combustio n gase s ar e coole di n thi s proces s uni t t o belo w thei r

fusio n point , som e solid s ar e generate dan dcollecte di n th e chamber
. Therefore , th e chambe r ha s acon e botto man ddoubl e valve s t o facilitat e th e remova l o f

solids
. Thes e solid s ar e discharge dont o aconveyo r syste mtha t transport s the mt o ahopper
. Spray DryerAbsorber Uni t 4 i s equippe dwit htw o Spra y Drye r Absorber s (SDA ) locate dimmediatel y downstrea mo f

th e Temperin g Chamber
. Eac hSD A uni t i s fabricate do f

3/ 8 inc h carbo n steel
. Th e SDA s operat e i n paralle l to :

• Furthe r

coo l th e combustio n gase s fro m600-80 0 degree s Ft o 300-50 0 degree s F ;
• Neutraliz e an dremov e HC 1 an dothe r acid s fro mthe combustio n gases ; and , • Remov e aportio n o f th e particulat e (flyash ) fro mthes e gases . Th e combine dunit s ar e size dt o remov e mor e tha n 82 0 lbs./hr
. o f chlorin e fro m th e combustio n gases . Eac hSD A i s approximatel y 72 ' hig hb y 10'7 " i n diameter
. Eac huni t

include s ahea dsection , an da60 ° conica l hopper
. Eac hSD A chambe r ha s on e acces s doo r

i n th e uppe r

section
. Eac hhoppe r ha s on e acces s door , a flange dclean-ou t

port , an dadrai n connection
. Th e SD A hea dsectio n consist s o f aflange dinle t

connectio n an daho t ga s inle t

plenum
. Th e dual-flui datomizin g nozzle s includ e stainles s stee l housing s an dstellite dinserts
. Th e nozzle s ar e assemble dt o permi t

fiel dremova l fro mth e piping
. Th e tw o lim e slurr y pipin g header s hav e automati c isolatio n valves
. Combustio n gase s ente r th e to p o f

eac ho f thes e units , flo w downwar dthroug ha centra l duct , an dar e disperse dsymmetricall y fro mthi s duc t int o th e absorbe r chambe r a t avelocit y an ddirectio n tha t assure s optima l contac t wit hth e clou do f atomize dlim e slurr y droplet s introduce dint o th e chambe r b y dual-flui d(lim e slurr y an dair ) nozzles
. Th e gase s the n flo w downwar dthroug heac habsorbe r chambe r an dexi t

throug habotto msid e duct
. A s th e gase s contac t an dpas s throug hth e clou do f atomize dlim e slurry , th e wate r i n th e slurr y evaporates , coolin g th e gases . Simultaneously , th e lim e i n th e slurr y react s wit hth e hydroge n chlorid e i n th e gase s t o produc e calciu msalts
. Som e o f th e resultin g dr y material , consistin g o f

calciu msalts , flyash , an dexces s lime , fall s to th e conica l botto mo f eac hunit
. Th e dr y materia l fro meac huni t i s discharge dt o aconveyo r system , whic htransport s i t

t o adum p traile r

o r equivalen t

typ e system . Fabric Filter Th e fabri c filte r

consist s o f

tw o module s connecte di n parallel
. Eac hmodul e i s divide dint o thre e compartment s connecte di n parallel , whic hcontai n multipl e fabri c filte r

bag s throug hwhic hth e combustio n gase s pas s t o remov e particulates
.
1 2Th e module s provid e a n operatin g air-to-clot hrati o o f approximatel y 4:1
. Th e bag s ar e periodicall y cleane dvi aapuls e ai r jet , whic hcause s th e particulat e matte r t o fal l t o th e botto mhopper s o f eac hmodule
. Fro mther e i t i s discharge d t o aconveyo r

syste mwhic htransport s i t t o adum p traile r

o r equivalen t

typ e system . Eac hfabri c filte r

consist s o f

atrailer-mounte duni t subdivide dint o thre e compartments . Eac hcompartmen t ha s aclea n ai r

plenu man dhousin g sectio n t o contai n approximatel y 30 8 bags
. Eac hba g i s approximatel y 5 inche s i n diamete r b y 5 fee t

long
. Th e baghouse s ar e fabricate dfro m3/16-inc hmil dstee l plate , o f welde dconstruction , ga s tight , an dstiffene dt o withstan dthe maximu moperatin g negativ e pressure . Eac hcompartmen t ha s atub e shee t

tha t support s th e bag s an d provide s fo r

to p bag/cag e removal
. Acces s t o th e clea n ai r plenu mi s vi aabolte d acces s door
. Eac htrailer-mounte duni t contain s th e compresse dai r headers , ga s inle t an doutle t

manifolds , an dth e conveyor . Th e fabri c filte r

i s equippe dwit hahigh-efficiency , pulse-je t cleanin g system . Th e cleanin g syste muse s lo w pressure , approximatel y 40-8 0 psig , an d compresse ddr y ai r

t o dislodg e th e accumulate dparticulate s fro mth e bags
. A soli dstat e programmabl e controlle r accomplishe s th e contro l o f th e ai r flow
. Th e filter unit s ar e designe dt o minimiz e filte r ba g wea r

b y cleanin g o n demand , ye t maintainin g th e desire dpressur e dro p acros s th e fabri c filter. Alternately , a t th e optio n o f

th e operator , th e unit s ca n b e cleane do n atime dcycle , i n amanua l mod e o r

o n th e basi s o f

hig hpressur e drop
. Th e pressur e dro p se t poin t i s adjustable , bu t

normall y i s les s tha n 8 " w.c . Th e bag s ar e designe dfo r 25 " w.c . vacuum , whic hi s greate r tha n th e maximu mnegativ e pressur e th e induce ddraf t fa n ca n develop
. Th e desig n allow s th e bag s t o b e cleane dwhe n th e fabri c filte r i s i n operation
. Fo r

asix-compartmen t

unit , one-sixt ho f

the tota l bags , o r

one thir do f amodule , ca n b e isolated
. Th e remainin g five-sixths o f th e fabri c filter capacit y i s mor e tha n adequat e t o accommodat e th e proces s requirements
. Th e filte r mediu mi s a2 2 oz/s qyd. , wove n fiberglass material , wit ha n acid-resistan t finish
. Bag s includ e sna p ring s fo r eas y an ddust-tigh t

installation
. Th e bag s ar e hel di n plac e b y ba g cage s constructe do f galvanize dstee l wire
. Carbon Injection and Lime Recirculation System Th e carbo n injectio n syste mair-inject s activate dcarbo n int o th e plenu m immediatel y upstrea mo f th e baghouse s an dallow s fo r amor e efficien t

mean s o f controllin g dioxin/fura n an dmercur y emissions
. T o complimen t thi s syste man d t o incorporat e wast e minimization , th e facilit y i s permitte dt o pul l asli p strea mo f th e partiall y reacte dlim e fro mth e exi t o f th e baghous e solid s discharg e syste m an drecirculate/recycl e thi s bac k t o th e Spra y Drye r

Absorber s (SDAs ) t o furthe r ai di n HC 1 remova l an ddioxin/fura n removal
. Th e carbo n injectio n syste mi s controlle db y aPLC , whic hwil l contro l th e inpu t o f activate dcarbo n t o th e baghous e inle t

plenu mt o allo w fro m2 t o 2 0 pound s pe r hou r o f powdere d

1 3activate dcarbo n t o b e ai r injecte dint o thi s plenu man dallo w fo r direc t contac t wit hth e stac k

gase s exitin g th e SDAs
. Th e amoun t

o f carbo n i s dose di n adust-fre e manne r int o alow-pressur e ai r strea mvi apneumati c eduction
. Th e educto r use s ablowe r

fo r th e motiv e air
. Th e carbon/ai r

strea mtravel s throug hpipin g t o th e injectio n nozzl e int o th e ductwork
. Th e carbo n contact s th e ga s strea mexitin g th e SDA s an dallow s fo r th e adsorptio n o f

an y dioxin/furan s an dmercur y tha t migh t b e presen t

i n thi s stream . Adsorptio n continue s a s th e stac k gase s procee dthroug hth e baghouses
. Th e clea n stac k

ga s exit s th e fina l stac k vi ath e induce ddraf t fan , an dth e capture d solid s ar e discharge dfro mth e baghouse s vi ath e scre w conveyin g syste mint o a n enclose ddum p traile r fo r disposa l a

t aSubtitl e C landfill
. I nadditio n t o thi s system , th e facilit y i s permitte dfo r alim e recirculatio n syste m tha t direct s aportio n o f th e spen t

lim e an dcarbo n strea mbac k int o th e SDAs
. Thi s recirculatio n syste mserve s tw o purposes . Th e mai n objectiv e i s t o furthe r ai di n th e neutralizatio n o f HC 1 an dth e adsorptio n o f dioxin/fura n an dmercur y i n th e SDAs
. Th e secon dobjectiv e i s t o minimiz e th e hazardou s wast e tha t wil l b e generate drequirin g disposa l a t aSubtitl e C landfil l b y recyclin g aportio n o f th e partiall y reacte dlime
. Th e spen t

lim e an dcarbo n strea mexitin g th e baghouse s wil l contai n u p to 50 % unreacte dlim e an daportio n o f unadsorbe dactivate dcarbon
. A sli p strea mo f thi s residua l wil l b e take n ou t o f eac hbaghous e syste man ddirecte dbac k t o eac h SDA
. Sinc e th e SDA s an dbaghouse s ar e i n parallel , th e Nort hbaghous e residua l strea mwil l b e directe dt o th e Nort hSD A an dth e Sout hbaghous e residua l strea m wil l b e directe dt o th e Sout hSDA
. Th e residua l wil l b e blow n int o th e SDA s vi a a n injectio n nozzl e tha t wil l b e locate dapproximatel y 2 0 fee t dow n fro mth e ga s inle t duc t o f eac hvessel
. Thi s strea mwil l ad dmor e neutralizin g an dadsorbin g surfac e are aan dfurthe r ai di n th e remova l efficienc y o f thi s vessel
. Th e unreacte dlim e portio n o f thi s strea mwil l ai di n neutralizatio n o f HC1 , an dth e increase dsurfac e are ao f th e tota l residua l strea mwil l ai di n th e adsorptio n o f an y dioxin/fura n compound s presen t i n th e off-gases
. Th e basi s i s providin g mor e surfac e are ai n th e ga s cleanin g trai n t o whic hth e dioxin/fura n compound s ca n adhere , thu s reducin g th e stac k emission s o f

thes e compounds
. Thi s closed

loope dsyste mwil l provid e aconstan t cycl e o f

addin g an dremovin g spen t lim e vi ath e recirculatio n system , so , theoretically , th e compositio n o f th e recirculatio n fee dstoc k

shoul dremai n fairl y constant . Induced Draft Fan and

Stack Th e induce ddraft

fa n draw s combustio n gase s throug hth e syste man ddischarge s the mthroug hth e stack
. I t ha s acarbo n stee l centrifuga l desig n size dt o develo p a pressur e o f

approximatel y 25 " w c a t amaximu mga s flo w o f approximatel y 53,00 0 acf ma

t 40 0 degree s F
. Th e induce ddraft fa n wa s size dt o maintai n a

1 4negativ e pressur e o f V%" w.c . i n the kil nan dgreate r negativ e pressure s throughou t th e remainde r

o f th e system , thereby , preventin g fugitiv e emissions
. Th e induce ddraft

fa n include s a n inle t volum e contro l dampe r t o b e use dt o contro l th e pressur e o f th e kiln
. Th e stac k

diamete r

fo r Uni t 4 i s 4 8 inche s insid e diamete r an di s 10 0 fee t

high
. Uni t

4' s stac k

i s equippe dwit hinstrumen t samplin g port s an dasamplin g platfor mfo r emission s testing
. Figur e 5- 2 provide s detail s o n th e desig n an dsampl e por t location s an dconfiguration s fo r th e stack
. 3 . Othe rTreatmen tUnit s
a . Materia l Processin g Area s Materia l processin g involve s repackagin g o f containerize dsoli dwaste s int o smaller , mor e manageabl e container s fo r incineration
. Som e soli dwaste s ma y b e receive d containin g fre e liquid s tha t ma y b e aqueou s o r

organic
. Durin g materia l processing , fre e liquid s ar e fixe dwit ha n iner t absorben t

t o facilitat e repackaging
. Materia l processin g occur s a

t MP-1 , MP-2 , an dth e La b Pac k Repac k Facilit y i n Buildin g 2B
. Se e Figur e 7 fo r

th e Materia l Processin g flo w diagram
. (Figure s ar e a t th e en do f

thi s section. ) Tabl e 5 . Materia l Processin g Area s Activit y Locatio n Materia l Processin g 1 MP- 1 Materia l Processin g 2 MP- 2 La b Pac k

Repac k Buildin g 2 B Thes e operation s emi t fugitiv e emission s i n a n enclose dbuilding
. Volatil e organi c materia l (VOM ) i s emitte dt o th e atmospher e throug hbuilding/are aexhaus t fans
. b . Bul kFee d Buildin g Bul k soli dwaste s ar e store di n fou r pit s i n th e Bul k

Fee dBuilding
. Solid s store di n thes e pit s ar e incinerate di n Uni t 4
. A carbo n adsorptio n syste mcontrol s volatil e emissions
. Th e buildin g i s equippe dwit hacyclon e an dtw o baghouse s t o contro l particulat e emissions
. Bul k soli dwaste s ar e move dfro mth e pit s t o Uni t 4 b y a clamshel l throug ha n enclose dgallery
. Se e Figur e 8 fo r th e Bul k

Fee dBuildin g proces s flo w diagram
. (Figure s ar e a t th e en do f

thi s section. )

c . Glov e Bo x Buildin g Waste s ma y als o b e processe di n th e Glov e Bo x Building , whic hi s locate dnea r Uni t 3 an dcontain s tw o separat e glov e bo x units
. Material s receive di n drums , la b packs , cylinders , o r

smal l container s tha t ar e reactiv e o r

odiferou s ar e opene di n orde r t o b e repacke dan dre-close dinsid e on e o f th e tw o glov e boxes
. Onl y on e glov e bo x i s i n 1 5us e a t atime , dependin g o n th e siz e o f th e containe r

t o b e processed
. A flexibl e connectio n duc t

i s connecte dt o th e glov e bo x i n operation
. Thi s duc t vent s al l emission s fro mth e materia l i n th e glov e bo x directl y t o incinerato r Uni t 3
. Th e draft o f th e syste minduce ddraft fa n provide s negativ e pressur e o f evacuatio n o f

th e glov e bo x i n use . Whe n handlin g ope n container s i n th e glov e box , al l equipmen t i s use db y th e operato r

fro moutsid e th e glov e bo x b y eithe r automatio n o r

glove s attache dt o th e glov e box
. d . Dru m Crushe r Drum s receive dtha t ar e unsuitabl e fo r

reus e ar e crushe da t th e Dru mCrushe r

afte r bein g emptied
. Thes e empt y drum s ma y contai n residua l organi c material
. Crushe d drum s ar e transporte doff-sit e fo r disposal
. Fugitiv e emission s o f VO M ar e emitte dt o th e atmosphere
. Se e Figur e 9 fo r th e Dru mCrushe r

proces s flo w diagram
. (Figure s ar e a t th e en do f

thi s section. ) 4 . Ancillar y Processe s Ther e i s on e 10. 6 MMBtu/h r natura l ga s boile r

locate dnort ho f

Tan k Far m#1
. Anothe r 12.5 5 MMBtu/h r

natura l ga s boile r

i s proposed
. Thes e boiler s ar e use dt o generat e hea t an dstea mfo r

on-sit e uses . Se e Figur e 1 0 fo r th e boile r

proces s flo w diagram
. (Figure s ar e a t th e en do f

thi s section. ) Ther e i s als o aportabl e 2. 5 MMBtu/h r boile r an dtw o emergenc y generators , eac hrate dat les s tha n 11 2 kW
. Ther e ar e n o emissio n contro l device s associate dwit hthes e units
. C . Genera l Ai rEmissio n Informatio n Emissio n unit s a

t th e Veoli aSauge t

facilit y emi t

CO , NOx , SOx , particulat e matter , semi

volatil e metals , low-volatil e metals , lead , HAPs , an dVOM
. Contro l device s an dstandar d wor k practice s ar e use dt o contro l emission s t o th e atmosphere
. Th e Veoli aSauge t

facilit y i s locate di n anonattainmen t are afo r

th e 8-hou r

ozon e an dPM2 . 5 nationa l ambien t

ai r qualit y standards
. Th e facilit y i s amajo r sourc e o f

HAPs , emittin g greate r tha n 1 0 ton s pe r

yea r o f HCl
. Th e facility' s potentia l t o emi t i s les s tha n 10 0 ton s pe r yea r fo r VO M an dNOx , an dles s tha n 25 0 ton s pe r yea r fo r al l othe r

regulate dpollutants
.

1 6

## REGULATOR Y APPLICABILIT Y AN D PERMI T CONDITION S A . Facility-wid e Requirement s an d Permi tShiel d Reques t[4 0 CF R71.6(f) ] Th e followin g requirement s appl y t o th e plan t operation s a s awhol e o r t o certai n categorie s o f equipmen t

throughou t

th e plant
. A listin g o f an y non-applicabl e requirement s an dth e reason s fo r

th e non-applicabilit y ar e provide di n Appendi x B
. Veoli arequest s apermi t shiel dsuc htha t

complianc e wit hth e condition s o f th e issue dPar t

7 1 permi t

shal l b e deeme d i ncomplianc e wit hth e applicabl e an dnon-applicabl e requirement s containe di n th e Titl e V renewa l applicatio n an daddendum
. 1 . Fugitiv e Particulat e Matte r[35 IA C 212.301 ] N o perso n shal l caus e o r allo w th e emissio n o f fugitiv e particulat e matte r fro man y process , includin g an y materia l handlin g o r storag e activit y tha t

i s visibl e b y a n observe r lookin g generall y towar dth e zenit ha t apoin t beyon dth e propert y lin e o f th e source . 2 . Ope n Burnin g Prohibition s [3 5 IA C 237.102 ] N o perso n shal l caus e o r allo w ope n burning , excep t a s provide db y permi t receive di n accordanc e wit hSectio n 237.20 1 o f th e regulations
. I n addition , n o perso n shal l caus e o r allo w th e burnin g o f an y refus e i n an y chambe r o r apparatus , unles s suc hchambe r o r apparatu s i s designe dfo r th e purpos e o f

disposin g o f

th e clas s o f

refus e bein g burned
. Landscap e wast e ma y b e exempte dunde r certai n condition s liste di n 3 5 IA C 237.12 0 (c)
. 3 . Organi c Emission s fro m Pump s an d Compressor s [3 5 IA C 219.142 ] N o perso n shal l caus e o r allo w th e discharg e o f mor e tha n 32. 8 m l ( 2 c u in ) o f volatil e organi c liqui d(VOL ) wit hvapo r pressur e o f

greate r tha n 2. 5 psi aa

t 7 0 degree s Fint o th e atmospher e fro man y pum p o r compresso r

i n an y 1 5 minut e perio da t standar d conditions
. 4 . NESHA Pfro m Off-sit e Wast e an d Recover y Operations : Equipmen tLeak s [4 0 C F R63.691(b)(1) ; 40 CF R6 1 Subpar tV ] Th e facilit y shal l compl y wit hth e lea k detectio n an drepai r standard s containe di n 4 0 C F R61.242- 1 throug h4 0 CF R61.242-1 1 fo r pumps , compressors , pressur e relie f devices , samplin g connectio n systems , open-ende dvalve s o r lines , valves , connectors , surg e contro l vessels , bottom s receivers , an dcontro l device s o r systems . 5 . Preventio n o f

Significan tDeterioratio n an d Nonattainmen tNe w Sourc e Revie w Th e facilit y i s locate di n St
. Clai r County , amargina l non-attainmen t are afo r

th e 8-h r ozon e an dth e PM -2. 5 nationa l ambien t ai r qualit y standard s (NAAQS)
. Th e are ai s designate dattainmen t o r unclassifiabl e fo r

al l othe r

regulate dpollutants
. Th e facilit y i s a majo r sourc e o f

hazardou s ai r

pollutant s wit hpotentia l emission s a s follows :

1 7POLLUTAN T P T E (tons/yr ) P M 1 0 

### 12.5 5 so 2 

### 66.1 9 N O x 

### 74.1 1 V O M (OZONE ) 

### 15.63 C O 

### 30.8 5 LEA D 

### 0.096 8 P M 

### 13.9 3 HAP S 

### 21.4 1 ARSENI C 

### <0.1 0 BENZEN E 

### <0.4 0 BERYLLIU M 

### <0.0 5 LEA D 

### <0.1 0 MERCUR Y 

### 0.05 5 Th e curren t

facility' s PT Ei s asummatio n o f th e potentia l t o emi t

o f eac hemissio n unit
. B . Incinerators : Uni t2 , Uni t3 , an d Uni t4 Emissio n Standar d Requirement s Th e regulation s applicabl e t o th e incinerator s ar e liste dbelow
. A listin g o f an y non applicabl e requirement s an dth e reason s fo r th e non-applicabilit y ar e provide di n Appendi x B
. 1 . Visibl e Emission s
a . Visibl e Emission s Limitation s [3 5 IA C 212.123(a) ] Th e emissio n o f

smok e o r

othe r particulat e matter , wit ha n opacit y greate r tha n 3 0 percent , int o th e atmospher e fro man y emissio n sourc e shal l no t b e cause do r

allowed , excep t a s allowe db y 3 5 IA C 212.123(b ) an d212.124
. b . Fugitiv e Particulat e Matte r[3 5 IA C 212.30 1 an d 212.314 ] Th e facilit y shal l no t caus e o r

allo w th e emissio n o f fugitiv e particulat e matte r fro m an y process , includin g an y materia l handlin g o r storag e activity , tha t i s visibl e b y a n observe r

lookin g generall y overhea da t apoin t beyon dth e propert y lin e o f th e sourc e unles s th e win dspee di s greate r tha n 40. 2 kilometer s pe r hou r (2 5 mile s pe r

hour. ) excep t a s describe di n 3 5 IA C 212.314
.

1 82 . Sulfu rDioxid e Emission s
a . Sulfu rDioxid e Annua l Emissio n Limitatio n Tota l sulfu r

dioxid e emission s fro mth e facilit y shal l no t excee d7. 7 ton s pe r

yea r fo r unit s 2 an d3 an d50.7 6 ton s pe r yea r fo r Uni t 4
. [Constructio n permit s #8710002 4 an d#88010001 ] 3 . Carbo n Monoxid e Emission s
a . NESHA Pfo rHazardou s Wast e Combustor s [4 0 CF R63.1219(a)(5) ] Emission s o f

carbo n monoxid e shal l b e les s tha n o r equa l t o 10 0 part s pe r millio nb y volume , ove r

a n hourl y rollin g averag e (monitore dcontinuousl y wit hacontinuou s emission s monitorin g system) , dr y basi s an dcorrecte dt o 7 % oxygen . I f th e facilit y elect s t o compl y wit hthi s carbo n monoxid e standar drathe r tha n th e hydrocarbo n standar dunde r

paragrap h(a)(5)(ii ) o f thi s section , i t

mus t als o documen t

that , durin g th e destructio n an dremova l efficienc y (DRE ) tes t run s o r thei r equivalen t

a s provide d b y 4 0 CF R63.1206(b)(7) , hydrocarbon s d o no t excee d1 0 part s pe r millio nb y volum e durin g thos e runs , ove r a n hourl y rollin g averag e (monitore dcontinuousl y wit hacontinuou s emission s monitorin g system) , dr y basis , correcte dt o 7 % oxygen , an dreporte da s propane . b . Carbo n Monoxid e Limitation s fo rIncinerator s [3 5 IA C 216.141 ] Carbo n monoxid e emission s fro meac hincinerato r shal l no t

excee d50 0 part s pe r millio n(ppm ) correcte dt o 50 % exces s air
. [Constructio n permit s #83120053 , #8710002 4 an d#88010001 ]

c . Carbo n Monoxid e Annua l Emissio n Limitatio n Tota l carbo n monoxid e emission s fro mth e facilit y shal l no t excee d6. 6 ton s pe r

yea r fo r Unit s 2 an d3 an d13.8 6 ton s pe r yea r fo r Uni t 4
. [Constructio n permit s #8710002 4 an d#88010001 ] 4 . Particulat e Matte rEmission s
a . Particulat e Matte rLimitation s fo rIncinerator s [3 5 IA C 212.181(b) ] Th e emissio n o f

particulat e matte r

int o th e atmospher e fro man y incinerato r burnin g mor e tha n 0.90 7 megagra mpe r hou r (Mg/hr ; 2,00 0 poun dpe r hou r (lb/hr) ) bu t

les s tha n 27. 2 Mg/h r

(60,00 0 lb/hr ) o f

refus e shal l b e limite dt o 18 3 milligram s pe r standar dcubi c mete r

(mg/scm ; 0.0 8 grai n pe r standar dcubi c foo t

(gr/scf) ) o f

effluen t gase s correcte dt o 12 % carbo n dioxide
. [Constructio n permi t #83120053 ]

1 9b . NESHA Pfo rHazardou s Wast e Combustor s [4 0 CF R63.1219(a)(7) ] Emission s o f

particulat e matte r

fro mth e facilit y shal l b e limite dt o 0.01 3 grai n pe r standar dcubi c foo t

(gr/scf) , correcte dt o 7 % oxygen .
c . Particulat e Matte rAnnua l Emissio n Limitatio n Tota l suspende dparticulat e matte r emission s fro mth e facilit y shal l no t excee d15. 0 ton s pe r

yea r fo r Unit s 2 an d3 an d16.9 2 ton s pe r yea r fo r Uni t 4
. [Constructio n permit s #8710002 4 an d#88010001 ] 5 . Volatil e Organi c Materia l Emission s
a . Us e o f

Organi c Materia l [3 5 IA C 219.30 1 an d 219.302 ] Th e facilit y shal l no t caus e o r

allo w th e discharg e o f mor e tha n 3. 6 kg/h r

( 8 lbs/hr ) o f organi c materia l int o th e atmospher e fro man y emissio n unit , excep t that , i f n o odo r nuisanc e exists , thi s limitatio n shal l appl y onl y t o photochemicall y reactiv e material
. Alternatively , th e facilit y ma y us e acontro l devic e t o reduc e suc hemission s eithe r t o 1 0 pp mequivalen t

methan e (molecula r weigh t 16 ) o r less , o r t o conver t

85 % o f

th e hydrocarbon s t o carbo n dioxid e an dwater . b . Volatil e Organi c Materia l Annua l Emissio n Limitatio n Volatil e organi c materia l emission s fro mth e facilit y shal l no t excee d0. 9 ton s pe r yea r fo r Unit s 2 an d3 an d3. 1 ton s pe r yea r fo r Uni t 4
. [Constructio n permit s #8710002 4 an d#88010001 ] 6 . Nitroge n Oxid e Emission s
a . Nitroge n Oxid e Annua l Emissio n Limitatio n Tota l nitroge n oxid e emission s fro mth e facilit y shal l no t excee d4. 0 ton s pe r

yea r fo r Unit s 2 an d3 an d61. 6 ton s pe r yea r fo r Uni t 4
. [Constructio n permit s #8710002 4 an d #88010001 ] 7 . Hazardou s Ai rPollutan tEmission s
a . NESHA Pfo rHazardou s Wast e Combustor s - Dioxi n an d Fura n Emissio n Limitation s [4

0 CF R63.1219(a)(1) ] Th e emissio n rat e o f dioxi n an dfuran s fro mth e facilit y shal l no t excee d0.2 0 n g TEQ/dscm , correcte dt o 7 % oxygen .

2 0b . NESHA Pfo rHazardou s Wast e Combustor s - Mercur y Emissio n Limitation s [4 0 CF R63.1219(a)(2) ] Th e emissio n rat e o f mercur y fro mth e facilit y shal l no t excee d13 0 ug/dscm , correcte dt o 7 % oxygen .
c . NESHA Pfo rHazardou s Wast e Combustor s - Semi-volatil e Meta l Emissio n Limitation s [4

0 CF R63.1219(a)(3) ] Th e emissio n rat e o f cadmiu man dlea dfro mth e facilit y shal l no t excee d23 0 Lig /dscm , combine demissions , correcte dt o 7 % oxygen . d . NESHA Pfo rHazardou s Wast e Combustor s - Lo w Volatil e Meta l Emissio n Limitation s [4

0 CF R63.1219(a)(4) ] Th e emissio n rat e o f arsenic , beryllium , an dchromiu mfro mth e facilit y shal l no t excee d9 2 jag/dscm , combine demissions , correcte dt o 7 % oxygen .
e . NESHA Pfo rBenzen e Wast e Operation s [4 0 CF R61.348(a)(l)(iii) ] Th e combustio n unit s shal l b e designed , installed , operated , an dmaintaine dsuc htha t benzen e i n th e wast e strea mi s destroye db y incineratin g th e waste . Th e combustio n unit s mus t

achiev e adestructio n efficienc y o f 99 % o r greate r fo r benzene
. f . NESHA Pfro m Off-sit e Wast e an d Recover y Operation s [4 0 CF R 63.689(c)(2) ] A l l joint s o r

seam s betwee n th e pip e section s o f an y transfe r

syste mtha t

consist s o f continuou s hardpipin g shal l b e permanentl y o r semi-permanentl y seale d(e.g. , a welde djoin t

betwee n tw o section s o f meta l pip e o r

abolte dan dgaskete dflange)
. 8 . Hydroge n Chlorid e Emission s
a . NESHA Pfo rHazardou s Wast e Combustor s - Hydroge n Chlorid e Emissio n Limitation s [4

0 CF R63.1219(a)(6) ] Th e hydroge n chlorid e an dchlorin e ga s (tota l chlorine ) emission s fro mth e facilit y shal l no t

excee d3 2 pp mb y volume , combine demissions , expresse da s achlorid e (Cl~ ) equivalent , dr y basi s an dcorrecte dt o 7 % oxygen . b . Hydroge n Chlorid e Emissio n Limitatio n Hydroge n chlorid e emission s fro mincinerator s 2 an d3 i n exces s o f 4. 0 pound s pe r hou r o r th e contro l device s shal l demonstrat e aminimu mHC l remova l efficienc y o f 99%
. [Constructio n permit s 8312005 3 an d87100024 ]

2 19 . Destructio n an d Remova l Efficienc y (DRE ) Requiremen t
a . NESHA Pfo rHazardou s Wast e Combustor s - DR E Standar d [4 0 CF R 63.1219(c)(1) ] Eac hHW C uni t

mus t achiev e a99.99 % DRE
. Excep t a s provide di n paragrap h(c)(2 ) o f thi s section , yo u mus t achiev e aDR E o f 99.99% > fo r

eac hprincipl e organi c hazardou s constituen t (POHC ) designate dunde r paragrap h(c)(3 ) o f

4 0 CF R63.1219
. Th e DR Efo r

eac hPOH C wil l b e calculate dusin g th e followin g equation :

D R E= [ 1 - (Wou

t / ) ] x 100 % Where : W i n=mas s feedrat e o f on e POH C i n awast e feedstream ; an d W 0 u t

=mas s emissio n rat e o f th e sam e POH C presen t i n exhaus t

emission s prio r t o releas e t o th e atmosphere
.
Th e emissio n limit s i n thi s rul e ar e presente dwit htw o significan t figures
. Th e intermediat e calculation s mus t b e performe dusin g a t leas t thre e significan t

figures ; however , th e resultan t emissio n level s ma y b e rounde dt o tw o significan t figure s t o documen t

compliance
. b . NESHA Pfo rHazardou s Wast e Combustor s - DR E Standar d [4 0 CF R 63.1219(c)(2) ] I f th e facilit y burn s th e dioxin-liste dhazardou s waste s F020 , F021 , F022 , F023 , F026 , o r F02 7 (se e § 261.3 1 o f thi s chapter) , i t

mus t achiev e aDR Eo f

99.9999 % fo r

eac h POH C tha t

i t designate s unde r

4 0 CF R63.1219(c)(3)
. Th e facilit y mus t demonstrat e thi s DR E performanc e o n POHC s tha t ar e mor e difficul t

t o incinerat e tha n tetra- , penta- , an dhexachlorodibenzo

- p -dioxin s an ddibenzofurans
. Th e equatio n i n 4 0 C F R63.1219(c)(1 ) mus t b e use dt o calculat e DR Efo r eac hPOHC
. I n addition , th e facilit y mus t

notif y th e Administrato r o f it s inten t

t o incinerat e hazardou s waste s F020 , F021 , F022 , F023 , F026 , o r F027
.
c . NESHA Pfo rHazardou s Wast e Combustor s - DR E Standar d [4 0 CF R 63.1219(c)(3) ]

• Eac hPOH C i n th e wast e fee dtha t th e facilit y specifie s unde r sectio n 63.1219(c)(3)(h ) mus t b e treate dt o th e exten t require db y section s 63.1219(c)(1 ) an d(c)(2)
. • On e o r

mor e POHC s tha t

ar e representativ e o f th e mos t

difficul t

t o destro y organi c compound s i n th e facility' s hazardou s wast e feedstrea mmus t b e specified
. Thi s specificatio n mus t b e base do n th e degre e o f difficult y o f incineratio n o f

th e organi c constituent s i n th e hazardou s wast e an do n thei r

2 2concentratio n o r mas s i n th e hazardou s wast e feed , considerin g th e result s o f hazardou s wast e analyse s o r othe r dat aan dinformation
. 

# • C . Incinerators : Uni t2 , Uni t3 , an d Uni t4 Wor k Practic e an d Operationa l Requirement s 1 . Operatin g Paramete rLimit s

a . NESHA Pfo rHazardou s Wast e Combustors[4 0 CF R63.1206(a) , (b ) an d 63.1209)0

) throug h (p) ] Unit s 2 , 3 , an d4 mus t b e operate di n accordanc e wit hth e operatin g paramete r limit s (OPLs ) specifie di n th e mos t recen t

Notificatio n o f

Complianc e (NOC)
. Th e operatin g parameter s ar e liste dbelow
. A cop y o f th e mos t

recen t NO C wit hth e curren t limit s i s provide di n Appendi x E
. Operatin g Parameter s Regulator y Citatio n Emissio n Standar d Minimu mprimar y combustio n chambe r temperature 63.1209G)(l),(k)(2 ) DRE , Dioxin/Fura n Minimu msecondary combustio n chambe r temperature 63.1209(j)(l),(k)(2 ) DRE , Dioxin/Fura n Maximu mflu e ga s flowrat e o r productio n rate 63.1209(j)(2)) , (k)(3) , (m)(2) , (n)(5) , (o)(2 ) DRE , Dioxin/Furan , P M , SVM , LVM , HCL/C1 2 Maximu mhazardou s waste pumpabl e feedrat e fo r

eac hfee d locatio n (63.1209©(3) , (k)(4) ) DRE , Dioxin/Fura n
Maximu mhazardou s waste tota l feedrat e fo r

eac hfee dlocatio n (63.1209(j)(3),(k)(4) ) DRE , Dioxin/Fura n Operatio n o f

waste firin g syste m fo r eac hlocatio n wher e waste i s fe dt o th e incinerato r (63.1209(j)(4 ) D R E
Maximu mtemperature o f th e ga s a t th e inle t

t o dr y contro l devic e (63.1209(k)(l)),(n)(l) ) Dioxin/Furan , SVM , L V M Minimu mcarbo n injectio n rat e (63.1209(k)(6)(i) ) Dioxin/Furan , Mercur y Minimu mcarrie r

flui d(ga s o r liquid ) flowrat e o r

pressure dro p (63.1209(k)(6)(ii) ) Dioxin/Furan , Mercur y Th e bran d(i.e. , manufacturer ) an dtyp e o f

carbo n use ddurin g th e comprehensiv e performanc e tes t (63.1209(k)(6)(iii) ) Dioxin/Furan , Mercur y

Maximu mtota l feedrate o f mercur y (63.1209(l)(l)(i) ) Mercur y Maximu mas hfeedrat e (63.1209(m)(3) ) P M Maximu mtota l feedrate o f semivolatil e metal s (63.1209(n)(2)(ii) ) S V M Maximu mtota l feedrat e o f lo w volatil e metal s (63.1209(n)(2)(ii) ) L V M Feedrat e limit s fo r

lo w volatil e metal s i n pumpabl e feedstream s (63.1209(n)(2)(vii) ) L V M

2 3Operatin g Parameter s Regulator y Citatio n Emissio n Standar d Feedrat e o f

tota l chlorin e an d chlorid e i n al l feedstream s (63.1209(n)(4),(o)(l) ) SVM , LVM , HCL/C1 2 Minimu msorben t

feedrat e (63.120 9 (o)(4)(i) ) HCL/C1 2 Minimu mcarrie r

flui dflowrat e o r nozzl e pressur e dro p fo r th e spra y dr y adsorbe r (63.1209(o)(4)(ii) ) HCL/Cl j
Th e bran d(i.e. , manufacturer ) an dtyp e o f

sorben t use ddurin g th e comprehensiv e performanc e tes t (63.1209(o)(4)(iii)(A) ) HCL/C1 2

Maximu mcombustio n chambe r pressur e (63.1209(p ) Combustio n Syste m Leak s Th e emissio n standard s an doperatin g requirement s 4 0 CF R6 3 Subpar t EE Eappl y a

t al l time s except :

• Durin g period s o f startup , shutdown , an dmalfunction ;
• Whe n hazardou s wast e i s no t i n th e combustio n chambe r (i.e. , th e hazardou s wast e fee dt o th e combusto r ha s bee n cu t

of f fo r aperio do f

tim e no t

les s tha n th e hazardou s wast e residenc e time ) an dth e facilit y ha s documente di n th e operatin g recor dcomplianc e wit hal l otherwis e applicabl e requirement s an d standard s promulgate dunde r authorit y o f

section s 11 2 (e.g. , 4 0 CFR
. par t 63 , subpart s LLL , DDDDD , an dNNNNN ) o r 12 9 o f th e Clea n Ai r

Ac t i n lie u o f th e emissio n standard s unde r 4 0 CF R63.1203 , 63.1204 , 63.1205 , 63.1215 , 63.1216 , 63.1217 , 63.1218 , 63.1219 , 63.1220 , an d63.1221 ; th e monitorin g an dcomplianc e standard s o f 4 0 CF R63.120 6 throug h63.1209 , excep t th e mode s o f

operatio n requirement s o f 4 0 CF R63.1209(q) ; an dth e notification , reporting , an drecordkeepin g requirement s o f 4 0 CF R63.121 0 throug h 63.1212 ;
• Durin g performanc e test s unde r approve dtes t

plan s accordin g t o 4 0 C F R63.1207(e) , (f) , an d(g) ; an d

• I f plan s t o chang e (a s define di n 4 0 CF R63.1206(b)(5)(iii) ) th e design , operation , o r

maintenanc e practice s o f th e unit s i n amanne r tha t ma y adversel y affec t

complianc e wit han y emissio n standar dtha t i s no t monitore d wit haCEM S ar e developed , the n hazardou s wast e mus t no t b e burne dfo r mor e tha n atota l o f 72 0 hour s (renewabl e a t th e discretio n o f

th e Administrator ) an donl y fo r th e purpose s o f

pretestin g o r

comprehensiv e performanc e testing
. Pretestin g i s define da t 4 0 CF R63.1207(h)(2)(i ) an d(ii)
. However , th e facilit y ma y petitio n th e Administrato r t o obtai n writte n approva l t o bur n hazardou s wast e i n th e interi mprio r t o submittin g a Notificatio n o f

Complianc e fo r

purpose s othe r

tha n testin g o r

pretesting
. Operatin g requirement s mus t b e specified , includin g limit s o n operatin g parameter s tha t

hav e bee n determine dt o ensur e complianc e wit hth e emissio n standard s o f

thi s permi t

base do n availabl e information
. Th e Administrato r wil l review , modif y a s necessary , an dapprov e i f warrante dth e interi m

2 4operatin g requirements
. A notificatio n mus t b e submitte dt o th e Administrato r

a t leas t 6 0 day s prio r

t o an y chang e describe dabove
. b . NESHA Pfo rHazardou s Wast e Combustor s [4 0 CF R63.1206(c)(1 ) an d 63.1211(c) ] Th e facilit y operatin g recor dmus t includ e aDocumentatio n o f Complianc e (DOC ) tha t identifie s th e applicabl e emissio n standard s unde r thi s subpar t

an dth e limit s o n th e operatin g parameter s unde r 4 0 CF R63.120 9 tha t wil l ensur e complianc e wit h thos e emissio n standards
. Th e DO C mus t b e update dwit han y change s t o th e OPL s o r affecte dsource s an dbecome s th e complianc e documen t unti l th e NO C i s submitted
. Veoli awil l operat e i n accordanc e wit hth e DO C and/o r th e mos t

curren t NOC
. (Appendi x E. )

c . NESHA Pfo rHazardou s Wast e Combustor s [4 0 CF R63.1206(c)(2 ) an d 63.6(e)(3) ]

• Th e facilit y mus t develo p awritte n startup , shutdown , an dmalfunctio n pla n (SSMP ) tha t

describes , i n detail , procedure s fo r operatin g an dmaintainin g th e sourc e durin g period s o f startup , shutdown , an dmalfunction ; an daprogra m o f correctiv e actio n fo r malfunctionin g process , ai r pollutio n control , an d monitorin g equipmen t use dt o compl y wit hth e relevan t standards
. Th e SSM P i s provide di n Appendi x G o f thi s document
. • Th e facilit y mus t maintai n acurren t

SSM Pan dmus t

mak e th e pla n availabl e upo n reques t

fo r inspectio n an dcopyin g b y th e Administrator
. I n addition , i f th e SSM Pi s subsequentl y revise da s provide di n 4 0 CF R63.6(e)(3)(viii) , th e facilit y mus t

maintai n eac hpreviou s (i.e. , superseded ) versio n o f th e SSMP , an dmus t

mak e eac hpreviou s versio n availabl e fo r inspectio n an dcopyin g fo r aperio do f

5 year s afte r

revisio n o f

th e plan
. I f

at an y tim e afte r

adoptio n o f a nSSM Pa n affecte dsourc e cease s operatio n o r i s otherwis e n o longe r subjec t t o th e provision s o f

thi s part , th e facilit y mus t retai n acop y o f

th e mos t

recen t pla n fo r

5 years . Al l retaine dplan s mus t b e availabl e fo r

inspectio n an d copyin g upo n request . • Th e content s o f th e SSM Pmus t

addres s th e requirement s i n 4 0 CF R 63.1206(c)(2 ) an d4 0 CF R63.6(e)(3)
. • Th e SSM Pan drevision s mus t b e submitte dt o th e Administrato r fo r revie w an dapproval
. d . NESHA Pfo rHazardou s Wast e Combustor s [4 0 CF R63.1206(c)(3 ) an d 35 IA C 201.149 ] Th e facilit y mus t

operat e th e hazardou s wast e combustor s wit hafunctionin g automati c wast e fue l cutof f (AWFCO ) syste mtha t immediatel y an dautomaticall y cut s of f th e hazardou s wast e fee dwhen :

2 5• An y o f th e followin g ar e exceeded : Operatin g paramete r limit s specifie dunde r 4 0 C F R63.1209 ; a n emissio n standar dmonitore db y aCEMS ; an dth e allowabl e combustio n chambe r

pressure ;
• Th e spa n valu e o f an y CM S detector , excep t aCEMS , i s me t

o r exceeded ;
• Upo n malfunctio n o f aCM S monitorin g a n OP Lspecifie dunde r 4 0 CF R63.120 9 o r a n emissio n level ; o r
• An y componen t

o f th e AWFC O syste mfails
. Th e AWFC O syste mmus t addres s th e requirement s i n 4 0 CF R63.1206(c)(3 ) an d constructio n permit s #83120053 , #8710002 4 an d#88010001
. Th e continue doperatio n o f a n emissio n sourc e durin g malfunctio n o r breakdow n o f th e emissio n sourc e o r relate dai r

pollutio n contro l equipmen t shal l no t

b e allowe di f suc hoperatio n woul dcaus e aviolatio n o f th e standard s o r

limitation s se t

fort hi n I L Titl e 35 , Subchapte r

c : Emissio n Standard s an dLimitation s fo r Stationar y Sources
. Violatio n o f

th e standard s o r

limitation s se t

fort hi n I L Titl e 35 , Subchapte r c : Emissio n Standard s an dLimitation s fo r Stationar y Source s shal l no t b e allowe d durin g startup . Th e AWFC O pla n i s provide di n Appendi x H o f thi s document
.
e . NESHA Pfo rHazardou s Wast e Combustor s [4 0 CF R63.1206(c)(4) ]

• Th e facilit y mus t develo p an dmaintai n a n Emergenc y Safet y Ven t (ESV ) operatin g plan , compl y wit hth e operatin g plan , an dkee p th e pla n i n th e operatin g record
. • Th e ES V operatin g pla n content s mus t addres s th e requirement s i n 4 0 CF R 63.1206(c)(4)
. Th e ES V operatin g pla n i s provide di n Appendi x I o f thi s document
. f . NESHA Pfo rHazardou s Wast e Combustor s [4 0 CF R63.1206(c)(5) ] Combustio n syste mleak s o f hazardou s ai r

pollutant s mus t

b e controlle db y maintainin g th e maximu mcombustio n zon e pressur e lowe r tha n ambien t

pressur e usin g a n instantaneou s monitor
. g . NESHA Pfo rHazardou s Wast e Combustor s [4 0 CF R63.1206(c)(6) ] Trainin g program s mus t b e establishe dfo r

al l categorie s o f

personne l whos e activitie s ma y reasonabl y b e expecte dt o directl y affec t emission s o f

hazardou s ai r

pollutant s fro mth e source . Eac htrainin g progra mshal l b e o f atechnica l leve l commensurat e wit hth e person' s jo b dutie s specifie di n th e trainin g manual
. Eac hcommensurat e trainin g progra mshal l requir e a n examinatio n t o b e administere db y th e instructo r at th e en do f

th e trainin g course . Passin g o f thi s tes t

shal l b e deeme dth e "certification " fo r personnel , excep t

that , fo r

contro l roo moperators , th e trainin g an dcertificatio n progra mshal l b e a s specifie dbelow
.

2 6Acertifie dcontro l roo moperato r mus t b e o n dut y a

t th e sit e a

t al l time s th e sourc e i s i noperation
. Hazardou s wast e incinerato r contro l roo moperator s must :

• B e traine dan dcertifie dunde r asite-specific , source-develope dan dimplemente d progra mtha t

meet s th e requirement s o f sectio n 2.1(C)(10)(d);o r
• B e traine dunde r

th e requirement s of , an dcertifie dunder , on e o f th e followin g America n Societ y o f Mechanica l Engineer s (ASME ) standards:QHO-l-1994 , QHO-la-1996 , o r

QHO-1-200 4 (Standar dfo r th e Qualificatio n an dCertificatio n o f Hazardou s Wast e Incinerato r Operators)
. I f

th e Permitte e elect s t o us e th e ASM Eprogram : (A ) Contro l roo moperator s must , prio r t o th e complianc e date , achiev e provisiona l certificatio n an dmus t submi t a n applicatio n t o ASM Ean db e schedule dfo r

th e ful l certificatio n exam . Withi n 1 yea r o f th e complianc e date , contro l roo moperator s mus t achiev e ful l certification
. (B ) Ne w operator s an doperator s o f ne w source s must , befor e assumin g thei r duties , achiev e provisiona l certification , submi t a n applicatio n t o ASME , an d b e schedule dfo r

th e ful l certificatio n exam . Withi n 1 yea r o f assumin g thei r duties , thes e operator s mus t achiev e ful l certification ; or . • B e traine dan dcertifie dunde r aStat e program . • Site-specific , source-develope dan dimplemente dtrainin g program s fo r contro l roo moperator s mus t

includ e th e element s describe d4 0 CF R63.1206(c)(6)(v ) an d (vi)
. • Documentatio n o f th e operato r

trainin g an dcertificatio n progra mwil l b e maintaine di n th e operatin g recor do f th e facility
. h . NESHA Pfo rHazardou s Wast e Combustor s [4 0 CF R63.1206(c)(7 ) an d 63.6((e) ] Th e facilit y mus t

prepar e an da

t al l time s operat e accordin g t o a n operatio n an d maintenanc e pla n (O& M Plan ) tha t describe s i n detai l procedure s fo r operation , inspection , maintenance , an dcorrectiv e measure s fo r al l component s o f th e combustor , includin g associate dpollutio n contro l equipment , tha t coul daffec t emission s o f

regulate dhazardou s ai r pollutants
. Th e content s o f

th e O& M Pla n mus t addres s th e requirement s i n 4 0 CF R 63.1206(c)(7 ) an d4 0 CF R63.6(e)
. Th e O& M Pla n i s maintaine di n th e operatin g recor donsite
. 2 . Wor kPractic e Requirement s Th e facilit y shal l no t bu mhospita l medica l infectiou s waste , municipa l waste , o r berylliu mNESHA Pcontainin g waste .

2 7D . Incinerators : Uni t2 , Uni t3 , an d Uni t4 Monitorin g Requirement s 1 . Continuou s Emission s Monitorin g System s (CEMS ) an d Continuou s Opacit y Monitorin g System s (COMS ) [4 0 CF R63.1209(a) ]

a . NESHA Pfo rHazardou s Wast e Combustor s [4 0 CF R63.1209(a)(l)(i) ] Th e facilit y mus t

us e eithe r

acarbo n monoxid e o r hydrocarbo n CEM S t o demonstrat e an dmonito r

complianc e wit hth e carbo n monoxid e o r hydrocarbo n standard
. A n oxyge n CEM S mus t

b e use dt o continuousl y correc t th e carbo n monoxid e t o 7 % oxygen . I f

th e facilit y elect s t o compl y wit hth e hydrocarbo n an dcarbo n monoxid e emissio n standard s wit haC O CEMS , the n th e facilit y mus t demonstrat e tha t hydrocarbo n emission s d o no t excee dth e hydrocarbo n standar ddurin g DR Etesting
. b . NESHA Pfo rHazardou s Wast e Combustor s [4 0 CF R63.1209(a)(l)(iii) ] Afte r suc htim e a s EP A promulgate s al l performanc e specification s an doperationa l requirement s applicabl e t o P M CEMS , th e facilit y mus t install , calibrate , maintain , an doperat e aparticulat e matte r CEM S t o demonstrat e an dmonito r complianc e wit h th e particulat e matte r standard s unde r

thi s permit
.
c . NESHA Pfo rHazardou s Wast e Combustor s [4 0 CF R63.1209(a)(2) ] Th e facilit y mus t

install , calibrate , maintain , an dcontinuousl y operat e th e CEM S an d COM S i n complianc e wit hth e qualit y assuranc e procedure s provide di n th e appendi x t o 4 0 C.F.R
. par t

63 , Subpar t

EE E an dPerformanc e Specification s 1 (opacity) , 4 B (carbo n monoxid e an doxygen) , 8 A (hydrocarbons ) i n Appendi x B t o 4 0 C.F.R
. Par t 60 , an dth e requirement s o f 4 0 CF R63.1209(3 ) an d(4)
. d . NESHA Pfo rHazardou s Wast e Combustor s [4 0 CF R63.1209(a)(5 ) an d 63.8(f) ] Th e facilit y ma y petitio n EP A t o us e CEM S fo r complianc e monitorin g fo r particulat e matter , mercury , semivolatil e metals , lo w volatil e metals , an dhydroge n chlorid e an d chlorin e ga s unde r

4 0 C.F.R
. § 63.8(f) , i n lie u o f complianc e wit hthe correspondin g OPLs
.
e . NESHA Pfo rHazardou s Wast e Combustor s [4 0 CF R63.1209(a)(6) ] Calculatio n o f

rollin g average s fo r CEM S an dCOM S shoul db e performe di n accordanc e wit hth e requirement s o f 4 0 CF R63.1209(a)(6)
.

2 82 . Othe rContinuou s Monitorin g System s (CMS ) [4 0 CF R63.1209(b) ]

a . NESHA Pfo rHazardou s Wast e Combustor s [4 0 CF R63.1209(b)(1 ) an d (2) ] Th e facilit y mus t

us e CM S t o documen t complianc e wit hth e applicabl e operatin g paramete r

limit s fo r

DRE , dioxin/furan , mercury , particulat e matter , semivolatil e metals , an dlo w volatil e metals
. Excep t a s specifie di n paragraph s 4 0 CF R 63.1209(b)(2)(i ) an d(ii ) o f thi s section , th e facilit y mus t instal l an doperat e CM S othe r tha n CEM S i n conformanc e wit h4 0 CF R63.8(c)(3 ) tha t require s the facility , a t aminimum , t o compl y wit hth e manufacturer' s writte n specification s o r recommendation s fo r installation , operation , an dcalibratio n o f th e system :

• Th e calibratio n o f thermocouple s mus t

b e verifie dat

afrequenc y an di n amanne r consisten t

wit hmanufacture r

specifications , bu t

n o les s frequen t

tha n onc e pe r year . Th e facilit y mus t operat e an dmaintai n optica l pyrometer s i n accordanc e wit hmanufacture r

specification s unles s otherwis e approve db y th e Administrator
. Th e facilit y mus t

calibrat e optica l pyrometer s i n accordanc e wit hthe frequenc y an dprocedure s recommende db y th e manufacturer , bu t n o les s frequen t

tha n onc e pe r year , unles s otherwis e approve db y th e Administrator
. • I f th e facilit y operate s acarbo n injectio n system , th e accurac y o f th e weigh t measuremen t

devic e mus t

b e ±1 % o f

th e weigh t

bein g measured
. Th e calibratio n o f th e devic e mus t

b e verifie da

t leas t onc e eac hcalenda r

quarte r a t afrequenc y o f approximatel y 12 0 days
. b . NESHA Pfo rHazardou s Wast e Combustor s [4 0 CF R63.1209(b)(3) ] C M S mus t

sampl e th e regulate dparamete r withou t

interruption , an devaluat e th e detecto r respons e a

t leas t onc e eac h1 5 seconds , an dcomput e an drecor dth e averag e value s a t leas t ever y 6 0 seconds
.
c. NESHA Pfo rHazardou s Wast e Combustor s [4 0 CF R63.1209(b)(4) ] Th e spa n o f

th e non-CEM S CM S detecto r mus t no t b e exceeded
. Th e facilit y mus t interloc k

th e spa n limit s int o th e AWFC O syste mrequire db y § 63.1206(c)(3)
. d . NESHA Pfo rHazardou s Wast e Combustor s [4 0 CF R63.1209(b)(5) ] Calculatio n o f

rollin g average s fo r

CM S shoul db e performe di n accordanc e wit hth e requirement s o f

4 0 CF R63.1209(b)(5)
. 3 . Ba g Lea kDetectio n System s (CMS ) [4 0 CF R63.1206(c)(8) ] Veolia' s incinerator s ar e equippe dwit habaghouse ; therefore , th e facilit y mus t continuousl y operat e eithe r aba g lea k

detectio n syste mo r aparticulat e matte r

detectio n system . Th e system s mus t mee t th e specification s liste di n 4 0 CF R63.1206(i ) - (iv)
.

2 94 . Feedstrea m Analysi s [4 0 CF R63.1209(c) ] A nanalysi s o f

eac hfeedstrea mt o the incinerator s mus t b e obtaine dprio r

t o feedin g th e materia l t o documen t complianc e wit hth e feedrat e limit s containe di n the mos t recen t NOC
.

• Th e facilit y mus t develo p an dimplemen t afeedstrea manalysi s pla n (FAP) , th e content s o f

whic haddres s th e requirement s i n 4 0 CF R63.1209(c)(2)
. • Th e FA P mus t

b e submitte dt o th e agenc y fo r revie w an dapprova l upo n reques t i naccordanc e wit h4 0 CF R63.1209(c)(3)
. Th e FA Pi s provide di n Appendi x J o f thi s document
. • T o compl y wit hth e applicabl e feedrat e limit s o f thi s section , th e facilit y mus t monito r an drecor dfeedrate s a s provide di n 4 0 CF R63.1209(c)(4) : (1 ) Determin e an drecor dth e valu e o f th e paramete r

fo r eac hfeedstrea mb y samplin g an danalysi s o r othe r method ; (2 ) Determin e an drecor dth e mas s o r volum e flowrat e o f

eac hfeedstrea mb y aCMS
. I f

th e facilit y determine s flowrat e o f afeedstrea mb y volume , th e facilit y mus t

determin e an drecor dth e densit y o f th e feedstrea mb y samplin g an danalysi s (unles s th e facilit y report s th e constituen t concentratio n i n unit s o f weigh t pe r uni t volum e (e.g. , mg/1)) ; an d (3 ) Calculat e an drecor dth e mas s feedrat e o f th e paramete r

pe r uni t time
. I naccordanc e wit h4 0 CF R63.1209(c)(5) , th e facilit y i s no t require dt o monito r th e level s o f

metal s o r

chlorin e i n th e followin g feedstream s t o documen t complianc e wit hth e feedrat e limit s unde r thi s sectio n provide dtha t th e facilit y document s i n th e comprehensiv e performanc e tes t pla n th e expecte dlevel s o f th e constituen t

i n th e feedstrea man daccoun t fo r thos e assume dfeedrat e level s i n documentin g complianc e wit hfeedrat e limits : natura l gas , proces s air , an d feedstream s fro mvapo r recover y systems . 5 . Performanc e Evaluation s [4 0 CF R63 .1209(d) , 63 .8(d ) an d 63 .8(e) ] Th e facilit y i s require dt o conduc t performanc e evaluation s o f component s o f

th e CM S unde r th e frequenc y an dprocedure s (fo r example , submitta l o f performanc e evaluatio n tes t pla n fo r

revie w an dapproval ) applicabl e t o performanc e test s a s provide db y 4 0 CF R 63.1207
. I n addition , th e qualit y assuranc e procedure s fo r CEM S prescribe di n th e appendi x t o 4 0 CF R6 3 Subpar t EE Ei s applicable
. 6
. Conduc to f

Monitorin g [4

0 CF R63 .1209(e ) an d 63 .8 (b) ] Monitorin g mus t

b e performe di n accordanc e wit h4 0 CF R63.8(b)
.

3 07 . Operatio n an d Maintenanc e o f Continuou s Monitorin g System s [4 0 CF R 63.1209(f

) an d 63.8(c) ] Th e provision s o f

4 0 CF R63.8(c ) appl y except :

• Th e requirement s o f 4 0 CF R63.1211(c) , tha t require s CMS s t o b e installed , calibrated , an doperationa l o n th e complianc e date , shal l b e complie dwit hinstea do f sectio n 63.8(c)(3) ; an d

• Th e performanc e specification s fo r carbo n monoxide , hydrocarbon , an doxyge n CEMS s i n subpar t

B , par t 6 0 o f thi s chapte r

tha t require s detector s t o measur e th e sampl e concentratio n a t leas t onc e ever y 1 5 second s fo r calculatin g a n averag e emissio n rat e onc e ever y 6 0 second s shal l b e complie dwit hinstea do f 4 0 CF R 63.8(c)(4)(h)
. 8 . Reductio n o f

Monitorin g Dat a[4 0 CF R63.1209(h ) an d 63.8(g) ] Reductio n o f

monitorin g dat amus t b e performe di n accordanc e wit h4 0 CF R63.8(b)
. 9 . Operatin g Parameter s fo rMultipl e Standard s [4 0 CF R63.1209(f

) throug h (p) ] Th e facilit y mus t

establis hlimit s o n th e operatin g parameter s identifie di n 4 0 CF R 63.1209(j ) throug h(p ) base do n comprehensiv e performanc e testin g t o ensur e i t maintain s complianc e wit hth e emissio n standard s o f thi s subpart
. Fo r severa l parameters , th e facilit y mus t establis halimi t

fo r th e paramete r

t o ensur e complianc e wit h mor e tha n on e emissio n standard
. I f th e performanc e test s fo r suc hstandard s ar e no t performe dsimultaneously , th e mos t stringen t

limi t fo r aparamete r

derive dfro m independen t

performanc e test s applies
. A lis t o f th e OPL s require di s provide di n sectio n C
. 1
. ao f

thi s document
. 10 . Operatin g Paramete rLimi tAveragin g Period s [4 0 CF R63.1209(r) ] Th e averagin g period s specifie dfo r operatin g parameter s ar e not-to-excee daveragin g periods
. Th e facilit y ma y elec t t o us e shorte r

averagin g periods
. Fo r example , th e facilit y ma y elec t

t o us e a1-hou r

rollin g averag e rathe r tha n th e 12-hou r

rollin g averag e specifie dfo r

mercury . E . Incinerators : Uni t2 , Uni t3 , an d Uni t4 Performanc e Testin g Requirement s 1 . Change s t

o th e Sourc e [4

0 CF R63.1206(b)(5)(i)(B) ] I f change s occu r

(a s define di n 4 0 CF R63.1206(b)(5)(iii) ) t o th e design , operation , o r maintenanc e practice s o f th e sourc e i n amanne r tha t ma y adversel y affec t complianc e wit han y emissio n standar dtha t i s no t monitore dwit haCEMS , acomprehensiv e performanc e tes t

mus t b e conducte dunde r

th e requirement s o f

4 0 CF R63.1207(f)(1 ) an d (g)(1 ) t o documen t

complianc e wit hth e affecte demissio n standard(s ) an dt o confir m

3 1existin g o r establis hne w OPL s a s require dunde r 4 0 CF R63.1209 , an dsubmi t ane w Notificatio n o f

Compliance
. 2 . Complianc e wit h C O an d TH C Emissio n Standar d [4 0 CF R63.1206(b)(6) ] Thi s paragrap happlie s t o source s tha t elec t t o compl y wit hth e carbo n monoxid e an d hydrocarbo n emission s standard s o f subpar t EE Eb y documentin g continuou s complianc e wit hth e carbo n monoxid e standar dusin g acontinuou s emission s monitorin g syste man d documentin g complianc e wit hth e hydrocarbo n standar ddurin g th e DR E performanc e tes t o r it s equivalent
. (a ) If , durin g th e acceptabl e DR E test , th e Permitte e di dno t obtai n hydrocarbo n emission s dat asufficien t t o documen t

complianc e wit hth e hydrocarbo n standard , th e facilit y mus t

either :

• Perform , a s par t o f th e performanc e test , a n "equivalen t DR E test " t o documen t complianc e wit hth e hydrocarbo n standard
. A n equivalen t DR Etes t

i s comprise do f

a minimu mo f

thre e runs , eac hwit haminimu mduratio n o f 1 hou r durin g whic hth e Permitte e operate s th e combusto r a s clos e a s reasonabl y possibl e t o th e OPL s tha t th e Permitte e establishe dbase do n th e initia l DR E test . Th e Permitte e mus t us e th e highes t hourl y rollin g averag e hydrocarbo n emissio n leve l achieve ddurin g th e equivalen t

DR Etes t

t o documen t

complianc e wit hth e hydrocarbo n standard ; o r
• Perfor maDR Etes t a s par t o f th e performanc e test . 3 . Type s o f

Performanc e Test s [4 0 CF R63.1207(b) ]

• Th e facilit y i s require dt o conduc t comprehensiv e performanc e test s t o demonstrat e complianc e wit hth e emissio n standard s provide db y thi s subpart , establis hlimit s fo r

the operatin g parameter s provide db y 4 0 CF R63.1209 , an d demonstrat e complianc e wit hth e performanc e specification s fo r continuou s monitorin g systems . • Th e facilit y mus t conduc t

confirmator y performanc e test s t o demonstrat e complianc e wit hth e dioxin/fura n emissio n standar dwhe n th e sourc e operate s unde r norma l operatin g condition s an dt o conduc t aperformanc e evaluatio n o f continuou s monitorin g system s require dfo r complianc e assuranc e wit hth e dioxin/fura n emissio n standar dunde r 4 0 CF R63.1209(k)
. 

## • 4 . Frequenc y o f

Performanc e Tests [4 0 CF R63.1207(d) ] Th e facilit y mus t

conduc t

testin g periodicall y a s prescribe di n 4 0 CF R63.1207(d)(1 ) throug h(d)(3)
.

• A comprehensiv e performanc e tes t mus t b e conducte dn o late r tha n 6 1 month s afte r th e beginnin g o f

th e previou s comprehensiv e performanc e tes t use dt o sho w complianc e wit h4 0 CF R6 3 Subpar t EE Erequirements
.

3 2• A confirmator y tes t mus t b e conducte dn o late r tha n 3 1 month s afte r th e beginnin g o f

th e previou s comprehensiv e performanc e tes t use dt o sho w complianc e wit h4 0 CF R6 3 Subpar t EE Erequirements
. Th e deadlin e fo r

commencin g confirmator y an dcomprehensiv e performanc e testin g i s base do n th e dat e o f

commencemen t

o f th e previou s comprehensiv e performanc e test . 5 . Conten to f

Performanc e Tes tPlan s [4 0 CF R63 .1207(f) ]

a . NESHA Pfo rHazardou s Wast e Combustor s [4 0 CF R63 .1207(f)(1) ] Comprehensiv e performanc e tes t plan s mus t

mee t th e requirement s o f 4 0 C F R63.7(c)(2)(i)-(iii ) an d(v)
. I n addition , comprehensiv e performanc e tes t plan s mus t includ e th e followin g information :

• A n analysi s o f

eac hfeedstream , includin g hazardou s waste , othe r fuels , an d industria l furnac e feedstocks , a s fired , tha t includes : heatin g value , level s o f as h (fo r hazardou s wast e incinerator s only) , level s o f semivolatil e metals , lo w volatil e metals , mercury , an dtota l chlorin e (organi c an dinorganic) ; an dviscosit y o r descriptio n o f

the physica l for mo f

th e feedstream
. • Fo r organi c hazardou s ai r pollutant s establishe db y 4 2 U.S.C
. 7412(b)(1) , excludin g caprolacta m(CA S numbe r 105602 ) a s provide db y § 63.60 : a n identificatio n o f

suc horgani c hazardou s ai r pollutant s tha t

ar e presen t

i n eac h hazardou s wast e feedstrea mexcep t a s provide db y paragrap h4 0 CF R 63.1207(f)(l)(ii)(D ) o f thi s section , a n approximat e quantificatio n o f suc h identifie dorgani c hazardou s ai r pollutant s i n th e hazardou s wast e feedstreams , withi n th e precisio n produce db y analytica l procedure s o f § 63.1208(b)(8) , an da descriptio n o f

blendin g procedures , i f applicable , prio r

t o firin g th e hazardou s wast e feedstream , includin g adetaile danalysi s o f th e material s prio r

t o blending , an dblendin g ratios
. A hazardou s wast e feedstrea manalysi s fo r organi c hazardou s ai r

pollutant s ma y approve do n acase-by-cas e basi s i n lie u o f th e analysi s require dunde r paragrap h4 0 CF R63.1207(f)(l)(ii)(A ) i f th e reduce d analysi s i s sufficien t t o ensur e tha t

th e POHC s use dt o demonstrat e complianc e wit hth e applicabl e DR Estandard s o f thi s subpar t

continu e t o b e representativ e o f th e mos t

difficul t

t o destro y organi c compound s i n th e facility' s hazardou s wast e feedstreams
. • A detaile dengineerin g descriptio n o f th e hazardou s wast e combustor , including : manufacturer' s nam e an dmode l numbe r o f th e hazardou s wast e combustor ; typ e o f hazardou s wast e combustor ; maximu mdesig n capacit y i n appropriat e units ; descriptio n o f

th e fee dsyste mfo r

eac hfeedstream ; capacit y o f eac hfee dsystem ; descriptio n o f

automati c hazardou s wast e fee dcutof f system(s) ; descriptio n o f th e design , operation , an dmaintenanc e practice s fo r an y ai r pollutio n contro l system ; an ddescriptio n o f

th e design , operation , an dmaintenanc e practice s o f an y stac k ga s monitorin g an dpollutio n contro l monitorin g systems . • A detaile ddescriptio n o f samplin g an dmonitorin g procedures , includin g samplin g an dmonitorin g location s i n th e system , th e equipmen t t o b e used , 3 3samplin g an dmonitorin g frequency , an dplanne danalytica l procedure s fo r sampl e analysis
. Adetaile dtes t

schedul e fo r

eac hhazardou s wast e fo r whic hth e performanc e tes t i s planned , includin g date(s) , duration , quantit y o f hazardou s wast e t o b e burned , an dothe r

relevan t

factors
. Adetaile dtes t

protocol , including , fo r eac hhazardou s wast e identified , th e range s o f hazardou s wast e feedrat e fo r eac hfee dsystem , and , a s appropriate , th e feedrate s o f

othe r fuel s an dfeedstocks , an dan y othe r relevan t

parameter s tha t ma y affec t

th e abilit y o f

th e hazardou s wast e combusto r t o mee t

th e emissio n standards
. Adescriptio n of , an dplanne doperatin g condition s for , an y emissio n contro l equipmen t

tha t wil l b e used
. Procedure s fo r

rapidl y stoppin g th e hazardou s wast e fee dan dcontrollin g emission s i n th e even t o f a n equipmen t

malfunction
. Adeterminatio n o f

th e hazardou s wast e residenc e tim e a s require db y 4 0 CF R 63.1206(b)(ll)
. I f th e facilit y i s requestin g t o extrapolat e meta l feedrat e limit s fro m comprehensiv e performanc e tes t level s unde r

4 0 CF R63.1209(l)(l)(v ) o r 63.1209(n)(2)(vii) : adescriptio n o f th e extrapolatio n methodolog y an drational e fo r ho w th e approac hensure s complianc e wit hth e emissio n standards , documentatio n o f

th e historica l rang e o f norma l (i.e. , othe r tha n durin g complianc e testing ) metal s feedrate s fo r eac hfeedstream , an ddocumentatio n tha t th e leve l o f

spikin g recommende ddurin g th e performanc e tes t wil l mas k

samplin g an danalysi s imprecisio n an dinaccurac y t o th e exten t tha t the extrapolate d feedrat e limit s adequatel y assur e complianc e wit hth e emissio n standards
. I f th e facilit y doe s no t

continuousl y monito r regulate dconstituent s i n natura l gas , proces s ai r

feedstreams , an dfeedstream s fro mvapo r recover y system s unde r 4 0 C F R63.1209(c)(5) , i t mus t includ e documentatio n o f the expecte dlevel s o f regulate dconstituent s i n thos e feedstreams
. Documentatio n justifyin g th e duratio n o f syste mconditionin g require dt o ensur e th e combusto r

ha s achieve dsteady-stat e operation s unde r performanc e tes t operatin g conditions , a s provide db y paragrap h(g)(l)(iii ) o f thi s section
. Fo r cemen t kiln s wit hin-lin e ra w mills , i f th e facilit y elect s t o us e th e emission s averagin g provisio n o f thi s subpart , i t

mus t notif y th e Administrato r o f it s inten t

i n th e initia l (an dsubsequent ) comprehensiv e performanc e tes t plan , an dprovid e th e informatio n require db y th e emissio n averagin g provision
. Fo r preheate r

o r preheater/precalcine r cemen t kiln s wit hdua l stacks , i f th e facilit y elect s t o us e th e emission s averagin g provisio n o f thi s subpart , i t

mus t notif y th e Administrato r

o f it s inten t

i n th e initia l (an dsubsequent ) comprehensiv e performanc e tes t

plan , an dprovid e th e informatio n require db y th e emissio n averagin g provision
. I f th e facilit y request s t o us e Metho d2 3 fo r dioxin/furan , i t

mus t provid e th e informatio n require dunde r 4 0 CF R63.1208(b)(l)(i)(B)
. I f th e facilit y i s no t require dt o conduc t performanc e testin g t o documen t complianc e wit hth e mercury , semivolatil e metals , lo w volatil e metals , o r hydroge n chloride/chlorin e ga s emissio n standard s 4 0 CF R63.1207(m) , i t mus t 3 4includ e wit hth e comprehensiv e performanc e tes t pla n documentatio n o f complianc e wit hth e provision s o f tha t section
. • I f th e facilit y propose s t o us e asurrogat e fo r measurin g o r

monitorin g ga s flowrate , i t

mus t documen t

i n th e comprehensiv e performanc e tes t pla n tha t

th e surrogat e adequatel y correlate s wit hga s flowrate , a s require db y 4 0 CF R 63.1207(m)(7) , an d4 0 CF R63.1209(j)(2) , (k)(3) , (m)(2)(i) , (n)(5)(i) , an d (o )(2)(i)
. • A n applicatio n mus t b e submitte dt o reques t alternativ e monitorin g unde r 4 0 CF R 63.1209(g)(1 ) no t

late r tha n wit hth e comprehensiv e performanc e tes t plan , a s require db y 4 0 CF R63 .1209(g)(l)(iii )(A) . • Th e temperatur e locatio n measuremen t mus t b e documente di n th e comprehensiv e performanc e tes t

plan , a s require db y 4 0 CF R63.1209(j)(l)(i ) an d 63 .1209(k)(2)(i)
. • Fo r th e activate dcarbo n injectio n system , th e facilit y mus t documen t

i n th e comprehensiv e performanc e tes t plan : th e manufacture r specification s fo r minimu mcarrie r

flui dflowrat e o r

pressur e drop , a s require db y 4 0 CF R 63.1209(k)(6)(ii) ; an dke y parameter s tha t affec t carbo n adsorption , an dth e operatin g limit s th e facilit y establishe s fo r thos e parameter s base do n th e carbo n use ddurin g th e performanc e test , i f i t elect s no t

t o specif y an dus e th e bran dan d typ e o f carbo n use ddurin g th e comprehensiv e performanc e test , a s require db y 4 0 C F R63 .1209(k )(6 )(iii)
. • Fo r adr y scrubbe r

use dt o contro l hydroge n chlorid e an dchlorin e gas , th e facilit y mus t documen t

i n th e comprehensiv e performanc e tes t pla n ke y parameter s tha t affec t adsorption , an dth e limit s i t establishe s fo r

thos e parameter s base do n th e sorben t use ddurin g th e performanc e test , i f th e facilit y elect s no t t o specif y an d us e th e bran dan dtyp e o f sorben t use ddurin g th e comprehensiv e performanc e test , a s require db y 4 0 CF R63.1209(o)(4)(iii)(A)
. • Fo r purpose s o f

calculatin g semivolatil e metal , lo w volatil e metal , mercury , an d tota l chlorin e (organi c an dinorganic) , an das h feedrat e limits , adescriptio n o f ho w th e facilit y wil l handl e performanc e tes t feedstrea manalytica l result s tha t determine s thes e constituent s ar e no t presen t a t detectabl e levels
. • Suc hothe r

informatio n a s th e Administrato r reasonabl y find s necessar y t o determin e whethe r

t o approv e th e performanc e tes t plan
. b . NESHA Pfo rHazardou s Wast e Combustor s [4 0 CF R63.1207(f)(2) ] Confirmator y performanc e tes t plan s mus t

mee t th e requirement s o f 4 0 C F R63.7(c)(2)(i)-(iii ) an d(v)
. I n addition , confirmator y performanc e tes t plan s mus t includ e th e followin g information :

• A descriptio n o f

th e norma l hydrocarbo n o r carbo n monoxid e operatin g levels , a s specifie di n paragrap h(g)(2)(i ) o f thi s section , an da n explanatio n o f ho w thes e norma l level s wer e determined
. • A descriptio n o f

th e norma l applicabl e operatin g paramete r levels , a s specifie di n paragrap h(g)(2)(ii ) o f thi s section , an da n explanatio n o f ho w thes e norma l level s wer e determined
. 3 5• A descriptio n o f th e norma l chlorin e operatin g levels , a s specifie di n paragrap h (g)(2)(iii ) o f

thi s section , an da n explanatio n o f ho w thes e norma l level s wer e determined
. • Fo r acarbo n injectio n syste mo r acarbo n bed , adescriptio n o f th e norma l cleanin g cycl e o f

th e particulat e matte r contro l device , a s specifie di n 4 0 CF R 63.1207(g)(2)(iv) , an da n explanatio n o f ho w thes e norma l level s wer e determined
. • A detaile ddescriptio n o f samplin g an dmonitorin g procedure s includin g samplin g an dmonitorin g location s i n th e system , th e equipmen t t o b e used , samplin g an d monitorin g frequency , an dplanne danalytica l procedure s fo r sampl e analysis
. • A detaile dtes t

schedul e fo r

eac hhazardou s wast e fo r whic hth e performanc e tes t i s planned , includin g date(s) , duration , quantit y o f hazardou s wast e t o b e burned , an dothe r

relevan t

factors
. • A detaile dtes t

protocol , including , fo r eac hhazardou s wast e identified , th e range s o f hazardou s wast e feedrat e fo r eac hfee dsystem , and , a s appropriate , th e feedrate s o f

othe r fuel s an dfeedstocks , an dan y othe r relevan t

parameter s tha t ma y affec t

th e abilit y o f

th e hazardou s wast e combusto r t o mee t

th e dioxin/fura n emissio n standard
. • A descriptio n of , an dplanne doperatin g condition s for , an y emissio n contro l equipmen t

tha t wil l b e used
. • Procedure s fo r

rapidl y stoppin g th e hazardou s wast e fee dan dcontrollin g emission s i n th e even t o f a n equipmen t

malfunction
. • Suc hothe r

informatio n a s th e Administrato r reasonabl y find s necessar y t o determin e whethe r

t o approv e th e confirmator y tes t plan
. 6 . Operatin g Condition s Durin g Performanc e Test s [4 0 CF R63.1207(g) ] Th e provision s o f

4 0 CF R63.7(e ) applies
. Performanc e testin g mus t b e conducte dunde r operatin g condition s representativ e o f th e extrem e rang e o f norma l condition s whic hi s consisten t

wit h4 0 CF R63.7(e)(1)
.
a . NESHA Pfo rHazardou s Wast e Combustor s [4 0 CF R63.1207(g)(a) ] Fo r th e followin g parameters , th e combusto r mus t b e operate ddurin g th e comprehensiv e performanc e tes t unde r norma l condition s (o r condition s tha t

wil l resul t i n highe r

tha n norma l emissions) :

• Chlorine feedrate. Th e facilit y mus t fee dnorma l (o r

higher ) level s o f

chlorin e durin g the dioxin/fura n performanc e test ;

• Ash feedrate. Fo r hazardou s wast e incinerators , th e facilit y mus t conduc t

th e followin g test s whe n feedin g norma l (o r higher ) level s o f

ash : th e semivolatil e meta l an dlo w volatil e meta l performanc e tests , an dth e dioxin/fura n an dmercur y performanc e test s i f

activate dcarbo n injectio n o r acarbo n be di s used ; an d

• Cleaning cycle of the particulate matter control device. Th e facilit y mus t conduc t th e followin g test s whe n th e particulat e matte r contro l devic e undergoe s it s norma l (o r

mor e frequent ) cleanin g cycle : th e particulat e matter , semivolatil e 3 6metal , an dlo w volatil e meta l performanc e tests ; an dth e dioxin/fura n an dmercur y performanc e test s i f

activate dcarbo n injectio n o r acarbo n be di s used
. Give n tha t

th e facilit y mus t

establis hlimit s fo r

th e applicabl e operatin g parameter s specifie di n 4 0 CF R63.120 9 base do n operation s durin g th e comprehensiv e performanc e test , th e facilit y ma y conduc t testin g unde r

tw o o r mor e operatin g mode s t o provid e operatin g flexibility
. Prio r t o obtainin g performanc e tes t data , th e facilit y mus t operat e unde r

performanc e tes t condition s unti l i t

reache s steady-stat e operation s wit hrespec t t o emission s o f pollutant s i t

mus t measur e durin g th e performanc e tes t an doperatin g parameter s unde r 4 0 CF R63.120 9 fo r whic hi t

mus t establis hlimits
. Durin g syste m conditioning , th e facilit y mus t ensur e tha t

eac hoperatin g paramete r fo r whic hi t mus t establis halimi t

i s hel dat

th e leve l planne dfo r th e performanc e test . Th e facilit y mus t

includ e documentatio n i n th e performanc e tes t pla n justifyin g th e duratio n o f

syste mconditioning
. b
. NESHA Pfo rHazardou s Wast e Combustor s [4 0 CF R63 .1207 (g )(b) ] Fo r th e followin g parameters , th e confirmator y performanc e testin g fo r dioxin/fura n mus t b e conducte dunde r

norma l operatin g conditions :

• Carbon monoxide (or hydrocarbon) CEM S emission s level s mus t b e withi n th e rang e o f

th e averag e valu e t o th e maximu mvalu e allowed , excep t a s provide db y paragrap h(g)(2)(v ) o f thi s section
. Th e averag e valu e i s define da s th e su mo f th e hourl y rollin g averag e value s recorde d(eac hminute ) ove r th e previou s 1 2 months , divide db y th e numbe r o f rollin g average s recorde ddurin g tha t time
. Th e averag e valu e mus t

no t includ e calibratio n data , startu p data , shutdow n data , malfunctio n data , an ddat aobtaine dwhe n no t burnin g hazardou s waste . • Eac hoperatin g limi t (specifie di n 4 0 CF R63.1209 ) establishe dt o maintai n complianc e wit hth e dioxin/fura n emissio n standar dmus t b e hel dwithi n th e rang e o f th e averag e valu e ove r th e previou s 1 2 month s an dth e maximu mo r minimum , a s appropriate , tha t

i s allowed , excep t

a s provide db y 4 0 CF R63.1207(g)(2)(v)
. Th e averag e valu e i s define da s th e su mo f th e rollin g averag e value s recorde d ove r th e previou s 1 2 months , divide db y th e numbe r o f rollin g average s recorde d durin g tha t

time
. Th e averag e valu e mus t no t includ e calibratio n data , startu p data , shutdow n data , malfunctio n data , an ddat aobtaine dwhe n no t burnin g hazardou s waste . • Chlorin e mus t

b e fe da

t norma l feedrate s o r

greater . • Fo r acarbo n injectio n syste mo r carbo n bed , norma l cleanin g cycl e o f th e particulat e matte r

contro l device
. • Th e Administrato r ma y approv e a n alternativ e rang e t o tha t require db y paragraph s 4 0 CF R63.1207(g)(2)(i ) an d(ii ) i f th e facilit y document s i n th e confirmator y performanc e tes t pla n tha t

i t ma y b e problemati c t o maintai n th e require drang e durin g th e test . I n addition , whe n makin g th e findin g o f compliance , th e Administrato r ma y conside r

tes t condition s outsid e o f th e rang e
3 7specifie di n th e tes t pla n base do n afindin g tha t th e facilit y coul dno t reasonabl y maintai n th e rang e specifie di n th e tes t pla n an dconsiderin g factor s includin g whethe r th e tim e duratio n an dleve l o f th e paramete r

whe n operation s wer e ou t o f th e specifie drang e wer e suc htha t operation s durin g th e confirmator y tes t ar e determine dt o b e reasonabl y representativ e o f norma l operations
. I n addition , th e Administrato r

wil l conside r

th e proximit y o f

th e emissio n tes t

result s t o th e standard
. 7 . Operatin g Condition s Durin g Subsequen tPerformanc e Tests [4 0 CF R 63.1207(h) ] Curren t operatin g paramete r

limit s establishe dunde r 4 0 CF R63.120 9 ar e waive ddurin g subsequen t

comprehensiv e performanc e testing
. Curren t operatin g paramete r

limit s ar e als o waive ddurin g pretestin g prio r t o comprehensiv e performanc e testin g fo r a n aggregat e tim e no t

t o excee d72 0 hour s o f operatio n (renewabl e a t th e discretio n o f

th e Administrator ) unde r a n approve dtes t

pla n o r

i f th e sourc e record s th e result s o f th e pretesting
. 8 . Tes tMethod s [4 0 CF R63.1208 ] Tes t method s a s describe di n 4 0 CF R63.120 8 mus t b e use dt o determin e complianc e wit hth e applicabl e emissio n standards
. 9 . Failur e o f

Performanc e Tes t[4 0 CF R63.1207(1) ]

a . NESHA Pfo rHazardou s Wast e Combustor s [4 0 CF R63.1207(f)(1) ] Th e provision s o f

thi s paragrap hd o no t appl y t o th e initia l comprehensiv e performanc e tes t

i f th e facilit y conduct s th e tes t prio r t o it s complianc e date
.

• I f i t i s determine d(base do n CE M recordings , result s o f analyse s o f

stac k samples , o r

result s o f

CM S performanc e evaluations ) tha t th e facilit y ha s exceede dan y emissio n standar ddurin g acomprehensiv e performanc e tes t fo r a mod e o f

operation , hazardou s wast e burnin g mus t ceas e immediatel y unde r tha t mod e o f

operation
. Thi s determinatio n mus t b e mad e withi n 9 0 day s followin g completio n o f

th e performanc e test . • I f th e facilit y ha s faile dt o demonstrat e complianc e wit hth e emissio n standard s fo r an y mod e o f

operation , prio r

t o submittin g arevise dNotificatio n o f Compliance , i t

ma y bur n hazardou s wast e onl y fo r th e purpos e o f

pretestin g o r comprehensiv e performanc e testin g unde r revise doperatin g conditions , an donl y fo r amaximu mo f

72 0 hour s (renewabl e a t th e discretio n o f

th e Administrator) , excep t a s provide db y 4 0 CF R63.1207(1)(3)
. • Th e facilit y mus t conduc t

acomprehensiv e performanc e tes t unde r revise d operatin g condition s followin g th e requirement s fo r performanc e testin g o f thi s section
.

3 8• Th e facilit y mus t submi t t o th e Administrato r aNotificatio n o f

Complianc e subsequen t

t o th e ne w comprehensiv e performanc e test . b . NESHA Pfo rHazardou s Wast e Combustor s [4 0 CF R63.1207(f)(2) ]

• I f i t i s determine d(base do n CE M recordings , result s o f analyse s o f

stac k samples , o r

result s o f

CM S performanc e evaluations ) tha t th e facilit y ha s faile d th e dioxin/fura n emissio n standar ddurin g aconfirmator y performanc e test , i t mus t ceas e burnin g hazardou s wast e immediately
. Thi s determinatio n mus t b e mad e withi n 9 0 day s followin g completio n o f th e performanc e test . • T o bur n hazardou s wast e i n th e future , th e facilit y mus t submi t

t o th e Administrato r

fo r revie w an dapprova l ates t pla n t o conduc t

acomprehensiv e performanc e tes t

t o identif y revise dlimit s o n th e applicabl e dioxin/fura n operatin g parameter s specifie di n 4 0 CF R63.1209(k)
. • T o bur n hazardou s wast e i n th e future , th e facilit y mus t submi t

t o th e Administrato r

aNotificatio n o f

Complianc e wit hth e dioxin/fura n emissio n standard
. Th e facilit y mus t includ e i n th e Notificatio n o f Complianc e th e revise d limit s o n th e applicabl e dioxin/fura n operatin g parameter s specifie di n 4 0 CF R 63.1209(k);an d

• Unti l th e Notificatio n o f Complianc e i s submitted , th e facilit y mus t no t bur n hazardou s wast e excep t fo r purpose s o f

pretestin g o r

confirmator y performanc e testing , an dfo r

amaximu mo f

72 0 hour s (renewabl e a t th e discretio n o f

th e Administrator) , excep t a s provide db y 4 0 CF R63.1207(1)(3 ) o f thi s section
.
c . NESHA Pfo rHazardou s Wast e Combustor s [4 0 CF R63.1207(f)(3) ] Th e facilit y ma y petitio n th e Administrato r t o obtai n writte n approva l t o bur n hazardou s wast e i n th e interi mprio r t o submittin g aNotificatio n o f Complianc e fo r purpose s othe r

tha n testin g o r

pretesting
. Th e facilit y mus t specif y operatin g requirements ; includin g limit s o n operatin g parameter s tha t ar e determine dt o ensur e complianc e wit hth e emissio n standard s o f thi s subpar t

base do n availabl e informatio n includin g dat afro mth e faile dperformanc e test . Th e Administrato r wil l review , modif y a s necessary , an dapprov e i f warrante dth e interi moperatin g requirements
. A n approva l o f interi moperatin g requirement s wil l includ e aschedul e fo r submittin g aNotificatio n o f Compliance
. F . Incinerators : Uni t2 , Uni t3 , an d Uni t4 Recordkeepin g an d Reportin g 1 . Summar y o f

Notificatio n Requirement s [4 0 CF R63.1210(a) ] Th e followin g notificatio n requirement s a s outline di n 4 0 CF R63.121 0 ar e applicable : Reference Notificatio n 63.9(b ) Initia l notification s tha t th e facilit y i s subjec t

to Subpart

EE Eo f thi s Part
.

3 9Reference Notificatio n

63.9(d ) Notificatio n that th e facilit y i s subjec t

to specia l complianc e requirements
. 63.9 © Notificatio n an ddocumentatio n o f an y chang e i n informatio n alread y provide dunde r

§ 63.9
. 63.1206(b)(5)(i ) Notificatio n o f change s i n design , operation , o r maintenance
. 63.1206(c)(8)(iv ) Notificatio n o f excessiv e ba g lea k

detectio n syste mexceedances
. 63.1206(c)(9)(v ) Notificatio n o f excessiv e particulat e matte r detectio n syste m exceedances
. 63.1207(e) , 63.9(e ) 63.9(g)(1 ) an d(3 ) Notificatio n o f performanc e tes t

an dcontinuou s monitorin g syste m evaluation , includin g the performanc e tes t pla n an dCM S performanc e evaluatio n plan. 1 63.1210(b ) Notificatio n o f inten t t o comply
. 63.1210(d) , 63.1207(j) , 63.1207(k) , 63.1207(1) , 63.9(h) , 63.10(d)(2) , 63.10(e)(2 ) Notificatio n o f compliance , includin g result s o f performanc e test s an d continuou s monitorin g syste mperformanc e evaluations
.
Th e facilit y mus t

submi t th e followin g notification s t o th e Administrato r i f i t request s o r elect s t o compl y wit halternativ e requirements :
Reference Notification , Request, Petition , o rApplicatio n 63.9(i ) Th e facilit y ma y reques t a n adjustmen t

to tim e period s o r

postmark

deadline s fo r

submitta l an drevie w o f

require dinformation
. 63.10(e)(3 )(ii ) Th e facilit y ma y reques t t o reduc e the frequenc y o f exces s emission s an dCM S performanc e reports . 63.10(f ) Th e facilit y ma y reques t t o waiv e recordkeepin g o r reportin g requirements
. 63.1204(d)(2)(iii) , 63.1220(d)(2)(iii ) Notificatio n tha t th e facilit y elect s t o compl y wit hth e emissio n averagin g requirement s fo r cemen t kiln s wit hin-lin e ra w mills
. 63.1204(e)(2)(iii) , 63.1220(e)(2)(iii ) Notificatio n tha t th e facilit y elect s t o compl y wit hth e emissio n averagin g requirement s fo r preheater o r preheater/precalcine r

kiln s wit hdua l stacks
. 63.1206(b)(4) , 63.1213 , 63.6(i) , 63.9(c ) Th e facilit y ma y reques t a n extensio n o f

th e complianc e dat

e fo r u p t o on e year . 63.1206(b)(5)(i)(C ) Th e facilit y ma y reques t t o bur n hazardou s waste fo r mor e tha n 72 0 hour s an dfo r purpose s other tha n testin g o r

pretestin g afte r

makin g achang e i n th e desig n o r operatio n tha

t coul d affec t complianc e wit hemissio n standard s an dprio r to submittin g arevise dNotificatio n o f Compliance
. 63.1206(b)(8)(iii)(B ) I f the facilit y elect s t o conduc t particulat e matter

CEM S correlatio n testin g an dwishe s to hav e federa l particulat e matter an dopacit y standard s an dassociate doperatin g limit s waive ddurin g th e testing , i t mus t notify the Administrato r b y submittin g th e correlatio n tes t pla n fo r revie w an dapproval
. 63.1206(b)(8)(v ) Th e facilit y ma y reques t approva l t o hav e th e particulat e matter an dopacit y standard s an d associate doperatin g limit s an dcondition s waive dfo r mor e than 9 6 hour s fo r acorrelatio n test . 4 0Reference Notification , Request, Petition , o rApplicatio n

63.1206(b)(9 ) Owner s an doperator s o f lightweigh t

aggregate kiln s ma y reques t approva l o f

alternativ e emissio n standard s fo r

mercury , semivolatil e metal , lo w volatil e metal , an dhydroge n chloride/chlorin e ga s unde r certai n conditions
. 63.1206(b)(10 ) Owner s an doperator s o f cemen t kiln s ma y reques t

approva l o f

alternativ e emissio n standard s fo r

mercury , semivolatil e metal , lo w volatil e metal , an dhydroge n chloride/chlorin e ga s unde r certai n conditions
. 63.1206(b)(14 ) Owner s an doperator s o f incinerator s ma y elec t

to compl y wit ha n alternativ e t o th e particulat e matte r

standard
. 63.1206(b)(15 ) Owner s an doperator s o f cemen t an dlightweigh t

aggregate kiln s ma y reques t to compl y wit hthe alternativ e t

o the interi mstandard s fo r mercury . 63.1206(c)(2)(ii)(C ) Th e facilit y ma y reques t to mak e change s to the startup , shutdown , an dmalfunctio n plan
. 63.1206(c)(5)(i)(C ) Th e facilit y ma y reques t a n alternativ e mean s o f contro l to provid e contro l o f combustio n syste mleaks
. 63.1206(c)(5)(i)(D ) Th e facilit y ma y reques t othe r technique s t o preven t

fugitiv e emission s withou t us e o f instantaneou s pressur e limits
. 63.1207(c)(2 ) Th e facilit y ma y reques t t o bas e initia l complianc e o n dat ai n lie u o f acomprehensiv e performanc e test . 63.1207(d)(3 ) Th e facilit y ma y reques t mor e tha n 6 0 day s to complet e aperformanc e tes t i f additiona l tim e i s neede dfo r

reason s beyon dit s control
. 63.1207(e)(3) , 63.7(h ) Th e facilit y ma y reques t atim e extensio n i f

the Administrato r

fail s t o approv e o r

den y it s tes t plan
. 63.1207(h)(2 ) Yo u ma y reques t t o waiv e curren t

operatin g parameter

limit s durin g pretestin g fo r mor e tha n 72 0 hours
. 63.1207(f)(l)(ii)(D ) Th e facilit y ma y reques t areduce dhazardou s waste feedstrea manalysi s fo r organi c hazardou s ai r

pollutant s i f

th e reduce danalysi s continue s t o b e representativ e o f organi c hazardou s ai r

pollutant s i n it s hazardou s waste feedstreams
. 63.1207(g)(2)(v

) Th e facilit y ma y reques t t o operate unde r

awide r operatin g rang e fo r

aparameter

durin g confirmator y performanc e testing
. 63.1207 © Th e facilit y ma y reques t u p to aone-year

tim e extensio n fo r

conductin g aperformanc e tes t (other tha n th e initia l comprehensiv e performanc e test) t o consolidat e testin g wit h other stat e o r federally-require dtesting
. 63.1207©(4 ) Th e facilit y ma y reques t mor e tha n 9 0 day s t o submi t aNotificatio n o f

Complianc e afte r completin g aperformanc e tes t i f additiona l tim e i s neede dfo r reason s beyon ditscontrol
. 63.1207(1)(3 ) Afte r failur e o f

aperformanc e test , the facilit y ma y reques t t o bur n hazardou s waste fo r mor e tha n 72 0 hour s an dfo r purpose s other

than testin g o r

pretesting
. 63.1209(a)(5) , 63.8( 0 Th e facilit y ma y request : (1 ) Approva l o f alternativ e monitorin g method s fo r complianc e wit hstandard s tha

t ar e monitore dwit haCEMS ; an d(2 ) approva l t o us e aCEM S i n lie u o f operatin g paramete r

limits
. 63.1209(g)(1 ) Th e facilit y ma y reques t approva l of : (1 ) Alternative s t o operatin g paramete r

monitorin g requirements , excep t

fo r standard s tha

t i t mus t monito r wit hacontinuou s emissio n monitorin g syste m(CEMS ) an dexcep t fo r request s to us e aCEM S i n lie u o f operatin g parameter

limits ; o r

(2 ) awaive r

o f a n operatin g parameter limit
.
4 1Referenc e Notification , Request, Petition , o rApplicatio n

63.1209 (1X1 ) Th e facilit y ma y reques t to extrapolat e mercur y feedrat e limits
. 63.1209(n)(2 ) Th e facilit y ma y reques t to extrapolat e semivolatil e an dlo w volatil e meta l feedrat e limits
. 63.1211(d ) Th e facilit y ma y reques t to us e dat acompressio n technique s t o recor ddat ao n ales s frequen t basi s tha n require db y § 63.1209
. 2 . Summar y o f

Reportin g Requirement s [4 0 CF R63.1211(a) ] Th e followin g report s mus t b e submitte di n accordanc e wit h4 0 CF R63.1211 : Reference Repor t 63.10(d)(4 ) Complianc e progres s reports , i f require da s aconditio n o f a n extensio n o f

th e complianc e date grante dunde r

§ 63.6(i)
. 63.10(d)(5) ® Periodi c startup , shutdown , an dmalfunctio n reports . 63.10(d)(5)(a ) Immediat e startup , shutdown , an dmalfunctio n reports . 63.10(e)(3 ) Excessiv e emission s an dcontinuou s monitorin g syste mperformanc e report an dsummary report . 63.1206(c)(2)(ii)(B ) Startup , shutdown , an dmalfunctio n plan
. 63.1206(c)(3)(vi ) Excessiv e exceedance s reports . 63.1206(c)(4)(iv ) Emergenc y safet y ven t openin g reports . 63.1206(c)(3)(vi ) AWFC O excessiv e exceedanc e reports . 63.1206(c)(8)(iv ) BLD S excessiv e exceedanc e reports . 63.1206(c)(4 ) ES V openin g tha t results i n failur e to meet emissio n standards
. 3 . Summar y o f

Recordkeepin g Requirement s [4 0 CF R63.1211(b) ] Th e followin g record s mus t b e retaine di n th e operatin g record : Referenc e Document, Data , orInformatio n 63.1200 , 63.10(b ) an d(c ) General
. Informatio n require dt o documen t an dmaintai n complianc e wit hth e regulation s o f

Subpart EEE , includin g dat arecorde db y continuou s monitorin g system s (CMS) , an dcopie s o f al l notifications , reports , plans , an dother document s submitte dt o th e Administrator
. 63.1206(b)(l)(ii ) I f th e facilit y elect s t o compl y wit hal l applicabl e requirement s an dstandard s promulgate dunde r

authority o f

th e Clea n Ai r

Act , includin g Section s 11 2 an d129 , i nlie u o f th e requirement s o f

Subpart EE Ewhe n no t

burnin g hazardou s waste , i t mus t documen t

i n th e operatin g recor dtha t i t i s i n complianc e wit hthos e requirements
. 63.1206(b)(5)(h ) Documentatio n tha t achang e wil l no t

adversel y affec t

complianc e wit hth e emissio n standard s o r

operatin g requirements
. 63.1206(b)(ll ) Calculatio n o f hazardou s wast e residenc e time
. 63.1206(c)(2 ) Startup , shutdown , an dmalfunctio n plan
.
4 2Reference Document, Data , o rInformatio n

63.1206(c)(2)(v)(A ) Documentatio n o f th e facility' s investigatio n an devaluatio n o f excessiv e exceedance s durin g malfunctions
. 63.1206(c)(3)(v ) Correctiv e measure s fo r an y automati c waste fee dcutoff that results i n a n exceedanc e o f

a n emissio n standar do r operatin g paramete r

limit
. 63.1206(c)(3)(vii ) Documentatio n an dresults o f the automati c waste fee dcutoff operabilit y testing
. 63.1206(c)(4)(ii ) Emergenc y safet y ven t operatin g plan
. 63.1206(c)(4)(iii ) Correctiv e measure s fo r an y emergenc y safet y ven t opening
. 63.1206(c)(5)(ii ) Metho duse dfo r contro l o f

combustio n syste mleaks
. 63.1206(c)(6 ) Operato r trainin g an dcertificatio n program . 63.1206(c)(7)(i)(D ) Operatio n an dmaintenanc e plan
. 63.1209(c)(2 ) Feedstreamanalysi s plan
. 63.1209(k)(6)(iii) , 63.1209(k)(7)(ii) , 63.1209(k)(9)(ii) , 63.1209(o)(4)(iii ) Documentatio n that asubstitut e activate dcarbon , dioxin/fura n formatio n reactio n inhibitor , o r

dr y scrubbe r

sorben t wil l provid e the same leve l o f contro l as the origina l material
. 63.1209(q ) Documentatio n o f change s i n mode s o f

operation
. 63.1211(c ) Documentatio n o f compliance
. Th e permitte e shal l maintai n al l record s fo r fiv e calenda r

year s an dmak e the mavailabl e a t al l time s fo r

inspectio n b y EPA , IEPA , loca l agencie s o r thei r dul y authorize d representative s i n accordanc e wit h4 0 CF R71.6(a)(3)(i)(B)
. G . Wast e Processin g Uni tRequirement s (MP-1 , MP- 2 an d LPR ) Materia l processin g involve s th e repackagin g o f soli dwast e materia l fro mlarge r container s suc ha s drum s an dtote s t o smalle r "charge " containers/boxe s fo r subsequen t

incineration
. Aqueou s o r

organi c fre e liquid s ma y als o b e present . A n iner t absorben t

i s use dt o fi x th e fre e liquid s t o facilitat e repackaging
. Volatil e organi c material s ma y b e emitte ddurin g materia l processin g i n MP- 1 an dMP-2
. Th e regulation s applicabl e t o th e emissio n unit s ar e liste dbelow
. A listin g o f an y non-applicabl e requirement s an dth e reason s fo r th e non applicabilit y ar e provide di n Appendi x B
. 1 . Visibl e Emission s Limitation s [3 5 IA C 212.123 ] Visibl e emission s fro meithe r MP- 1 o r

MP- 2 shal l no t

excee d30 % opacity , excep t that , fo r an y 8-on e minut e perio di n an y on e hour , th e opacit y ma y b e greate r tha n 30 % bu t les s tha n 60%>

, provide dtha t

th e opacit y greate r

tha n 60 % occur s a

t on e emissio n uni t limite dt o 3 time s withi n a24-hou r period
.

4 32 . Us e o f Organi c Materia l [3 5 IA C 219.301 ] Emissio n o f

organi c materia l fro mthes e emissio n unit s shal l no t excee d8 lb/hr
. I f

n o odo r nuisanc e exists , th e limitatio n shal l appl y onl y t o photochemicall y reactiv e material
. 3 . NESHA Pfo rOff-Sit e Wast e an d Recover y Operation s [4 0 CF R6

3 Subpar tDD ] Veoli ai s awast e managemen t operatio n tha t

receive s off-sit e materia l an di s regulate da s ahazardou s wast e treatment , storage , an ddisposa l facilit y (TSDF)
. Th e Nationa l Emissio n Standard s fo r Hazardou s Ai r

Pollutant s fro mOff-Sit e Wast e an dRecover y Operation s ar e applicabl e t o th e MP- 1 an dMP- 2 operation s a t th e facility
. A s require di n 4 0 CF R63.683(b)(1)(f) an d63.688(a) , Veoli acontrol s ai r emission s fro mth e container s processe di n thes e wast e managemen t unit s b y followin g th e standard s fo r Containe r Leve l 1 control s specifie di n 4 0 CF R63.92 2 fo r Containers
. 4 . NESHA Pfo rContainer s [4 0 CF R63.922 ] Acontaine r

usin g Containe r

Leve l 1 control s i s on e o f th e following :
a . A containe r

tha t meet s th e applicabl e U.S
. Departmen t o f Transportatio n (DOT ) regulation s o n packagin g hazardou s material s fo r transportatio n a s specifie di n 4 0 C F R63.922(f)
. b
. A containe r

equippe dwit hacove r an dclosur e device s tha t for macontinuou s barrie r ove r th e containe r

opening s suc htha t

whe n th e cove r

an dclosur e device s ar e secure di n th e close dpositio n ther e ar e n o visibl e holes , gaps , o r othe r ope n space s int o th e interio r o f th e container
. Th e cove r ma y b e aseparat e cove r installe do n th e containe r (e.g. , ali do n adrum , asuitabl y secure dtar p o n aroll

of f box ) o r

ma y b e a n integra l par t o f th e containe r

structura l desig n (e.g. , abul k carg o containe r

equippe dwit hascrew-typ e cap)
. c . A n open-to p containe r i n whic ha n organi c vapor-suppressin g barrie r i s place do n o r ove r th e regulate dmateria l i n th e containe r suc htha t

n o regulate dmateria l i s expose dt o th e atmosphere
. On e exampl e o f suc habarrie r

i s applicatio n o f suitabl e organi c vapo r suppressin g foam
. d
. A containe r

use dt o mee t

th e requirement s o f eithe r paragrap h4 0 CF R 63.922(b)(2 ) o r

(b)(3 ) shal l b e equippe dwit hcover s an dclosur e devices , a s applicabl e t o th e container , tha t ar e compose do f

suitabl e material s t o minimiz e exposur e o f

th e regulate dmateria l t o th e atmospher e an dt o maintai n the equipmen t

integrit y fo r

a s lon g a s i t

i s i n service
. Factor s t o b e considere dwhe n selectin g th e material s fo r an ddesignin g th e cove r an dclosur e device s shal l include : organi c vapo r permeability ; th e effect s o f contac t wit hth e materia l o r it s vapo r manage di n th e container ; th e effect s o f outdoo r

exposur e t o wind , moisture , an dsunlight ; an dth e operatin g practice s use dfo r containe r

o n whic h th e cove r

i s installed
. Wheneve r aregulate dmateria l i s i n acontaine r usin g Containe r

Leve l 1 controls , th e owne r o r operato r

shal l instal l al l cover s an d closur e device s fo r

th e container , an dsecur e an dmaintai n eac hclosur e devic e i n th e close dpositio n excep t a s describe di n 4 0 CF R63.922(d)(1 ) throug h(d)(5)
.
4 4Th e owne r o r operato r shal l inspec t

container s usin g Containe r Leve l 1 control s i n accordanc e wit hth e procedure s specifie di n 4 0 CF R63.926(a)
. 5 . NESHA Pfo rContainer s [4 0 CF R63.925 an d 4 0 CF R71.6(a)(3)(i)(A) ] T o determin e tha t

ther e ar e n o detectabl e organi c emission s fo r th e purpos e o f

complyin g wit h4 0 CF R6 3 Subpar t PP , th e facilit y shal l conduc t ates t annuall y i n accordanc e wit h th e procedure s specifie di n Metho d2 1 o f 4 0 CFR
. Par t

60 , Appendi x A an d4 0 CF R 63.925
. Eac hpotentia l lea k interfac e (i.e. , alocatio n wher e organi c vapo r leakag e coul d occur ) o n th e cove r

an dassociate dclosur e device s shal l b e checke dannually
. Th e tes t shal l b e performe dwhe n amateria l havin g atota l organi c concentratio n representativ e o f th e rang e o f

concentration s fo r

th e material s expecte dt o b e manage di n th e unit s i s i n th e containers
. 6 . NESHA Pfo rContainer s [4 0 CF R71.6(a)(3) ]

• Th e facilit y shal l promptl y notif y th e permittin g authorit y o f deviation s o f

th e affecte dwast e processin g unit s wit hth e permi t requirements , pursuan t t o 4 0 CF R 71.6(a)(3)(iii)(B)
. Report s shal l describ e th e probabl e caus e o f suc hdeviations , an d an y correctiv e action s o r preventiv e measure s taken
. • Th e facilit y shal l maintai n th e record s o f eac hvisua l inspection , visibl e emissio n observation , finding s o f an y investigatio n required , an dresult s o f an y Metho d9 observatio n conducted
. • Th e record s shal l includ e th e date , time , typ e o f investigatio n conducted , an dtyp e o f correctiv e action s a s applicable
. 7 . NESHA Pfo rBenzen e Wast e Operation s [4 0 CF R6 1 Subpar tFF ] Veoli aoperate s ahazardou s wast e TS D facilit y tha t manage s benzene-containin g hazardou s wast e a s regulate db y thi s subpart
. Container s o f benzene-containin g wast e ar e processe di n MP- 1 an dMP- 2 followin g standar dwor k practice s tha t

addres s th e provision s o f

4 0 CF R61.345
. 8 . Emissio n Calculatio n Requirement s [4 0 CF R71.6(a)(3)(i)(B) ] VOM/HA Pemission s fro munit s MP1 , MP2 , an dth e labpac k shal l b e calculate dbase d o nth e mos t

recen t versio n o f

th e TANK S program . H . Liqui d Wast e Storag e Tan kRequirement s Bul k liqui dwaste s ar e store di n Tan k Far m# 1 an dTan k

Far m#3
. Al l tank s ar e vertical , fixed-roo f

tanks
. Tan k

Far m# 1 supplie s liqui dwast e t o Uni t 2 an dUni t

3 incinerators
. Tan k Far m#

3 supplie s liqui dwast e t o Uni t 4 incinerator
. Th e regulation s applicabl e t o th e emissio n unit s ar e liste dbelow
. A listin g o f an y non-applicabl e requirement s an dth e reason s fo r th e non-applicabilit y ar e provide di n Appendi x B
.

4 51 . Us e o f Organi c Materia l [3 5 IA C 219.301 ] Emissio n o f

organi c materia l fro mthes e emissio n unit s shal l no t excee d8 lb/hr
. I f

n o odo r nuisanc e exists , th e limitatio n shal l appl y onl y t o photochemicall y reactiv e material
. 2 . Organi c Materia l Emissio n fro m Pump s an d Compressor s [3 5 IA C 219.142 ] N o perso n shal l caus e o r allo w th e discharg e o f mor e tha n 32. 8 m l ( 2 c u in ) o f VO Lwit h vapo r pressur e o f

17.2 4 kP a(2. 5 psia ) o r greate r a t 294.3° K

(70°F ) int o th e atmospher e fro man y pum p o r

compresso r

i n an y 15-minut e perio da t standar dconditions
. 3 . Standard s o f

Performanc e fo rVolatil e Organi c Liqui d Storag e Vessel s (includin g petroleu m liqui d storag e vessels ) fo rwhic h Construction , Reconstruction , o rModificatio n Commence d Afte rJul y 23,198 4 [4 0 CF R6

0 Subpar tKb ] Th e facilit y shal l equi p th e applicabl e tan k wit hacontro l metho da s liste di n 4 0 CF R 60.112b
. Th e requirement s o f thi s regulatio n appl y t o Organi c Liqui dStorag e Tank s #300 , #302 , #304 , #306 , #308 , an d#310 , al l o f whic hhav e capacit y greate r tha n 7 5 cubi c meter s (19,81 3 gallons)
. Documentatio n an drecord s a s describe di n 4 0 CF R60.115b(c ) shal l b e retaine do n site
. 4 . Storag e Tank s [3 5 IA C 219.122 an d 129] Eac haffecte dliqui dwast e storag e tan k i s subjec t

t o 3 5 IA C 219.129(f ) an d3 5 IA C 219.122(b)
.

• Th e Permitte e shal l maintai n readil y accessibl e record s o f th e dimensio n an d analysi s o f

th e capacit y o f

eac haffecte dliqui dwast e storag e tank
. • Eac haffecte dliqui dwast e storag e tan k shoul db e equippe dwit hapermanen t submerge dloadin g pipe
. 5 . NESHA Pfo rBenzen e Wast e Operation s [4 0 CF R6 1 Subpar tFF ] Veoli aoperate s ahazardou s wast e TS D facilit y tha t manage s benzene-containin g hazardou s wast e a s regulate db y thi s subpart
. Tank s containin g benzen e wast e mus t b e designe dan doperate da s describe di n 4 0 CF R61.34 3 an d61.349
. Documentatio n an d record s a s describe di n 4 0 CF R61.35 6 shal l b e retaine do n site
. 6 . NESHA Pfo rOff-Sit e Wast e an d Recover y Operation s [4 0 CF R6

3 Subpar tDD ] Veoli ai s awast e managemen t operatio n tha t

receive s off-sit e materia l an di s regulate da s ahazardou s wast e TS D facility
. Th e Nationa l Emissio n Standard s fo r Hazardou s Ai r Pollutant s fro mOff-Sit e Wast e an dRecover y Operation s i s applicabl e t o th e liqui dwast e storag e tank s whe n onl y non-benzen e wast e i s stored
. Th e provision s o f 4 0 CF R 63.683(b)(2)(i ) exempt s th e tank s fro mth e contro l requirement s o f Subpar t D D i f suc h
4 6unit s ar e subjec t t o anothe r

subpar t o f 4 0 CF RPar t

6 3 o r par t 6 1 an dth e HA Pemission s ar e controlled
. Th e tank s ar e subjec t t o 4 0 CF R6 1 Subpar t F Ffo r benzene-containin g waste . 7 . Monitorin g an d Testin g [4 0 CF R71.6(a)(3)(i)(A ) an d (B) ] Th e facilit y shal l compl y wit hth e monitorin g requirement s establishe di n 4 0 CF R 61.354(d) , th e inspectio n requirement s i n 4 0 CF R61.349(f)-(g) , an dthe testin g requirement s o f

4 0 CF R61.349(c ) an d61.355(h)
. I f abreakthroug hdoe s no t occu r withi n 36 5 day s o f operatio n o n ahig hBt u tank , th e permitte e mus t

replac e th e carbon
. I f abreakthroug hdoe s no t occu r withi n 3 year s o f operatio n o n alo w Bt u tank , th e carbo n mus t b e replaced
. Th e presenc e an dconditio n o f th e submerge dloadin g pipe s fro mth e to p wil l b e observe d an ddocumente ddurin g th e quarterl y inspections ; wit haphysica l inspectio n ever y fiv e years . 8 . Recordkeepin g [4 0 CF R71.6(a)(3) ] Th e followin g record s mus t b e maintaine do n site :

• Tota l organi c liqui dwaste s processe di n gallon s pe r mont han dgallon s pe r year ;
• Averag e VOM/HA Pconten t o f receive dwastes , (percen t b y weight )

• Averag e vapo r

pressur e o f

receive dliqui dwastes ;
• Record s o f

th e siz e (capacity ) o f th e affecte dliqui dwaste s storag e tanks ; an d

• Record s o f

al l inspection s performed
. 9 . Organi c Materia l Emission s [C P#88030001 , Conditio n 3] Emission s o f

organi c materia l fro mTan k Far m# 3 shal l no t

excee d2. 5 tons/year
. I . Bul kSoli d Wast e Storag e Facilit y Requirement s Bul k soli dwast e i s store di n fou r pit s i n th e Bul k

Fee dBuilding
. A clamshel l move s soli d waste s fro mth e Bul k Fee dBuildin g t o th e Uni t 4 incinerator
. Th e buildin g i s equippe dwit h acyclone , abaghouse , an dacarbo n adsorptio n system . Th e regulation s applicabl e t o th e emissio n uni t

ar e liste dbelow
. A listin g o f an y non-applicabl e requirement s an dth e reason s fo r th e non-applicabilit y ar e provide di n Appendi x B
. 1 . Particulat e Emissio n fro m Proces s Unit s fo rwhic h Constructio n o rModificatio n Commence d o n o rAfte rApri l 14,197 2 [3 5 IA C 212.321 ] Th e facilit y shal l caus e o r allo w th e emissio n o f particulat e matte r

int o th e atmospher e i n an y on e hou r

perio dfro man y ne w proces s emissio n uni t which , eithe r

alon e o r

i n combinatio n wit hth e emissio n o f particulat e matte r

fro mal l othe r

simila r proces s
4 7emissio n unit s fo r whic hconstructio n o r modificatio n commence do n o r afte r Apri l 14 , 1972 , a t asourc e o r

premises , exceed s th e allowabl e emissio n rate s specifie di n subsectio n 3 5 IA C 212.321(c)
. 2 . Us e o f

Organi c Materia l [3 5 IA C 219.301 ] Emissio n o f

organi c materia l fro mthi s emissio n uni t shal l no t

excee d8 lb/h r

excep t a s allowe db y 3 5 IA C 219.302(b)
. I f n o odo r nuisanc e exists , th e limitatio n shal l appl y onl y t o photochemicall y reactiv e material
. 3 . Visibl e Emission s Limitation s [3 5 IA C 212.123 ] Visibl e emission s fro mth e uni t shal l no t

excee d30 % opacity , excep t that , fo r

an y eigh t one-minut e period s i n an y on e hour , th e opacit y ma y b e greate r tha n 30 % bu t

les s tha n 60%) , provide dtha t

th e opacit y greate r

tha n 60 % occur s a

t on e emissio n uni t

limite dt o 3 time s withi n a24-hou r period
. 4 . NESHA Pfo rBenzen e Wast e Operation s [4 0 CF R6 1 Subpar tFF ] Veoli aoperate s ahazardou s wast e TS D facilit y tha t manage s benzene-containin g hazardou s wast e a s regulate db y thi s subpart
. Thi s emissio n uni t i s define da s atan k withi n a n enclosure
. Unit s containin g benzen e wast e mus t b e designe dan doperate da s describe di n 4 0 CF R61.34 3 an d61.349
. Th e bul k

soli dwast e storag e facilit y mus t b e designe dan doperate di n accordanc e wit h th e criteri afo r

apermanen t

tota l enclosur e a s specifie di n "Procedur e T-Criteri afo r an d Verificatio n o f

apermanen t

o r Temporar y Tota l Enclosure " i n 4 0 CF R52.741 , Appendi x B
. A n averag e facia l velocit y o f a t leas t 20 0 ft/minut e flowin g int o th e enclosur e a t al l natura l draft

opening s mus t

b e maintained
. Annua l verificatio n testin g mus t b e performe di n accordanc e wit h4 0 CF R61.343(e)
. 5 . NESHA Pfo rOff-Sit e Wast e an d Recover y Operation s [4 0 CF R6

3 Subpar tDD ] Veoli ai s awast e managemen t operatio n tha t

receive s off-sit e materia l an di s regulate da s ahazardou s wast e TS D facility
. Th e Nationa l Emissio n Standard s fo r Hazardou s Ai r

Pollutant s fro mOff-Sit e Wast e an dRecover y Operation s i s applicabl e t o th e bul k

soli dwast e storag e facility
. Th e provision s o f 4 0 CF R63.683(b)(2)(i ) exempt s th e tank s fro mth e contro l requirement s o f Subpar t D D i f suc hunit s ar e subjec t t o anothe r

subpar t o f 4 0 CF RPar t

6 3 o r par t 6 1 an dth e HA P emission s ar e controlled
. Th e uni t

i s subjec t

t o 4 0 CF R6 1 Subpar t FF
. 6 . Wor kPractic e an d Operationa l Requirement s [4 0 CF R71.6(a)(1) ]

• Excep t

durin g time s whe n bul k soli dwaste s ar e unloade dint o th e pits , al l door s o f th e buildin g shal l b e close dan dal l operation s shal l b e enclose dinsid e th e building
.

4 8• Th e enclose dbuildin g wher e bul k soli dwast e i s accumulate dshal l b e operate dunde r permanen t

negativ e pressure . 7 . Monitorin g an d Testin g [4 0 CF R71.6(a)(3)(i)(A ) an d (B) ] Th e facilit y shal l compl y wit hth e monitorin g procedure s i n 4 0 CF R61.354(c) , th e inspectio n requirement s i n 4 0 CF R349 , an dth e testin g requirement s o f 4 0 CF R61.34 9 an d61.355(h)
. Avisua l surve y th e Bul k Fee dBuildin g shal l b e performe deac hda y fo r th e presenc e o f visibl e emission s o r fugitiv e emission s o f particulat e matter . I f visibl e emission s o r fugitiv e emission s o f particulat e matte r

ar e observe dth e followin g procedure s shal l b e followed :

• Immediately , upo n conclusio n o f th e visua l observation , investigat e th e sourc e an d reaso n fo r

th e presenc e o f

visibl e emission s o r

fugitiv e emissions ; an d

• A s soo n a s practicable , tak e appropriat e correctiv e action
. I f th e correctiv e action s undertake n d o no t eliminat e th e visibl e o r fugitiv e emissions , a Metho d9 tes t

shal l b e conducte dwithi n 2 4 hour s o f th e initia l survey . I f an y o f th e visibl e emission s observation s indicat e visibl e emission s greate r tha n 20 % opacity , th e Permitte e shal l conduc t dail y visibl e emission s observations , fo r thirt y minutes , o f

th e emissio n poin t

i n questio n unti l tw o consecutiv e dail y observation s indicat e visibl e emission s o f

20%opacit y o r

less
. I f

th e Metho d9 visibl e emission s observation , o r i f tw o consecutiv e dail y observations , indicat e visibl e emission s o f 20 % opacit y o r

less , th e Permitte e shal l conduc t weekl y visibl e emission s observation s o f th e emissio n poin t

fo r thre e additiona l weeks
. 8 . Recordkeepin g an d Reportin g [4 0 CF R71.6(a)(3) ] Record s a s describe di n 4 0 CF R61.356(f ) - (j ) an d(n ) shal l b e maintaine do n site
. I naddition , th e followin g record s wil l b e maintaine do n site :

• Amoun t

o f accepte dsoli dwastes , i n ton s pe r mont han dton s pe r

year . • A lo g o f

maintenanc e an drepai r o f ai r pollutio n contro l device s wit hth e date s o f service/repai r

made , an dinspectio n conducted
. • Record s o f

th e pressur e bein g maintaine dinsid e th e building
. • Monthl y an dannua l VOM/HA Pemissions
. Detail s o f eac hvisua l surve y o r visibl e emission s observation , includin g date , time , observe r an dresult s fo r

eac hemissio n uni t an dan y othe r

pollutan t

emittin g activity
. • Date , time , an dtyp e o f an y investigatio n conducted
. • Finding s o f

th e investigation , includin g th e reason s fo r th e presenc e o f

visibl e emission s o r

fugitiv e emission s o f particulat e matter . • Date , time , an dtyp e o f correctiv e action s taken
.

4 9• Result s o f an y Metho d9 visibl e emission s observation s conducte do n th e sourc e o f visibl e o r

fugitiv e emissions
. J . Dru m Crushe rRequirement s Drum s tha t

ar e unsuitabl e fo r

reus e ar e crushe db y thi s emissio n unit
. Th e regulation s applicabl e t o th e emissio n uni t ar e liste dbelow
. A listin g o f an y non-applicabl e requirement s an dth e reason s fo r

th e non-applicabilit y ar e provide di n Appendi x B
. 1 . Us e o f

Organi c Materia l [3 5 IA C 219.301 ] Emissio n o f

organi c materia l fro mthi s emissio n uni t shal l no t

excee d8 lb/hr
. I f

n o odo r nuisanc e exists , th e limitatio n shal l appl y onl y t o photochemicall y reactiv e material
. 2 . Particulat e Matte rLimitatio n [3 5 IA C 219.321 ] Th e emissio n o f

particulat e matte r

int o th e atmospher e i n an y one-hou r perio dfro man y ne w proces s emissio n unit , eithe r alon e o r

i n combinatio n wit hth e emissio n o f particulat e matte r fro mal l othe r

simila r

proces s emissio n unit s fo r whic hconstructio n o r modificatio n commence do n o r afte r Apri l 14 , 197 2 a

t asourc e o r

premises , shal l no t excee dth e allowabl e emissio n rate s specifie di n subsectio n (c ) o f 3 5 IA C 212.321
. 3 . Visibl e Emission s Limitation s [3 5 IA C 212.123 ] Emissio n o f

smok e o r

othe r particulat e matte r

shal l no t

excee da n opacit y greate r tha n 30%t , int o th e atmospher e fro man y emissio n source , excep t a s allowe db y 3 5 IA C 212.123(b ) an d212.124
. 4 . Monitorin g an d Testin g [4 0 CF R71.6(a)(3)(i)(A ) an d (B) ] Avisua l surve y o f

th e dru mcrushe r

shal l b e performe deac hda y fo r th e presenc e o f visibl e emission s o r fugitiv e emission s o f particulat e matter . I f th e observation s conducte didentif y an y visibl e emission s o r fugitiv e emission s o f particulat e matter , th e facilit y shall :

• Immediately , upo n conclusio n o f th e visua l observation , investigat e th e sourc e an dreaso n fo r

th e presenc e o f

visibl e emission s o r

fugitiv e emissions ; an d

• A s soo n a s practicable , tak e appropriat e correctiv e action
. I f th e correctiv e action s undertake n d o no t eliminat e th e visibl e o r fugitiv e emissions , th e facilit y shall , withi n 2 4 hour s o f th e initia l survey , conduc t ates t usin g EP A Referenc e Metho d9 (se e 4 0 CF Rpar t 60 , appendi x A)
. I f an y o f th e visibl e emission s observation s indicat e visibl e emission s greate r tha n 20 % opacity , aMetho d9 visibl e emission s observatio n shal l b e conducte do f th e emissio n poin t

i n questio n fo r

thirt y minute s eac h day , unti l tw o consecutiv e dail y observation s indicat e visibl e emission s o f 20% > opacit y o r less
. I f

th e Metho d9 visibl e emission s observatio n o r i f tw o consecutiv e dail y
5 0observation s indicat e visibl e emission s o f 20 % opacit y o r

less , th e facilit y shal l conduc t weekl y visibl e emission s observation s o f th e emissio n poin t

fo r thre e additiona l weeks
. 5 . Recordkeepin g an d Reportin g [4 0 CF R71.6(a)(3) ]

• Record s o f

th e tota l numbe r

o f drum s crushe d(drums/hou r an ddrums/year ) fo r th e dru mcrushe r

shal l b e maintaine dpursuan t t o 4 0 C.F.R
. § 71.6(a)(i)(3)(B)
. • Th e facilit y shal l calculat e an dkee p record s o f VO M emission s fro mth e dru m crushe r base do n th e emissio n facto r equa l t o 0.022 1 l b VOM/ 1 dru mcrushed
. Thi s emissio n facto r

i s base do n acharacterizatio n o f th e dru mresidu e a s containin g th e mos t prevalen t

organic s a

t th e concentration s presen t i n th e wast e receive ddurin g 200 7 - 2011
. Th e maximu mdru mcrushin g rat e i s 4 0 drum s pe r hour
. • Record s o f

th e fugitiv e emission s shal l b e maintaine dincluding : detail s o f eac h visua l surve y o r

visibl e emission s observation , includin g date , time , nam e o f observe r an dresult s fo r

eac hemissio n uni t

an dan y othe r

pollutan t

emittin g activit y an ddate , tim e an dtyp e o f

an y investigatio n conducted
. K . Boile rRequirement s On e 10.4 6 millio nBt u pe r hou r natura l gas-fire dboile r i s locate don-site
. Th e existin g boile r supplie s hea t

an dstea mt o th e facility
. Th e regulation s applicabl e t o th e existin g emissio n uni t ar e liste dbelow
. A listin g o f an y non-applicabl e requirement s an dth e reason s fo r th e non-applicabilit y ar e provide di n Appendi x B
. 1 . Fue l Combustio n Emissio n Source s ( > 1 0 MMBtu/hr ) [3

5 IA C 216.121 ] Carbo n monoxid e emission s fro mthi s emissio n uni t shal l no t

excee d20 0 pp mcorrecte d t o 50 % exces s air
. 2 . Standard s o f

Performanc e fo rSmal l Industrial-Commercial-Institutiona l Stea m Generatin g Unit s [4 0 CF R6

0 Subpar tDc ] Th e facilit y shal l recor dan dmaintai n record s o f th e amoun t

o f fue l combuste ddurin g eac hday
. Th e owne r o r operato r

o f a n affecte dfacilit y tha t onl y burn s ver y lo w sulfu r fue l oi l o r

othe r liqui do r

gaseou s fuel s wit hpotentia l sulfu r dioxid e emission s rat e o f 14 0 ng/ J (0.3 2 lb/MMBtu ) hea t inpu t o r les s shal l recor dan dmaintai n record s o f th e fuel s combuste ddurin g eac hcalenda r month
. 3 . Visibl e Emission s Limitation s [3 5 IA C 212.123 ] Emissio n o f

smok e o r

othe r particulat e matte r

shal l no t

excee da n opacit y greate r tha n 30%o , int o th e atmospher e fro man y emissio n source , excep t a s allowe db y 3 5 IA C 212.123(b ) an d212.124
.

5 14 . Emissio n an d Operationa l Limitation s [CP #95080025 ] Emission s an doperatio n o f thi s boile r

shal l no t

excee dth e followin g limits : Operatin g Hour s = 8,76 0 N O x 1.4 6 lb/hr , 6.4 1 ton/y r C02. 1 lb/hr , 9. 2 ton/y r Fue l = Natura l Ga s onl y a t maximu mo f

7. 6 mmscf/mont han d91. 1 mmscf/year
. Thes e limit s ar e base dupo n th e maximu mfirin g rat e fo r th e boiler , an dstandar d emissio n factors / 5 . Emissio n Limitation s [4 0 CF R63.52 ] Emission s o f

C O fro mth e boile r

shal l no t

excee d10 0 pp mb y volum e o n adr y basi s correcte dt o 3% t

oxygen . 6 . NESHA PMajo rSources : Industrial , Commercia l An d Institutiona l Boiler s an d Proces s Heater s [4

0 CF R6

3 Subpar tDDDDD ] Boile r # 1 mus t

mee t th e wor k

practic e standard s liste dbelow
.

• Performanc e o f

a n annua l tune-u p addressin g al l regulate demissions
. Th e tune-u p shal l includ e th e followin g a s describe di n 4 0 CF R63.7540(10) : 1
. Inspectio n o f

th e burner , th e flam e pattern , an dth e air-to-fue l rati o control s fo r operatio n i n accordanc e wit hmanufacturer' s specification s an d performanc e o f

adjustment s a s necessary . 2
. Optimizatio n o f

tota l C O emission s i n coordinatio n wit hNO x limitations
. 3
. Measuremen t

o f C O concentration s an doxyge n concentratio n i n th e boile r exhaust
. 4
. Productio n o f

awritte n repor t

documentin g C O concentrations , correctiv e actions , an dth e amoun t o f fue l combuste ddurin g th e year . • Performanc e o f

aone-tim e energ y assessmen t b y aqualifie denerg y assessor . • Submissio n o f

aNotificatio n o f

Complianc e Statu s withi n 6 0 day s o f th e initia l tune
up . Th e applicabl e informatio n liste di n 4 0 CF R63.7545(e)(1 ) throug h(8 ) mus t b e provide di n th e Notificatio n o f Complianc e Status
. • Submissio n o f

a n Annua l Complianc e Repor t a s describe di n 4 0 CF R63.755 0 b y Januar y 31 s t

o f eac hyear . 7 . Monitorin g an d Testin g [4 0 CF R71.6(a)(3)(i)(A ) an d (B) ]

• A n annua l Metho d9 tes t t o ensur e complianc e wit hth e opacit y limi t shal l b e performed
. • A n annua l tune-u p i n accordanc e wit h4 0 CF R63.754 0 shal l b e performed
.

5 28 . Recordkeepin g an d Reportin g [4 0 CF R71.6(a)(3 ) an d 4 0 CF R63.7550(b ) an d 40 CF R63.7555 ] Th e followin g record s mus t b e maintaine do n site :

• Monthl y record s o f natura l ga s usage . • Annua l record s o f natura l ga s usag e (millio n squar e cubi c fee t pe r year . • Record s o f

th e result s o f

th e annua l tune-up . • Documentatio n o f th e one-tim e energ y assessment . A nannua l complianc e repor t mus t b e submitte dwhic hcontains :

• Compan y an dfacilit y nam e an daddress
. • Proces s uni t

information
. • Statemen t

b y aresponsibl e officia l wit htha t official' s name , title , an dsignature , certifyin g th e truth , accuracy , an dcompletenes s o f th e conten t

o f th e report . • Dat e o f

repor t an dbeginnin g an dendin g date s o f th e reportin g period
. • Th e tota l fue l us e b y th e boiler , fo r eac hcalenda r

mont hwithi n th e annua l reportin g period , including
. • Dat e o f

th e mos t

recen t tune-u p an dburne r

inspection
. • Th e dat e an dduratio n o f th e boile r

startup , shutdown , and/o r malfunctio n event s durin g th e reportin g period
. L . Emergenc y Generato rRequirement s Tw o emergenc y generator s ar e locate da t th e facility
. The y ar e stationar y reciprocatin g interna l combustio n engine s (RICE ) wit hasit e ratin g o f les s tha n 50 0 brak e H P use donl y fo r emergenc y purpose s tha t operat e a

t amajo r sourc e o f

HA Pemissions
. 1 . NESHA Pfo rStationar y Reciprocatin g Interna l Combustio n Engine s [4 0 CF R 6 3 Subpar tZZZZ ] Th e emergenc y RIC Emus t compl y wit hth e requirement s o f 4 0 CF R63.6640(f ) i n orde r t o b e considere demergenc y stationar y RICE
. Thes e requirement s ar e liste dbelow
.

• Fo r owner s an doperator s o f emergenc y engines , an y operatio n othe r tha n emergenc y operation , maintenance , an dtesting , an doperatio n i n nonemergenc y situation s fo r 5 0 hour s pe r

year , a s permitte di n thi s section , i s prohibited
. • Ther e i s n o tim e limi t o n th e us e o f

emergenc y stationar y RIC Ei n emergenc y situations
. • Th e emergenc y stationar y RIC Ema y b e operate dfo r th e purpos e o f

maintenanc e check s an dreadines s testing , provide dtha t th e test s ar e recommende db y federal , state , o r loca l government ; th e manufacturer ; th e vendor ; o r th e insuranc e compan y associate dwit hth e engine
. Maintenanc e check s an dreadines s testin g o f suc hunit s i s limite dt o 10 0 hour s pe r year . Th e owne r

o r operato r

ma y petitio n th e Administrato r fo r approva l o f

additiona l hour s t o b e use dfo r maintenanc e check s an dreadines s 5 3testing , bu t apetitio n i s no t

require di f

th e owne r

o r operato r

maintain s record s indicatin g tha t

federal , state , o r

loca l standard s requir e maintenanc e an dtestin g o f emergenc y RIC Ebeyon d10 0 hour s pe r year . • Th e emergenc y stationar y RIC Ema y b e operate du p t o 5 0 hour s pe r yea r i n non emergenc y situations , bu t thos e 5 0 hour s ar e counte dtowar dth e 10 0 hour s pe r yea r provide dfo r

maintenanc e an dtesting
. Th e 5 0 hour s pe r yea r fo r non-emergenc y situation s canno t

b e use dfo r

pea k shavin g o r

t o generat e incom e fo r afacilit y t o suppl y powe r

t o a n electri c gri do r otherwis e suppl y powe r a s par t o f afinancia l arrangemen t

wit hanothe r

entity ; excep t

tha t owner s an doperator s ma y operat e th e emergenc y engin e fo r amaximu mo f

1 5 hour s pe r

yea r a s par t o f ademan drespons e progra mi f

th e regiona l transmissio n organizatio n o r equivalen t

balancin g authorit y an dtransmissio n operato r ha s determine dther e ar e emergenc y condition s tha t coul d lea dt o apotentia l electrica l blackout , suc ha s unusuall y lo w frequency , equipmen t overload , capacit y o r energ y deficiency , o r unacceptabl e voltag e level
. Th e engin e ma y no t b e operate dfo r

mor e tha n 3 0 minute s prio r t o th e tim e whe n th e emergenc y conditio n i s expecte dt o occur , an dth e engin e operatio n mus t b e terminate d immediatel y afte r

th e facilit y i s notifie dtha t th e emergenc y conditio n i s n o longe r imminent
. Th e 1 5 hour s pe r yea r o f deman drespons e operatio n ar e counte da s par t o f th e 5 0 hour s o f

operatio n pe r

yea r provide dfo r

nonemergenc y situations
. Th e suppl y o f emergenc y powe r

t o anothe r

entit y o r

entitie s pursuan t

t o financia l arrangemen t i s no t limite db y thi s paragrap h(f)(4) , a s lon g a s th e powe r provide db y th e financia l arrangemen t

i s limite dt o emergenc y power . 2 . Wor kPractic e Standard s [4 0 CF R63.6602) ] Eac hemergenc y RIC Emus t compl y wit hth e followin g requirements
. Durin g norma l operations :

• Chang e oi l an dfilte r ever y 50 0 hour s o f

operatio n o r

annually , whicheve r come s first ;
• Inspec t

ai r cleane r ever y 1,00 0 hour s o f operatio n o r

annually , whicheve r come s first ;
• Inspec t

al l hose s an dbelt s ever y 50 0 hour s o f operatio n o r

annually , whicheve r come s first , an dreplac e a s necessary . • Durin g startup , minimiz e th e engine' s tim e spen t a t idl e an dminimiz e th e engine' s startu p tim e a

t startu p t o aperio dneede dfo r appropriat e an dsafe loadin g o f th e engine , no t

t o excee d3 0 minutes , afte r whic htim e th e non-startu p emissio n limitation s apply
. Operat e an dmaintai n th e stationar y RIC Ean dafter-treatmen t contro l devic e (i f

any ) accordin g t o th e manufacturer' s emission-relate dwritte n instruction s o r develo p an d follo w th e facility' s ow n maintenanc e plan , whic hmus t provide , t o th e exten t practicable , fo r th e maintenanc e an doperatio n o f th e engin e i n amanne r consisten t

wit hgoo dai r pollutio n contro l practic e fo r minimizin g emissions
. Instal l anon-resettabl e hou r mete r i f on e i s no t

alread y installed
.

5 43 . Recordkeepin g an d Reportin g [4 0 CF R63.6655 ] Maintai n th e followin g records :

• Descriptio n o f

eac hmalfunctio n o f

operation/monitorin g equipment ;
• Descriptio n o f

al l maintenanc e performed ;
• Descriptio n o f

action s take n durin g malfunctio n t o minimiz e emissions ;
• Descriptio n o f

correctiv e actions ;
• Lis t o f maintenanc e conducte dt o demonstrat e tha t RIC Ewa s operate dan d maintaine di n accordanc e wit hth e maintenanc e plan/manufacturer' s recommendations ;
• Th e hour s o f

operatio n a s monitore db y th e non-resettabl e hou r meter ; an d

• Descriptio n o f

purpos e o f

operatio n hour s spent . Source s mus t

repor t an y failur e t o perfor mth e wor k practice s o n th e require dschedule
. M . Gasolin e Storag e Tank s 1 . Storag e o f

Gasolin e [3

5 IA C 219.122 ] Th e loadin g o f

an y organi c materia l i n an y stationar y tan k havin g astorag e capacit y o f greate r tha n 94 6 liter s (25 0 gallons ) shal l no t b e allowed , unles s suc htan k i s equippe d wit hapermanen t

submerge dloadin g pip e o r a n equivalen t

devic e approve db y th e Agenc y accordin g t o th e provision s o f 3 5 IA C 201 , an dfurthe r processe dconsisten t

wit h 3 5 IA C 219.108 , o r

unles s suc htan k

i s apressur e tan k

a s describe di n 3 5 IA C 219,12 1 (a ) o r i t fitte dwit harecover y syste ma s describe di n 3 5 IA C 219.121(b)(2)
. 2 . Gasolin e Dispensin g Operation s [3 5 IA C 219.583 ] Th e transfe r

o f gasolin e fro man y deliver y vesse l int o th e stationar y storag e tan k a t a gasolin e dispensin g operation s shal l no t b e allowe dunles s th e tan k i s equippe dwit ha submerge dloadin g pipe
. 3 . Recordkeepin g an d Reportin g [4 0 CF R71.6(a)(3) ] Record s retaine dfo r th e storag e tan k

includ e desig n informatio n o n th e capacit y o f th e tan k an ddocument s tha t confir mth e presenc e o f apermanen t

submerge dloadin g pipe
. I n addition , a n inspection , maintenance , an drepai r lo g o r othe r record s fo r

th e storag e tan k shal l b e maintaine dthat , a t aminimum , include s informatio n relate dt o an y repai r o r replacemen t

o f th e submerge dloadin g pipe
.

5 5

## AI REMISSION S INFORMATIO N A . Insignifican tAi rEmissio n Source s Thi s sectio n identifie s an ddescribe s th e insignifican t activitie s a

t th e Veoli afacility
. Th e tabl e belo w contain s alis t o f th e insignifican t

activitie s an dth e regulator y referenc e tha t exempt s the mfro mpermittin g requirements
. Insignifican tEmissio n Unit s Insignifican tEmissio n Unit s Regulator y Citatio n 2. 5 mmBtu/h r

Tiog aportabl e boile r 3 5 IA C 27 0 Sectio n 201.210(a)(4 ) Horizonta l 550-gallo n tan k (Kerosene ) 3 5 IA C 27 0 Sectio n 201.210(a)(ll ) Horizonta l 550-gallo n tan k (No
. 2 fue l oil ) 3 5 IA C 27 0 Sectio n 201.210(a)(ll ) Horizonta l 550-gallo n tan k (Gasoline ) 3 5 IA C 27 0 Sectio n 201.210(a)(ll ) Horizonta l 550-gallo n tan k (No
. 2 fue l oil ) 3 5 IA C 27 0 Sectio n 201.210(a)( l 1 ) A s hHandlin g Se e Belo w Explanatio n Handlin g o f

spen t dr y scrubbe r

solid s (DSS ) Se e Belo w Explanatio n Lim e unloadin g (silo ) an dproportionin g Se e Belo w Explanatio n Gasolin e storag e an ddispensin g Se e Belo w Explanatio n Us e o f absorben t

(fugitiv e particulat e generation ) Se e Belo w Explanatio n Genera l Vehicl e maintenanc e an dservicing , assume dt o includ e diese l fue l handlin g 3 5 IA C 27 0 Sectio n 201.210(b)(4 ) Laborator y (chemica l an dphysica l analysis ) 3 5 IA C 27 0 Sectio n 201.210(b)( l 1 ) Pipin g an dstorag e syste mfo r natura l ga s 3 5 IA C 27 0 Sectio n 201.210(b)(15 ) Non-halogenate dcol dcleanin g degreaser s 3 5 IA C 27 0 Sectio n 201.210(b)(19 ) Interna l combustio n engine s o f moto r vehicle s (primaril y forklifts ) 3 5 IA C 27 0 Sectio n 201.210(b)(24 ) Storag e an dhandlin g o f close ddrum s 3 5 IA C 27 0 Sectio n 201.210(b)(26 ) Th e as hhandling , handlin g o f spen t dr y scrubbe r

solid s (DSS) , lim e unloadin g (silo ) an d proportioning , gasolin e storag e an ddispensing , an dus e o f absorben t

(fugitiv e particulat e generation ) d o no t

emi t mor e tha n 1. 0 lb/h r o f an y regulate dai r

pollutan t

no t liste da s hazardou s pursuan t

t o Sectio n 112(b ) o f th e CA A i n th e absenc e o f ai r pollutio n contro l equipment
. The y d o no t emi t mor e tha n 0. 1 lb/h r

o f an y regulate dai r

pollutan t

tha t i s liste d a s hazardou s pursuan t t o Sectio n 112(b ) o f th e CA Ai n th e absenc e o f ai r pollutio n contro l equipment ; an dnon e ar e proces s units
.

5 6B . Lis to f Ai rEmissio n Source s wit h Regulator y Requirement s Uni tNam e Uni tDescriptio n Incineratio n Uni t

2 Fixe dHeart hIncineratio n Uni t use di n th e destructio n o f hazardou s wast e Incineratio n Uni t

3 Fixe dHeart hIncineratio n Uni t use di n th e destructio n o f hazardou s wast e Incineratio n Uni t

4 Rotar y Kil nIncinerato r (Transportable ) use di n th e destructio n o f

hazardou s wast e Materia l Processin g Are a1 Materia l processing/repackaging , repackagin g o f containerize dsoli dwast e Materia l Processin g Are a2 Materia l processing/repackaging , repackagin g o f containerize dsoli dwast e La b Pac k

Repac k Materia l processing/repackaging , repackagin g o f La b Pack s Dru mCrushe r Drum s ar e crushe d Bul k Fee dBuildin g Temporar y storag e o f bul k soli dwaste s befor e bein g fee d t o Uni t 4 Boile r 1 Stea mBoile r use dfo r

stea mgeneratio n a

t plan t Tan k # 2 4,931-gallo n tan k use dfo r

th e storag e o f

liqui dwast e Tan k # 4 4,931-gallo n tan k use dfo r

th e storag e o f

liqui dwast e Tan k #6 7,200-gallo n tan k use dfo r

th e storag e o f

liqui dwast e Tan k # 8 5,820-gallo n tan k use dfo r

th e storag e o f

liqui dwast e Tan k #1 0 12,869-gallo n tan k use dfo r

th e storag e o f

liqui dwast e Tan k #2 0 12,869-gallo n tan k use dfo r

th e storag e o f

liqui dwast e Tan k #3 0 12,869-gallo n tan k use dfo r

th e storag e o f

liqui dwast e Tan k #4 0 12,869-gallo n tan k use dfo r

th e storag e o f

liqui dwast e Tan k #5 0 12,869-gallo n tan k use dfo r

th e storag e o f

liqui dwast e Tan k #6 0 12,869-gallo n tan k use dfo r

th e storag e o f

liqui dwast e Tan k #30 0 19,850-gallo n tan k use dfo r

th e storag e o f

liqui dwast e Tan k #30 2 30,000-gallo n tan k use dfo r

th e storag e o f

liqui dwast e Tan k #30 4 30,000-gallo n tan k use dfo r

th e storag e o f

liqui dwast e Tan k #30 6 30,000-gallo n tan k use dfo r

th e storag e o f

liqui dwast e Tan k #30 8 30,000-gallo n tan k use dfo r

th e storag e o f

liqui dwast e Tan k #31 0 30,000-gallo n tan k use dfo r

th e storag e o f

liqui dwast e Tan k #31 2 10,000-gallo n tan k use dfo r

th e storag e o f

liqui dwast e Tan k #31 4 10,000-gallo n tan k use dfo r

th e storag e o f

liqui dwast e Tan k #39 0 30,000-gallo n tan k use dfo r

storag e o f

No
. 2 Diese l Fue l

5 7C . Emissio n Calculation s Th e followin g ar e th e emissio n calculation s fo r al l th e significan t

source s at

th e plant
. 1 . Uni t2 Incineratio n Th e actua l emission s an dpotentia l emission s fo r Uni t 2 ar e presente di n th e followin g table
. Th e basi s fo r eac h o f

th e emissio n rate s i s provide dalso
. Th e potentia l t o emi t (PTE ) wa s calculate dusin g emissio n testin g infonnation , permi t limits , an demissio n limitation s i n regulator y standard s an d8,76 0 hour s o f operation
. Uni t2 Emission s Summar y

Pollutan t Actua l

Emissio n Rat e (lbs/hr) Basi s of

Actua l Emissio n Rate PT E

(Lbs/hr ) PT E

(tons/yr ) PT E Basi s P M 0.064 0 12/200 9 CP T 0.577 5 2.5 3 Base don HWCMAC T Limit , 0.01 3 gr/dsc f P M 1 0 0.064 0 Same as P M 0.577 5 2.5 3 Base don HWCMAC T Limit , 0.01 3 gr/dsc f P M 2 . 5 0.064 0 Same as P M 0.577 5 2.5 3 Base do n HWCMAC T Limit , 0.01 3 gr/dsc f HC1/C1 2 0.561 2 12/200 9 CP T 0.911 7 3.9 9 Base don HWCMAC T Limit , 3 2 ppm

v N O x 2.5 1 200 7 stac k tes t No t

availabl e 4. 0 Constructio n permi t #8801000 1 C O 0.04 5 CEM S 2.3 1 6. 6 Base don HWCMAC T Limit , 10 0 ppm v Constructio n permit #8710002

4 V O M 0.4 3 Ma x Fee d& D R E 8. 0 0. 9 Constructio n permi t #8710002 4 

### so 2 4.0 0 0.1 % Tota l Fee d No t

availabl e 7. 7 Constructio n permi t #8710002

4 H g 0.000 8 8/200 8 CP T 0.002 6 0.011 4 Base do n HWCMAC T Limit , 130ug/m 3 A s 0.0000 2 9/200 8 CP T 0.001 8 0.008 1 Base don HWCMAC T Limit , 9 2 ug/m 3 B e 0.000001 7 9/200 8 CP T 0.001 8 0.008 1 Base don HWCMAC T Limit , 92 ug/m3 C d 0.00002 2 9/200 8 CP T 0.004 6 0.020 2 Base do n HWCMAC T Limit , 23 0 ug/m 3 C r 0.00006 9 9/200 8 CP T 0.001 8 0.008 1 Base do n HWCMAC T Limit , 9 2 ug/m 3 S b 0.0000034 2 6/200 2 stac k tes t 0.0000034 2 0.00001 5 6/200 2 stac k tes t P b 0.0002 8 9/200 8 CP T 0.004 6 0.020 2 Base don HWCMAC T Limit , 23 0 ug/m 3 N i 0.0000044 6 6/200 2 stac k tes t 0.0000044 6 0.00002 0 6/200 2 stac k tes t S e 0.0000085 4 6/200 2 stac k tes t 0.0000085 4 0.00003 7 6/200 2 stac k tes t Dioxin/Fura n n g TE Q 7 % 0 2 0.0017 8 6/201 2 Conf
. Tes t 4.3 8 x 10" 9 1.9 2 x 10
- 8 Base don HWCMAC T Limit , 0.2 0 ng/dscmTE Q

582 . Uni t3 Incineratio n Th e actua l emission s an dpotentia l emission s fo r Uni t 3 ar e presente di n th e followin g table
. Th e basi s fo r eac h o f

th e emissio n rate s i s provide dalso
. Th e PT E wa s calculate d usin g emissio n testin g information , permi t limits , an demissio n limitation s i n regulator y standard s an d8,76 0 hour s o f operation
. Uni t3 Emission s Summar y

Pollutan t Actua l

Emissio n Rat e (lbs/hr) Basi s o

f Actua l Emissio n Rate PT E (Lbs/hr ) PT E

(tons/yr ) PT E Basi s P M 0.070 8 12/200 9 CP T 0.577 5 2.5 3 Base don HWCMAC T Limit , 0.01 3 gr/dsc f P M 1 0 0.070 8 Same as P M 0.577 5 2
. 5 3 Basedo n HWCMAC T Limit , 0.01 3 gr/dsc f P M 2 . 5 0.070 8 Same as P M 0.577 5 2.5 3 Basedon HWCMAC T Limit , 0.01 3 gr/dsc f HC1/C1 2 0.398 9 12/200 9 CP T 0.934 0 4.0 9 Basedo n HWCMAC T Limit , 3 2 ppm v N O x 2.5 1 200 7 stac k tes t No t

availabl e 4. 0 Constructio n permi t #8801000 1 C O 0.025 0 CEM S 2.3 1 6. 6 Base don HWCMAC T Limit , 10 0 ppm v Constructio n permit

#8710002

4 V O M 0.4 3 Ma x Fee d& DR E 8. 0 0. 9 Constructio n permi t #8710002 4 

### so 2 4.0 0 0.1 % Tota l Fee d No t availabl e 7. 7 Constructio n permi t #8710002

4 H g 0.000 8 8/200 8 CP T 0.002 6 0.011 4 Basedo n HWCMAC T Limit , 130 ug/m 3 A s 0.0000 2 9/200 8 CP T 0.001 8 0.008 1 Base do n HWCMAC T Limit , 92 ug/m3 B e 0.000001 9 9/200 8 CP T 0.001 8 0.008 1 Basedon HWCMAC T Limit , 9 2 ug/m 3 C d 0.000005 4 9/200 8 CP T 0.004 6 0.020 2 Basedon HWCMAC T Limit , 23 0 ug/m 3 C r 0.00027 8 9/200 8 CP T 0.001 8 0.008 1 Basedon HWCMAC T Limit , 9 2 ug/m 3 S b 0.0000034 2 6/200 2 stac k tes t 0.0000034 2 0.00001 5 6/200 2 stac k tes t P b 0.00082 4 9/200 8 CP T 0.004 6 0.020 2 Base don HWCMAC T Limit , 23 0 ug/m 3 N i 0.0000044 6 6/200 2 stac k tes t 0.0000044 6 0.00002 0 6/200 2 stac k tes t S e 0.0000085 4 6/200 2 stac k tes t 0.0000085 4 0.00003 7 6/200 2 stac k tes t Dioxin/Fura n n g TE Q 7 % 0 2 0.0006 8 6/201 2 Conf
. Tes t 4.5 6 x 10" 9 2.0 0 x 10" 8 Base do n HWCMAC T Limit , 0.2 0 ng/dscmTE Q 3 . Uni t4 Incineratio n Th e actua l emission s an dpotentia l emission s fo r Uni t 4 ar e presente di n th e followin g table
. Th e basi s fo r eac h o f

th e emissio n rate s i s provide dalso
. Th e potentia l t o emi t (PTE ) wa s calculate dusin g emissio n testin g information , permi t limits , an demissio n limitation s i n regulator y standard s an d8,76 0 hour s o f operation
.

5 9Uni t4 Emission s Summar y

Pollutan t Actua l

Emissio n Rate (lbs/hr) Basi s of

Actua l Emissio n Rate PT E

(Lbs/hr ) PT E

(tons/yr ) PT E Basi s P M 0.441 6 12/200 9 CP T 1.63 7.1 5 Basedo n HWCMAC T Limit , 0.01 3 gr/dsc f P M 1 0 0.441 6 Same as P M 1.63 7.1 5 Basedon HWCMAC T Limit , 0.01 3 gr/dsc f P M 2 . 5 0.441 6 Same as P M 1.6 3 7.1 5 Basedo n HWCMAC T Limit , 0.01 3 gr/dsc f HC1/C1 2 2.3 4 12/200 9 CP T 2.6 4 11.5 7 Basedo n HWCMAC T Limit , 3 2 ppm v NO x 9.1 4 200 7 stac k tes t No t

availabl e 61. 6 Constructio n permi t #8801000 1 C O 0.11 5 CEM S 6.5 2 13.8 6 Basedo n HWCMAC T Limit , 10

0 ppm v Constructio n permi

t #8801000 1 V O M 1.4 8 Ma x Fee d& D R E 8. 0 3. 1 Constructio n permi t #8801000 1 

### so 2 3.6 9 0.1 % Tota l Fee d No t

availabl e 50.7 6 Constructio n permi t #8801000 1 H g 0.001 2 8/200 8 CP T 0.007 3 0.031 9 Basedon HWCMAC T Limit , 13 0 ug/m3 A s 0.0002 6 9/200 8 CP T 0.005 2 0.022 6 Basedo n HWCMAC T Limit , 9 2 ug/m 3 B e 0.000005 1 9/200 8 CP T 0.005 2 0.022 6 Basedon HWCMAC T Limit , 9 2 ug/m 3 C d 0.000028 7 9/200 8 CP T 0.012 9 0.056 4 Basedo n HWCMAC T Limit , 23 0 ug/m 3 C r 0.00013 5 9/200 8 CP T 0.005 2 0.022 6 Basedon HWCMAC T Limit , 9 2 ug/m3 S b 0.000011 1 2/200 2 stac k tes t 0.000011 1 0.000048 6 6/200 2 stac k tes t P b 0.0010 9 9/200 8 CP T 0.012 9 0.056 4 Basedo n HWCMAC T Limit , 23 0 ug/m3 N i 0.000011 0 2/200 2 stac k tes t 0.000011 0 0.000048 2 6/200 2 stac k tes t S e 0.000027 7 2/200 2 stac k tes t 0.000027 7 0.00012 1 6/200 2 stac k tes t Dioxin/Fura n n g TE Q 7 % 0 2 0.19 5 6/201 2 Conf
. Tes t 1.3 8 x 10" 8 6.0 5 x 10" 8 Basedo n HWCMAC T Limit , 0.2 0 ng/dscmTE Q 4 . Existin g Boile r A l l boile r

emissio n factor s ar e take n fro mth e AP-4 2 - Sectio n 1. 4 Natura l Ga s Combustion
. Actua l emission s ar e base do n natura l ga s burne di n 2012
. PT E i s base do n maximu mhourl y hea t inpu t int o th e boile r

an d8,76 0 hour s pe r yea r o f operation
. Th e tabl e belo w contain s al l emissio n factor s an demissio n rates .

6 0Existin g Boile rEmission s Summar y Maximu mHourl y Hea t Input : 10. 6 MMBtu/h r (90.1 5 mmscf/hr ) Actua l Natura l Ga s Usag e 2012 : 86.8 3 mmscf/y r Emissio n Actua l Facto r Emission s P T E P T E Pollutan t (lb/mmscf ) (tons/yr ) (lb/hr ) (tons/yr ) C O 8 4 3.6 5 0.86 4 3.7 9 V O M 5. 5 0.23 9 0.05 7 0.24 8 N O x 10 0 4.3 4 1.0 3 4.5 1 P M 2 . 5 7. 6 0.33 0 0.07 8 0.34 3 P M 1 0 7. 6 0.33 0 0.07 8 0.34 3 P M 7. 6 0.33 0 0.07 8 0.34 3 

### s o 2 0. 6 0.02 6 0.00 6 0.02 7 N H 3 3. 2 0.13 9 0.03 3 0.14 4 5 . La b Pac kRepac kBuildin g (LPR ) Th e LP Rbuildin g emissio n facto r i s base do n exposur e monitorin g dat acollecte di n th e are adurin g norma l operations
. Thi s emissio n facto r i s multiplie db y th e hour s o f operatio n i n 201 2 t o giv e a n estimat e o f th e actua l emissio n rat e an dmultiplie db y 8,76 0 hour s pe r

yea r o f operatio n t o giv e th e potentia l t o emit
. V O M Actua l Emissio n = 0.332 1 (lbs/hr ) x 644 0 (hrs ) / 200 0 = 1.0 7 tons/yea r V O M PT E= 0.332 1 (lbs/hr ) x 876 0 (hrs ) / 200 0 = 1.4 5 tons/yea r Benzen e Actua l Emissio n = 0.055 2 (lbs/hr ) x 644 0 (hrs ) / 200 0 = 0.177 7 tons/yea r Benzen e PT E= 0.055 2 (lbs/hr ) x 876 0 (hrs ) / 200 0 = 0.241 8 tons/yea r 6. Materia l Processin g Are a1 (MP-1 ) Th e MP- 1 buildin g emissio n facto r i s base do n exposur e monitorin g dat acollecte di n th e operation s are adurin g norma l operations
. Thi s emissio n facto r i s multiplie db y th e hour s o f operatio n i n 201 2 t o giv e a n estimat e o f th e actua l emissio n rat e an dmultiplie db y 8,76 0 hour s pe r

yea r o f operatio n t o giv e th e PTE
. V O M Actua l Emissio n = 0.054 5 (lbs/hr ) x 731 0 (hrs ) / 200 0 = 0.199 2 tons/yea r V O M PT E= 0.054 5 (lbs/hr ) x 876 0 (hrs ) / 200 0 = 0.238 7 tons/yea r Benzen e Actua l Emissio n = 0.011 3 (lbs/hr ) x 731 0 (hrs ) / 200 0 = 0.041 3 tons/yea r Benzen e PT E= 0.011 3 (lbs/hr ) x 876 0 (hrs ) / 200 0 = 0.049 5 tons/yea r

6 17 . Materia l Processin g Are a2 (MP-2 ) Th e MP- 2 buildin g emissio n facto r i s base do n exposur e monitorin g dat acollecte di n th e operation s are adurin g norma l operations
. Thi s emissio n facto r i s multiplie db y th e hour s o f operatio n i n 201 2 t o giv e a n estimat e o f th e actua l emissio n rat e an dmultiplie db y 8,76 0 hour s pe r

yea r o f operatio n t o giv e th e PTE
. V O M Actua l Emissio n = 0.054 5 (lbs/hr ) x 523 0 (hrs ) / 200 0 = 0.142 5 tons/yea r V O M PT E= 0.054 5 (lbs/hr ) x 876 0 (hrs ) / 200 0 = 0.238 7 tons/yea r Benzen e Actua l Emissio n = 0.011 3 (lbs/hr ) x 523 0 (hrs ) / 200 0 = 0.029 5 tons/yea r Benzen e PT E = 0.011 3 (lbs/hr ) x 876 0 (hrs ) / 200 0 = 0.049 5 tons/yea r 8 . Bul kSolid s Storag e Th e bul k

solid s storag e buildin g emissio n facto r i s base do n monitorin g dat acollecte di n th e storag e an dhandlin g area . Thi s emissio n facto r i s multiplie db y th e hour s o f operatio n i n 201 2 t o giv e a n estimat e o f th e actua l emissio n rat e an dmultiplie db y 8,76 0 hour s pe r

yea r o f operatio n t o giv e th e PTE
. V O M Actua l Emissio n = 0.583 6 (lbs/hr ) x 876 0 (hrs ) / 200 0 = 2.5 6 tons/yea r V O M PT E= 0.583 6 (lbs/hr ) x 876 0 (hrs ) / 200 0 = 2.5 6 tons/yea r Benzen e Actua l Emissio n = 0.004 3 (lbs/hr ) x 876 0 (hrs ) / 200 0 = 0.018 8 tons/yea r Benzen e PT E= 0.004 3 (lbs/hr ) x 876 0 (hrs ) / 200 0 = 0.018 8 tons/yea r 9 . Dru m Crushe r Actua l Emission s Emission s - Volatil e Organi c Materia l (VOM ) Basis : Veoli aha s collecte ddat afo r th e fiv e year s sinc e th e permi t wa s issue dincluding : th e numbe r

o f container s crushed , th e typ e o f volatil e constituent s likel y t o b e i n containe r

residue , an dth e amoun t o f thes e volatil e constituent s processe do n a n annua l basis
. A ne w VO M emissio n facto r wa s calculate dutilizin g thi s dat afro m actua l operations
. Th e containe r residu e wa s characterize da s containin g th e to p organic s at

thei r overal l concentration s i n th e wast e receive di n 200 7 - 2011
. Th e remainde r

o f th e wast e wa s represente da s wate r an diner t

solids
. Thi s approac h yielde daVO M emissio n facto r o f 0.022 1 pound s VO M pe r dru mcrushed
. Wit h amaximu mcrushin g rat e o f 4 0 drum s pe r

hour , th e PT E fo r

th e dru mcrushe r

wa s
6 2calculate dt o b e 0.883 3 pound s VO M pe r hou r an d3.8 7 ton s VO M pe r year . Th e detaile dcalculation s ar e provide dbelow
. Drum s crushe dpe r

yea r = 350,40 0 (4 0 drum s /hour , 8,76 0 hours/yea r V O M Emissio n Facto r Calculatio n fo r

Dru mCrushe r Emissio n Facto r

= Summatio n o f Pound s VO M fro mColum n I belo w

= 0.022 1 pound s pe r dru m Maximu mrat e o f

crushin g = 4 0 drum s pe r hou r Maximu mVO M emissio n rat e = 0.022 1 x 4 0 = 0.883 3 pound s VO M pe r hou r Maximu mannua l VO M rat e = 0.883 3 x 179/2,00 0 = 0.079 0 ton s VO M pe r yea r

6 3Vesse l Content s Analysi s Vesse l volum e (ft3 ) = 7.352 4 R = 998. 9 (mmHg)(ft3)/(lbmole)(K )

Assumptions : 1
. Eac hcontaine r

content s i s uniforml y representativ e o f th e overal l wast e mixtur e receive da t th e plant
. 2
. Th e overal l waste mixtur e a t th e plan t

i s characterize db y th e to p organi c constituent s i n waste receive dfo r 200 7 - 2011
. A B C D E F G H I J
VO C M W

(lb/lbmole) Weigh t

(lbs) lbmoles X i Psat i P i Vapo r

(lbmoles) Vapo r

(lbs) Comment s acetonitril e 41.0 5 3,361,22 8 81,88 1 0.010 0 86.3 7 0.8 6 0.0000 2 0.0008 7 acrylonitril e 53. 1 804,31 6 15,14 7 0.001 8 105.8 3 0.2 0 4.83E-0 6 0.0002 6 atrazin e 215.6 8 356,14 8 1,65 1 0.000 2 0.0 0 0.0 0 1.44E-1 5 3.10E-1 3 cyanid e compound s 27.0 3 138,87 9 5,13 8 0.000 6 1.00 0.0 0 1.55E-0 8 4.19E-0 7 ethylbenzen e 106.1 7 633,27 4 5,96 5 0.000 7 9.5 1 0.0 1 1.71E-0 7 0.0000 2 hydrazin e 32.0 5 180,23 8 5,62 4 0.000 7 10.0 0 0.0 1 1.69E-0 7 0.0000 1 methano l 32.0 4 6,070,50 1 189,46 6 0.023 1 126.9 4 2.9 3 0.0000 7 0.0023 2 methy l isobuty l keton e 100.1 6 3,042,48 3 30,37 6 0.003 7 19.2 8 0.0 7 1.77E-0 6 0.0001 8 methy l tert-buty l ether 88.1 5 405,41 3 4,59 9 0.000 6 273.7 1 0.1 5 3.79E-0 6 0.0003 3 n-buty l alcoho l 74.1 2 1,503,98 6 20,29 1 0.002 5 6.1 6 0.0 2 3.77E-0 7 0.0000 3 n-hexan e 86.1 8 747,61 4 8,67 5 0.001 1 151.5 4 0.1 6 3.96E-0 6 0.0003 4 nitrat e compound s 84.9 9 181,23 9 2,13 2 0.000 3 0.0 0 0.0 0 0.00E+0 0 0.00E+0 0 Non e i n vapo r pthali c anhydrid e 148. 1 154,63 5 1,044 0.000 1 0.0 0 0.0 0 0.00E+0 0 0.00E+0 0 Non e i n vapo r pyridin e 79. 1 169,55 4 2,14 4 0.000 3 45.0 9 0.0 1 2.91E-0 7 0.0000 2 styren e 104.1 5 1,915,48 7 18,39 2 0.002 2 6.1 8 0.0 1 3.43E-0 7 0.0000 4 toluen e 92.1 3 8,657,46 8 93,97 0 0.011 5 28.4 4 0.3 3 0.0000 1 0.0007 4 triethylamin e 101. 2 850,75 2 8,40 7 0.001 0 67.7 8 0.0 7 1.72E-0 6 0.0001 7 xylen e 106.1 7 2,328,68 8 21,93 4 0.002 7 8.3 0 0.0 2 5.49E-0 7 0.0000 6

as ethano l 46.0 7 93,612,15 0 2,031,95 5 0.247 9 59.1 6 14.6 7 0.0003 6 0.0166 9 Av g volatilit y fo r smalle r amount s V O M i n waste as wate r 18.0 2 93,612,15 0 5,194,90 3 0.633 9 23.6 9 15.0 1 0.0003 7 0.0066 8 solid s (a s lead ) 207. 2 93,612,15 0 451,79 6 0.055 1 Non e i n vapo r 6 4Potential-To-Emi t(PTE ) Emission s - Volatil e Organi c Materia l (VOM ) V O M Emissio n Facto r Calculatio n fo r

Dru mCrushe r Emissio n Facto r

= Summatio n o f Pound s VO M fro mColum n I

= 0.022 1 pound s pe r dru m Maximu mrat e o f

crushin g = 4 0 drum s pe r hou r Maximu mVO M emissio n rat e = 0.022 1 x 4 0 = 0.883 3 pound s VO M pe r hou r Maximu mannua l VO M rat e = 0.883 3 x 8,760/2,00 0 = 3.8 7 ton s VO M pe r yea r P T EVO M emission s fro mdru mcrushin g operation s = 3.8 7 to n VOM/y r 10 . Tank s A l l th e tank s emi t

bot hVO M an dbenzene
. Th e actua l VO M emission s ar e thos e reporte di n th e Annua l Ai r

Emission s Repor t

fo r 2012
. Th e VO M an dbenzen e PTE s wer e calculate dfro m th e emissio n facto r

detennine dusin g 201 2 emissio n rate s an dthroughputs
. Th e emissio n facto r wa s the n multiplie dtime s th e maximu mhourl y throughpu t t o yiel dth e potentia l VO M emission s i n pound s pe r hour ; an dthe n converte dt o ton s pe r yea r usin g 8,76 0 hour s pe r year . Tan kEmission s Summar y Tan k Numbe r Pollutan t Actua l Emission s 201 2 (lb/yr ) 201 2

Throughpu t (10 3gals/yr ) Emissio n

Facto r (lbs/10 3 gals ) P T E

(Lb/hr ) P T E

(Ton/yr )
Tan k # 2 V O M 1.5 8 60 2 0.002 6 0.005 2 0.023 0 Tan k # 2 Benzen e 0.001 5 60 2 2.49E-0 6 4.98E-0 6 2.18E-0 5 Tan k # 4 V O M 1.7 3 60 2 0.002 9 0.005 7 0.025 2 Tan k # 4 Benzen e 0.01 7 60 2 2.82E-0 5 5.65E-0 5 2.47E-0 4 Tan k # 6 V O M 2.7 6 306 1 0.000 9 0.001 8 0.007 9 Tan k # 6 Benzen e 0.002 7 306 1 8.82E-0 7 1.76E-0 6 7.73E-0 6 Tan k # 8 V O M 2.8 1 246 1 0.001 1 0.002 3 0.010 0 Tan k # 8 Benzen e 0.002 7 246 1 1.10E-0 6 2.19E-0 6 9.61E-0 6 Tan k #1 0 V O M 10.6 8 50 0 0.021 4 0.042 7 0.187 1 Tan k #1 0 Benzen e 0.010 4 50 0 2.08E-0 5 4.16E-0 5 1.82E-0 4 Tan k #2 0 V O M 1.1 2 31 0 0.003 6 0.007 2 0.031 6 Tan k #2 0 Benzen e 0.001 1 31 0 3.55E-0 6 7.10E-0 6 3.11E-0 5 Tan k #3 0 V O M 2.3 3 7 9 0.029 5 0.059 0 0.258 4 Tan k #3 0 Benzen e 0.002 3 7 9 2.91E-0 5 5.82E-0 5 2.55E-0 4
6 5Tan kEmission s Summar y Tan k Numbe r Pollutan t Actua l Emission s 201 2 (lb/yr ) 201 2

Throughpu t (10 3gals/yr ) Emissio n

Facto r (lbs/10 3 gals ) P T E

(Lb/hr ) P T E

(Ton/yr )
Tan k #40 V O M 2.42 65 7 0.003 7 0.007 4 0.032 3 Tan k #40 Benzen e 0.002 3 65 7 3.50E-0 6 7.00E-0 6 3.07E-0 5 Tan k #5 0 V O M 0.765 0 76 4 0.001 0 0.002 0 0.008 8 Tan k #5 0 Benzen e 0.000 7 76 4 9.46E-0 7 1.83E-0 6 8.03E-0 6 Tan k #60 V O M 5.5 5 95 0 0.005 8 0.011 7 0.051 2 Tan k #60 Benzen e 0.005 4 95 0 5.68E-0 6 1.14E-0 5 4.98E-0 5 Tan k #30 0 V O M 1.90 58 0 0.003 3 0.006 6 0.028 7 Tan k #30 0 Benzen e 0.001 8 58 0 3.10E-0 6 6.21E-0 6 2.71E-0 5 Tan k #30 2 V O M 11.7 4 54 3 0.021 6 0.043 2 0.189 4 Tan k #30 2 Benzen e 0.011 4 54 3 2.10E-0 5 4.20E-0 5 1.84E-0 4 Tan k #30 4 V O M 2.8 1 43 4 0.006 5 0.013 0 0.056 7 Tan k #30 4 Benzen e 0.002 7 43 4 6.22E-0 6 1.24E-0 5 5.45E-0 5 Tan k #30 6 V O M 5.2 8 46 6 0.011 3 0.022 7 0.099 3 Tan k #30 6 Benzen e 0.005 1 46 6 1.09E-0 5 2.19E-0 5 9.59E-0 5 Tan k #30 8 V O M 8.9 9 35 5 0.025 3 0.050 6 0.221 8 Tan k #30 8 Benzen e 0.008 7 35 5 2.45E-0 5 4.90E-0 5 2.15E-0 4 Tan k #31 0 V O M 8.2 7 28 2 0.029 3 0.058 7 0.256 9 Tan k #31 0 Benzen e 0.008 0 28 2 2.84E-0 5 5.67E-0 5 2.48E-0 4 Tan k #31 2 V O M 7.7 1 19 2 0.040 2 0.080 3 0.351 7 Tan k #31 2 Benzen e 0.007 5 19 2 3.91E-0 5 7.81E-0 5 3.42E-0 4 Tan k #31 4 V O M 4.6 4 19 2 0.024 2 0.048 3 0.211 7 Tan k #31 4 Benzen e 0.004 5 19 2 2.34E-0 5 4.69E-0 5 2.05E-0 4 

## COMPLIANC E METHOD S A . Continuou s Emissio n Monitor s Th e continuou s emission s monitorin g (CEM ) syste mconsist s o f sampl e probes , sampl e deliver y an dconditionin g apparatus , an dga s analyzers
. Eac hincinerato r i s equippe dwit haCEMS , whic h consist s o f

th e followin g majo r

components :
• Heate dstac k

sampl e prob e
• Heate dtrace dumbilica l

• Heate dsampl e pum p
• EcoChe mMC 3 multicomponen t infrare d(IR ) ga s analyze r
• Zirconiu moxide-base doxyge n analyze r
• Syste mcontrolle r an ddat aacquisitio n syste m Sample s ar e extracte dfro mth e stac k at Unit s 2 an d3 an dth e transitio n ductin g locate dbetwee n th e scrubbe r

an dstac k

a t Uni t 4
. Th e Continuou s Emissio n Monitorin g Syste mQualit y Assuranc e

6 6Pla n contain s detaile dinformatio n abou t th e operatio n an dmaintenanc e o f th e CE M system s a

t th e facility
. A cop y o f

th e mos t

curren t pla n i s provide di n Appendi x D
. Response s fro meac hCEM S ar e fe dt o th e Contro l Syste m(CS)
. Th e syste mcontrolle r control s the samplin g syste m temperatures , purge/blowback , calibratio n checks , dat ahandling , messaging , an dalarms
. Th e CEM S controlle r

i s integrate dwit hth e incinerato r dat aacquisitio n system , automati c wast e fee d cutof f (AWFCO ) syste man dth e mai n contro l system . B . Proces s Paramete rMonitorin g Veoli amonitor s anumbe r o f proces s parameter s fo r th e purpos e o f

demonstratin g on-goin g complianc e wit hregulator y requirement s an dpermi t conditions
. Continuou s monitorin g device s equippe dwit hdat aloggin g allo w Veoli at o calculate , record , an dvie w value s fo r proces s parameter s tha t

ar e regulated
. Operation , maintenance , an ddat ahandlin g procedure s ar e describe d i nth e Continuou s Monitorin g Syste mQualit y Contro l Program
. A cop y o f th e mos t

recen t progra mi s provide di n Appendi x D
. Description s o f th e parameter s monitore dan dth e instrumentatio n use di s provide dbelow
. 1 . Mass/Feedrat e Monitor s Liqui dwast e feedrate s fro mtank s ar e measure db y corioli s mas s flowmeters
. Direc t injec t liqui dfeedrate s fro mth e tanke r truc k ar e calculate dusin g th e continuousl y monitore dweigh t o f th e tanker
. Al l soli dwast e charge s ar e weighe dusin g ascale/loa dcel l prio r t o bein g fe dt o th e incinerator
. Thes e measurement s ar e use dt o calculat e pumpabl e waste , tota l waste , an d constituen t

feedrates
. Fo r Uni t 4 , th e outpu t

o f acalibrate dfeede r

i s utilize dt o calculat e th e feedrat e o f powdere d activate dcarbon , whic hi s injecte dint o th e plenu mupstrea mo f th e baghouses
. 2 . Pressure/Differentia l Pressur e Monitor s Primar y combustio n chambe r pressur e i s measure db y diaphragm-actuate dpressur e transmitters
. Th e positio n o f th e dampe r

immediatel y upstrea mo f th e induced-draft

fa n i s varie dt o contro l stac k ga s flowrat e an dt o maintai n kil ncombustio n chambe r negativ e pressur e (draft)
. Th e primar y combustio n chambe r pressur e i s interlocke dwit hwast e feeds
. Fo r Unit s 2 an d3 , pressur e dro p i n th e cylinde r ga s feedstrea mi s measure dan dconverte dt o a feedrate
. Th e feedrat e i s use dt o calculat e thi s feedstream' s contributio n t o th e chlorine , low

volatil e metals , an dsemi-volatil e metal s feedrate s t o th e incinerator
. Fo r Uni t 4 , pressur e switche s ar e utilize dt o ensur e tha t th e carbo n feede r

discharg e pressur e an dth e carbo n injectio n ai r blowe r discharg e pressur e ar e withi n th e desig n limits
. Th e pressur e dro p acros s apito t tub e i n th e stac k

i s continuousl y monitore dan duse dt o calculat e th e stac k

ga s flowrate
.

6 73 . Temperatur e Monitor s Fo r Unit s 2 an d3 , redundan t thermocouple s ar e use dt o measur e th e temperatur e i n bot h combustio n chambers
. A thermocoupl e i s als o locate dat th e exi t t o th e SD A an di s th e primar y elemen t fo r th e SD A exi t

temperatur e contro l loop
. Uni t 4 i s equippe dwit hredundan t pyrometer s i n th e primar y chambe r an dredundan t thermocouple s i n th e secondar y chamber
. Eac hSD A outle t i s equippe dwit hredundan t thermocouple s use dfo r temperatur e contro l an dmonitorin g o f th e baghous e inle t

temperature . 4 . Emergenc y Safet y Ven tPositio n Monitor s Th e positio n o f

th e emergenc y safet y ven t i s indicate da s ope n o r close db y apositio n transmitter
. N o wast e o r fue l ca n b e fe di f

th e emergenc y safet y ven t positio n i s "open. " Th e Emergenc y Safet y Ven t Pla n provide s detail s o n th e emergenc y safet y ven t systems . 5 . Ba g Lea kDetectio n Syste m Atriboelectri c senso r i s locate ddownstrea mo f th e induce ddraft

fa n tha t monitor s th e relativ e particulat e matte r

loadin g o f

th e combustio n ga s exitin g th e baghouses
. Alarm s an dinterlock s base do n thi s relativ e measuremen t ar e indication s o f apotentia l ba g lea k o r failure
. Procedure s fo r

setu p an dadjustment s t o th e ba g lea k detectio n syste mar e no t covere db y thi s qualit y contro l program . Th e Operatio n an dMaintenanc e Pla n provide s detail s o n th e ba g lea k detectio n system . C . Demonstratio n o f Complianc e wit h Applicabl e Requirement s Th e method s fo r

demonstratin g complianc e wit hth e applicabl e requirement s identifie di n Sectio n I V o f thi s applicatio n ar e describe di n th e followin g table
.

6 8EMISSIO N

UNI T ID(S ) APPLICATIO N

REFERENC E FO R APPLICABL E REQUIRMEN T CITATIO N COMPLIANC E METHO D Hazardou s Wast

e Combustors : Emissio n Standar d Requirement s Incinerators : Uni t 2 , Uni t 3 , Uni t 4 Sectio n IV.B.l. a 3 5 IA C 212.123(a ) Monitoring/Recordkeepin g - Continuou s opacit y monitors an

drecording devices
. Incinerators : Uni t 2 , Uni t 3 , Uni t 4 Sectio n IV.B.l. b 3 5 IA C 212.30 1 Wor k Practice s - Standar

doperation s a

t th e facilit y ar

e designedt

o avoi dth

e generatio n o f fugitiv e particulat

e emissions
. Surface s ar e pavedandkep

t free o f materia l tha t coul dgenerat

e particulate
. Materia l handlin g operation s ar e enclosed processe s designedt

o minimiz e particulat

e emission s t

o th e atmosphere
. Incinerators : Uni t 2 , Uni t 3 , Uni t 4 Sectio n IV.B.2. a Constructio n Permit s #8710002

4 an d#8801000 1 Recordkeeping - Emission s ar e calculate don a

n annua l basi s using tes

t results , monitorin g data , engineering calculation s andstandar demission factors
. Record s o f thes e calculation s ar

e maintainedonsite
. Incinerators : Uni t 2 , Uni t 3 , Uni t 4 Sectio n IV.B.3. a 40 CF R63.1219(a)(5 ) Monitoring/Recordkeepin g - Continuou s emissio n monitor an drecording device
. Incinerators : Uni t 2 , Uni t 3 , Uni t 4 Sectio n IV.B.3. b Constructio n Permit s #83120053,#8710002

4 an d #8801000 1 Monitoring/Recordkeepin g - Continuou s emissio n monitor an drecording device
. Incinerators : Uni t 2 , Uni t 3 , Uni t 4 Sectio n IV.B.3 . C Constructio n Permit s #8710002

4 an d#8801000 1 Recordkeeping - Emission s ar e calculate do n a

n annua l basi s usin g tes

t results , monitorin g data , engineering calculation s andstandar demission factors
. Record s o f these calculation s ar

e maintainedonsite
. Incinerators : Uni t 2 , Uni t 3 , Uni t 4 Sectio n IV.B.4. a 3 5 IA C 212.181(b ) Testing/Monitoring/Recordkeepin g - Complianc e withNESHA Pfo r Hazardou s Wast e Combustors a

s referencedi n Section B.4. b below
. Incinerators : Uni t 2 , Uni t 3 , Uni t 4 Sectio n IV.B.4. b 40 CF R63.1219(a)(7 ) Testing/Monitoring/Recordkeepin g - CP T t o establis hOPL s a

s provide di n most recen t NO C (Appendi x E)
. Incinerators : Uni t 2 , Uni t 3 , Uni t 4 Sectio n IV.B.4 . C Constructio n Permit s #8710002

4 an d#8801000 1 Recordkeeping - Emission s ar e calculate do n a

n annua l basi s usin g tes

t results , monitoring data , engineering calculation s an dstandar demission factors
. Record s o f these calculation s ar

e maintainedonsite
. ncinerators : Jnit2 , Uni t

3 , Uni t 4 Sectio n rV.B.5. a 3 5 IA C 219.30 1 an d219.30 2 Testing/Monitoring/Recordkeepin g - Complianc e wit hNESHA Pfo r

Hazardou s Wast e Combustors DR Erequiremen t o f a t leas t 99.99 % destruction provide s fo r complianc e withthi s requirement
. Incinerators : Uni t 2 , Uni t 3 , Uni t 4 Sectio n FV.B.5. b Constructio n Permit s #8710002

4 an d#8801000 1 Recordkeeping - Emission s ar e calculate do n a

n annua l basi s using tes

t results , monitorin g data , engineering calculation s an dstandar demission factors
. Record s o f these calculation s ar

e maintaine donsite
. Incinerators : Uni t 2 , Uni t 3 , Uni t 4 Sectio n IV.B.6. a Constructio n Permit s #8710002

4 an d#8801000 1 Recordkeeping - Emission s ar e calculate do n a

n annua l basi s using tes

t results , monitorin g data , engineering calculation s andstandar demission factors
. Record s o f these calculation s ar

e maintainedonsite
. Incinerators : Uni t 2 , Uni t 3 , Uni t 4 Sectio n IV.B.7. a 40 CF R63.1219(a)(1 ) Testing/Monitoring/Recordkeepin g - CP T t o establis hOPL s a

s provide di n most recen t NO C (Appendi x E)
. Incinerators : Uni t 2 , Uni t 3 , Uni t 4 Sectio n IV.BJ. b 40 CF R63.1219(a)(2) Testing/Monitoring/Recordkeepin g - CP T t o establis hOPL s a

s provide di n most recen t NO C (Appendi x E)
. Incinerators : Uni t 2 , Uni t 3 , Uni t 4 Sectio n IV.B.7 . C 40 CF R63.1219(a)(3 ) Testing/Monitoring/Recordkeepin g - CP T t o establis hOPL s a

s provide di n most recen t NO C (Appendi x E)
. Incinerators : Uni t 2 , Uni t 3 , Uni t 4 Sectio n IV.B.7. d 40 CF R63.1219(a)(4) Testing/Monitoring/Recordkeepin g - CP T t o establishOPL s a

s provide di n most recen t NO C (Appendi x E)
. Incinerators : Uni t 2 , Uni t 3 , Uni t 4 Sectio n IV.B.7. e 4 0 CFR61.348(a)(l)(iii ) Testing/Monitoring/Recordkeepin g - Complianc e wit hNESHA Pfo r

Hazardou s Wast e Combustors DR Erequiremen t o f a t least 99.99 % destruction provide s fo r complianc e withthi s requirement
. Incinerators : Uni t 2 , Uni t 3 , Uni t 4 Sectio n IV.B.7. f 40 CF R63.689(c)(2 ) The design o f al l transfe

r system s subject t o thi s rul e call s fo r

weldedjoint s fo r continuou s hardpiping
. Incinerators : Uni t 2 , Uni t 3 , Uni t 4 Sectio n IV.B.8. a 40 CF R63.1219(a)(6) Testing/Monitoring/Recordkeepin g - CP T t o establis hOPL s a

s provide di n most recen t NO C (Appendi x E)
. Incinerators : Uni t 2 , Uni t 3 , Uni t 4 Sectio n IV.B.8. b Constructio n Permit s #8312005 3 an

d#8710002

4 Testing/Monitoring/Recordkeepin g - Complianc e wit hNESHA Pfo r

Hazardou s Wast e Combustors HC l emission s limitation s provide s fo r complianc e withthi s requirement
. Incinerators : Uni t 2 , Uni t 3 , Uni t 4 Sectio n IV.B.9. a 40 CF R63.1219(c)(1 ) Testing/Monitoring/Recordkeepin g - CP T t o establis hOPL s a

s provide di n most recen t NO C (Appendi x E)
. 6 9EMISSIO N

UNI T ID(S ) APPLICATIO N

REFERENC E FO R APPLICABL E REQUIRMEN T CITATIO N COMPLIANC E METHO D Incinerators : Uni t 2 , Uni t 3 , Uni t 4 Sectio n IV.B.9. b 40 CF R63.1219(c)(2 ) Recordkeeping - The facilit y does not accep t dioxin-liste dhazardou s wast e i n thei r wast e stream s fo r combustion
. Incinerators : Uni t 2 , Uni t 3 , Uni t 4 Sectio n IV.B.9 . C 4 0 CF R63.1219(c)(3 ) Testing/Monitoring/Recordkeepin g - CP T t o establis hOPL s a

s provide di n most recen t NO C (Appendix E)
. Hazardou s Wast

e Combustors : Wor kPractic e an d Operationa l Requirement s Incinerators : Uni t 2 , Uni t 3 , Uni t 4 Sectio n IV.C.l. a 40 CFR63.1206(a)&(b) , 63.1209G ) through (p) Testing/Monitoring/Recordkeepin g - CP T t o establis hOPL s a

s provide di n most recen t NO C (Appendi x E)
. NO C submitta l t o agency . Incinerators : Uni t 2 , Uni t 3 , Uni t 4 Sectio n rV .C.l. b 4 0 CF R63.1206(c)(1) , 63.1211(c ) Recordkeeping - aDocumentation o f Complianc e (DOC ) ha

s bee n developedand i s maintainedi n th

e facihty operating record
. Incinerators : Uni t 2 , Uni t 3 , Uni t 4 Sectio n IV.C.l. c 4 0 CF R63.1206(c)(2) , 63.6(e)(3 ) SSM Pdeveloped , implementedandmaintainedi n accordance wit h40 CF R63. 6 an d63.1206(c)(2)
. Incinerators : Uni t 2 , Uni t 3 , Uni t 4 Sectio n IV.C.l. d 40 CF R63.1206(c)(3 ) 3 5 IA C 201.14 9 AWFC O syste mi n operation fo r

al l thre e incinerators
. Hazardou s wast e fee di s shutof f according t

o procedure s specifie di n th e faculty' s Automati c Wast e Fee d Cutof f Plan
. Incinerators : Uni t 2 , Uni t 3 , Uni t 4 Sectio n IV.C.l. e 4 0 CF R63.1206(c)(4 ) ES V operatin g plan developed , implementedandi s maintainedi n th e operating recor do f th e facility
. Incinerators : Uni t 2 , Uni t 3 , Uni t 4 Sectio n IV.C.l. f 4 0 CF R63.1206(c)(5 ) Testing/Monitoring/Recordkeepin g - CP T t o establis hOPL s a

s provide di n most recen t NO C (Appendi x E)
. Incinerators : Uni t 2 , Uni t 3 , Uni t 4 Sectio n rV .C.l. g 40 CF R63.1206(c)(6 ) Trainin g Progra man dOperato

r Certificatio n Progra

mdeveloped , implemented an di s maintained
. Record s o f trainin g andoperato

r certificatio n retainedo n site
. Incinerators : T Jnit2,Unit3 , Jnit4 Sectio n PV.C.l. h 4 0 CF R63.1206(c)(7) , 63.6(e) A nOperatio n andMaintenanc e Plan ha s bee n developed , implementedan d maintainedi n th

e operating record s on site
. Hazardou s Wast

e Combustors : Monitorin g an d Testin g Requirement s Incinerators : Uni t 2 , Uni t 3 , Uni t 4 Sectio n IV.D
. 1.a 40CFR63.1209(a)(l)(i ) Continuou s C O monitor an ddat aacquisitio n syste

m(DAS)
. TH C testing durin g CPT
. Incinerators : Uni t 2 , Uni t 3 , Uni t 4 Sectio n IV.D.l. b 40CFR63.1209(a)(l)(iii ) Wil l instal l an doperat e continuou s P M CEM S when required
. Incinerators : Uni t 2 , Uni t 3 , Uni t 4 Sectio n IV.D.l. c 40 CF R63.1209(a)(2) , (a)(3 ) and(a)(4 ) CEM S an dCOM s installed , calibrated , maintainedan dcontinuousl

y operate di n accordance withth

e performanc e specification s i n thi s rule
. CEM S & COM S QA/Q C Plan developed , implementedandmaintainedt o reflec t these requirements
. Incinerators : Uni t 2 , Uni t 3 , Uni t 4 Sectio n IV.D.l. d 40 CF R63.1209(a)(5) , 63.8(f ) No t applicable
. Incinerators : Uni t 2 , Uni t 3 , Uni t 4 Sectio n IV.D.l. e 40 CF R63.1209(a)(6) Rollin g averages fro mCEMS , COM S dat aar e calculate dby th

e DA S i n accordance wit

hthi s requirement
. Incinerators : Uni t 2 , Uni t 3 , Uni t 4 Sectio n IV.D.2. a 4 0 CF R63.1209(b)(1) , (b)(2) CM S installed , calibrated , maintainedan dcontinuously operate

da s describedi n most recen t NO C (Appendi x E)
. CM S QA/Q C Plan developed , implementedand maintainedt

o reflec t thes e requirements
. Incinerators : Uni t 2 , Uni t 3 , Uni t 4 Sectio n IV.D.2. b 40 CF R63.1209(b)(3 ) CM S installed , calibrated , maintainedan dcontinuously operate

da s describedi n mos t recen t NO C (Appendi x E)
. CM S QA/Q C Plan developed , implementedand maintainedt

o reflec t these requirements
. incinerators : Uni t 2 , Uni t 3 , Uni t 4 Sectio n IV.D.2 . C 40 CF R63.1209(b)(4) CM S installed , calibrated , maintainedandcontinuously operate da s describedi n mos t recen t NO C (Appendi x E)
. CM S QA/Q C Plan developed , implementedand maintainedt

o reflec t thes e requirements
. Incinerators : Uni t 2 , Uni t 3 , Uni t 4 Sectio n IV.D.2. d 4 0 CF R63.1209(b)(5 ) Rollin g averages fro mCM S dat aar e calculate db y th

e DA S i n accordance with thi s requirement
. Incinerators : Uni t 2 , Uni t 3 , Jni t 4 Sectio n IV.D. 3 40 CF R63.1206(c)(8 ) BLD S installed , maintainedan dcontinuously operated
. CM S QA/Q C Plan developed , implementedan dmaintainedt

o reflec t these requirements
. Incinerators : Uni t 2 , Uni t 3 , Uni t 4 Sectio n IV.D. 4 4 0 CF R63.1209(c ) FA Pdeveloped , implementedan dmaintainedt

o reflec t these requirements
. 7 0EMISSIO N

UNI T ID(S ) APPLICATIO N

REFERENC E FO R APPLICABL E REQUIRMEN T CITATIO N COMPLIANC E METHO D Incinerators : Uni t 2 , Uni t 3 , Uni t 4 Sectio n IV.D. 5 4 0 CF R63.1209(d) , 63.8(d) , 6..8(e ) CM S installed , calibrated , maintainedan dcontinuously operate

da s describedi n mos t recen t NO C (Appendi x E)
. CM S QA/Q C Pla n developed , implementedan d maintainedt

o reflec t thes e requirements
. Incinerators : Uni t 2 , Uni t 3 , Uni t 4 Sectio n IV.D. 6 4 0 CF R63.1209(e) , 63.8(b ) CM S installed , calibrated , maintainedan dcontinuously operate

da s describedi n mos t recen t NO C (Appendi x E)
. CM S QA/Q C Plan developed , implementedan d maintainedt

o reflec t thes e requirements
. Incinerators : Uni t 2 , Uni t 3 , Uni t 4 Sectio n IV.D. 7 40 CFR63.1209(f) , 63.8(c ) CM S installed , calibrated , maintainedan dcontinuously operate

da s describedi n mos t recen t NO C (Appendi x E) . CM S QA/Q C Plan developed , implementedan d maintainedt

o reflec t thes e requirements
. Incinerators : Uni t 2 , Uni t 3 , Uni t 4 Sectio n rV.D. 8 4 0 CF R63.1209(h) , 63.8(g ) CM S installed , calibrated , maintainedan dcontinuously operate

da s describedi n mos t recen t NO C (Appendi x E) . CM S QA/Q C Plan developed , implementedand maintainedt

o reflec t thes e requirements
. Incinerators : Uni t 2 , Uni t 3 , Uni t 4 Sectio n IV.D. 9 40 CF R63.1209(i) , 63.8(b ) Testing/Monitoring/Recordkeepin g - CP T t o establis hOPL s a

s provide di n mos

t recen t NO C (Appendi x E) . NO C submitta l t o agency . Incinerators : Uni t 2 , Uni t 3 , Uni t 4 Sectio n IV.D.1 0 40 CFR63.1209(r ) Testing/Monitoring/Recordkeepin g - CP T t o establis hOPL s a

s providedi n mos

t recen t NO C (Appendi x E) . NO C submitta l t o agency . Incinerators : Uni t 2 , Uni t 3 , Uni t 4 Sectio n IV .E
. l 40CFR63.1206(b)(5)(i)(B ) Change s t o asource ar

e evaluateddurin g planning
. A ne w CP T wil l b e performe d an dNO C submittedi f

indicated
. Incinerators : Uni t 2 , Uni t 3 , Uni t 4 Sectio n IV .E
. 2 4 0 CF R63.1206(b)(6 ) Testing/Monitoring/Recordkeepin g - CP T t o establis hOPL s a

s provide di n mos

t recen t NO C (Appendi x E) . Incinerators : Uni t 2 , Uni t 3 , Uni t 4 Sectio n IV .E
. 3 40 CF R63.1207(b ) Testing - CP T t o establis hOPL s a

s provide di n most

recen t NO C (Appendi x E) . Confkmator

y testing conductedfo r

dioxin/furan standar

da s provide di n mos

t recen t NOC
. Incinerators : Uni t 2 , Uni t 3 , Uni t 4 Sectio n PV .E
. 4 40 CF R63.1207(d ) Testing - CP T t o establis hOPL s a

s provide di n most

recen t NO C (Appendi x E) . Confirmator

y testing conductedfo r

dioxin/furan standar

da s provide di n mos

t recen t NOC
. ncinerators : Jnit2 , Uni t

3 , Uni t 4 Sectio n rV.E .5. a 40 CF R63.1207(f)(1) , 63.7(c)(2 ) CP T plan s submittedfo r approva l prio r t o test wit hcontent s a s describedi n regulations
. Incinerators : Uni t 2 , Uni t 3 , Uni t 4 Sectio n IV .E .5. b 40 CF R63.1207(f)(2) , 63.7(c)(2 ) Confirmator y tes t plan s submittedfo r

approva l prio r t o tes t withcontent

s a s describedi n regulations
. Incinerators : Uni t 2 , Uni t 3 , Uni t 4 Sectio n IV .E .6. a 4 0 CF R63.1207(g)(a) , 63.7(e) Testing - CP T t o establis hOPL s a

s provide di n most

recen t NO C (Appendi x E) . Incinerators : Uni t 2 , Uni t 3 , Uni t 4 Sectio n rV.E .6. b 40 CFR63.1207(g)(b) , 63.7(e) Corifirmator y testing conductedfo r

dioxin/furan standar

da s provide di n mos

t recen t NOC
. Incinerators : Uni t 2 , Uni t 3 , Uni t 4 Sectio n IV .E
. 7 40 CF R63.1207(h ) Performanc e tes t plan s submittedfo r

approva l prio r t o test . Incinerators : Uni t 2 , Uni t 3 , Uni t 4 Sectio n IV .E
. 8 40 CF R63.120 8 Performanc e tes t plan s submittedfo r

approva l prio r t o tes t usin g prescribe dtes

t methods
. Incinerators : Uni t 2 , Uni t 3 , Uni t 4 Sectio n IV.E.9. a 4 0 CF R63.1207(1)(1 ) Procedure s wil l be followe dfo r hazardou s wast

e burnin g i f

failure t o demonstrat

e complianc e occurs . Incinerators : Uni t 2 , Uni t 3 , Uni t 4 Sectio n IV .E .9. b 40 CF R63.1207(1)(2 ) Procedure s wil l be followe dfo r hazardou s wast

e burnin g i f

failure t o demonstrat

e complianc e occurs . Incinerators : Uni t 2 , Uni t 3 , Uni t 4 Sectio n IV .E .9 . C 40 CF R63.1207(1)(2 ) Procedure s wil l be followe dfo r hazardou s wast

e burnin g i f

failure t o demonstrat

e complianc e occurs . Hazardou s Wast

e Combustors : Recordkeepin g and Reportin g Requirement s Incinerators : Uni t 2 , Uni t 3 , Uni t 4 Sectio n rV .F. l 4 0 CF R63.1210(a ) Notification s wil l b e submitteda s required
. Incinerators : Uni t 2 , Uni t 3 , Uni t 4 Sectio n IV.F. 2 40 CF R63.1211(a ) Report

s wil l be preparedan

dsubmitteda

s required
. Incinerators : Uni t 2 , Uni t 3 , Uni t 4 Sectio n IV.F. 3 40 CF R63.1211(b ) Record s requiredb y the regulations , by th e plan s utilize da

t th e facility andb y standar doperatin

g procedure s wil l b e retainedo n sit e fo r a t least five years . 7 1EMISSIO N

UNI T ID(S ) APPLICATIO N

REFERENC E FO R APPLICABL E REQUIRMEN T CITATIO N COMPLIANC E METHO D Wast e Procesin g Units : Requirements Wast e Processing : MP-1 , MP-2 , LP R Sectio n rV .G. l 3 5 IA C 212.123(a ) Monitoring/Recordkeepin g - Routin e visibl e emission s observations
. Wast e Processing : MP-1 , MP-2 , LP R Sectio n IV.G. 2 3 5 IA C 219.30 1 Recordkeeping - VO M emissio n rat e calculations
. Wast e Processing : MP-1 , MP-2 , LP R Sectio n IV.G. 3 40 CFR63.683(b)(l)(i) , 63.688(a ) Veoli acontrol s ai r emission s fro mcontainers i n accordance withContaine r Leve l 1 requirements
. Wast e Processing : MP-1 , MP-2 , LP R Sectio n IV.G. 4 4 0 CF R63.922 Veoli acontrol s ai r emission s fro mcontainers i n accordance withContaine r Leve l 1 requirements andfacilit y SOPs
. Wast e Processing : MP-1 , MP-2 , LP R Sectio n IV.G. 5 40 CF R63.925 , 71.6(a)(3)(i)(A) Veoli acontrol s ai r emission s fro mcontainers i n accordance withContaine r Leve l 1 requirements an

dfacilit y SOPs
. Wast e Processing : MP-1 , MP-2 , LP R Sectio n rV .G. 6 4 0 CF R71.6(a)(3 ) Veoli acontrol s air emission s fro mcontainers i n accordance withContaine r Leve l 1 requirements andfacilit y SOPs
. Wast e Processing : MP-1 , MP-2 , LP R Sectio n IV.G. 7 4 0 CF R6 1 Subpar t F F Standar

dwor k practice s a

s reflecte di n SOP s ar

e followe dfo r

containers o f benzene-containing waste . Wast e Processing : MP-1 , MP-2 , LP R Sectio n IV.G. 8 40 CFR71.6(a)(3)(i)(B ) VOM/HA Pemissio n calculation s performedan drecordedusin g TANK S program . Liqui d Wast

e Storage Tanks : Requirement s Liqui dWast

e Storage Tanks Sectio n rV .H. l 3 5 IA C 219.30 1 Recordkeeping - VO M emissio n rat e calculations
. Liqui dWast

e Storage Tank s Sectio n TV.H. 2 3 6 IA C 219.142 LDA Rprogra mincludin g inspections , monitoring an dcorrectiv e action s ha

s bee n implemented
. Liqui dWast

e Storage Tank s Sectio n IV.H. 3 40 CF R60.112 b Close dven t syste mandcontro l devic e installe dan doperate dfo r Tanks 300 , 302 , 304,306 , 30 8 and310
. Liqui dWast

e Storage Tanks Sectio n IV.H. 4 4 0 CFR63.115b(c),3 5 IA C 219.122 an

d219.129 Eac htan k i s equippedwithpermanen t submerge dloadin g pip e an

drecords ar

e retaineda s t o th e desig n o f

th e tank
. liqui dWast

e Storage Tank s Sectio n IV.H. 5 40 CF R6 1 Subpar t F F Standar

dwor k practice s a

s reflecte di n SOP s ar

e followe dfo r

tanks
. Liqui dWast

e Storage Tanks Sectio n IV.H. 6 40 CF R6 3 Subpar t D D Standar

dwor k practice s a

s reflecte di n SOP s ar

e followe dfo r

tanks an dequipmen

t leaks
. Liqui dWast

e Storage Tank s Sectio n IV.H. 7 40 CFR71.6(a)(3)(i)(A)an d (B ) Testing/monitoring/inspectio n o f carbon adsorption syste

mwil l b e conducted
. Liqui dWast

e Storage Tanks Sectio n IV
. H
. 8 4 1 CF R71.6(a)(3 ) Record s wil l b e retainedo n sit e fo r a t least five years . Liqui dWast

e Storage Tanks Sectio n IV.H. 9 Constructio n Permit 8803000 1 VO M emissio n calculation s performe dan drecorded
. Bul kSoli d Waste Storage Facility : Requirement s Bul k Feed Buildin g Sectio n rV .I. l 3 5 IA C 212.32 1 P M emissio n calculation s performe dan drecorded
. Bul k Feed Buildin g Sectio n IV.I. 2 3 5 IA C 219.30 1 Recordkeeping - VO M emissio n rat e calculations
. Bul k Feed Buildin g Sectio n IV.I. 3 3 5 IA C 212.123(a ) Monitoring/Recordkeepin g - Routin e visibl e emission s observations
. Bul k Feed Buildin g Sectio n IV
. 1. 4 40 CF R6 1 Subpar t F F Standar

dwor k practice s a

s reflecte di n SOP s ar

e followe dfo r

tanks
. Monitoring/testin g t

o verif y operatio n a

s aTotall y Enclose dUnit
. Closed-ven t syste mandcontro l devic e installe dan dmaintained
. Bul k Feed Buildin g Sectio n LV.I. 5 40 CF R6 3 Subpar t D D Standar

dwor k practice s a

s reflecte di n SOP s ar

e followe dfo r

tanks an dequipmen

t leaks
. Bul k Fee d Buildin g Sectio n IV.I. 6 4 0 CF R71.6(a)(1 ) SOP s fo r enclosedoperation , negative pressure . Bul k Feed Buildin g Sectio n LV.I. 7 4 0 CFR71.6(a)(3)(i)(A)an d (B ) Testing/monitoring/inspectio n o f carbon adsorption syste

mwil l be conducted
. Routine visibl e emission s observation s ar e performedanddocumented
. Bul k Feed Buildin g Sectio n IV.I. 8 40 CF R71.6(a)(3 ) Record s wil l b e retainedon sit e fo r a t least fiv e years . Dru m Crusher : Requirements Dru mCrushe

r Sectio n IV.J. l 3 5 IA C 219.30 1 Recordkeeping - VO M emissio n rat e calculations
. Dru mCrushe

r Sectio n IV.J. 2 3 5 IA C 212.32 1 P M emissio n calculation s performe dan drecorded
. Dru mCrushe

r Sectio n IV.J. 3 3 5 IA C 212.123(a ) Monitoring/Recordkeepin g - Routin e visibl e emission s observations
.

7 2EMISSIO N

UNI T ID(S ) APPLICATIO N

REFERENC E FO R APPLICABL E REQUIRMEN T CITATIO N COMPLIANC E METHO D Dru mCrushe

r SectionIV.J. 4 40CFR71.6(a)(3)(i)(A)an d (B ) Routin e visibl e emission s observation s ar e performe dan

ddocumented
. Dru mCrushe

r SectionIV.J. 5 4 0 CF R71.6(a)(3 ) Record s wil l b e retainedon sit e fo r a t least fiv e years . Boiler : Requirement s Boile r Sectio n FV.K. l 3 5 IA C 216.12 1 Monitorin g withC O CEM S an drecordkeeping
. Boile r Sectio n rV.K. 2 4 0 CF RSubpar t D c Recordkeeping o f fue l combusted
. Boile r Sectio n IV.K. 3 3 5 IA C 212.123(a ) Monitoring/Recordkeepin g - Routine visibl e emission s observations
. Boile r Sectio n IV.K. 4 Constructio n permit 95080025 NOx , C O emissio n rate calculation s fo r annua l operatin g hours
. Boile r Sectio n TV.K. 5 40 CF R63.5 2 Monitorin g withC O CEM S andrecordkeeping
. Boile r Sectio n IV.K. 6 4 0 CF R6 3 Subpar t DDDD D Wor

k practice s fo r

annua l tune-up , one-tim

e energ y assessment

, submissio n o f NO C andannua

l complianc e report . Boile r Sectio n IV.K. 7 4 0 CFR71.6(a)(3)(i)(A)an d (B ) Annua l visibl e emission s test s ar e performe danddocumented
. Boile r Sectio n TV.K. 8 40 CF R71.6(a)(3 ) Record s wil l b e retainedon sit e fo r a t least fiv e years . A semiannua l complianc e repor t wil l be submitted
. Emergenc y Generators : Requirement s Emergenc y Generators Sectio n IV.L. l 4 0 CF R6 3 Subpar t ZZZ Z Recordo f th e hour s o f operation wil l b e retained
. Emergenc y Generators Sectio n IV.L. 2 40 CF R63.6602 Wor k practic e procedure s fo r

maintenance , inspectio n an didl e operation wil l be followed
. Emergenc y Generators Sectio n IV.L. 3 40 CF R71.6(a)(3 ) Record s wil l be retainedo n sit e fo r a t least fiv e years . A semiannua l complianc e repor t wil l be submitted
. Gasolin e Storage Tank : Requirement s Gasolin e Tan

k Sectio n IV.M. l 3 5 IA C 219.12 2 The tan k i s equippedwithasubmerge dloadin g pipe
. Gasolin e Tan

k Sectio n TV.M. 2 3 5 IA C 219.58 3 The tan k i s equippedwithasubmerge dloadin g pipe
. jasolin e Tan

k Sectio n TV.M. 3 40 CF R71.6(a)(3 ) Record s wil l b e retainedo n sit e fo r a t least fiv e years .

7 3

## VII . RECORDKEEPIN G AN D REPORTIN G Veoli amonitor s an drecord s multipl e operatin g parameter s tha t ar e par t

o f the operatin g record
. Th e Continuou s Emission s Monitorin g Syste m(CEMS ) bein g utilize da t incinerato r Unit s 2 , 3 , an d4 include s measuremen t o f th e combustio n ga s oxygen , carbo n monoxide , hydrocarbon , an dhydroge n chlorid e concentrations ; opacity ; an dga s velocity
. Th e tabl e belo w summarize s th e analyze r specifications
. I f

performanc e o r

stac k test s ar e require dt o b e conducte di n th e future , Veoli awil l recor dan drepor t testin g result s a s describe di n th e appropriat e tes t

plan
. Prio r

t o an y testin g activities , instrumentatio n associate dwit hke y parameter s o f

th e tes t

wil l b e checked , calibrated , o r replaced , a s appropriate , t o ensur e prope r operatio n o f

th e instrumentatio n durin g testing
. Record s o f suc hactivitie s wil l b e retained
. Recorde d Operatin g Parameter s fo rIncinerator s Paramete r Curren tManufacture r Rang e Principl e Oxyge n COS A 0-25 % Electrochemica l Carbo n Monoxid e Ecoche mMC 3 0-20 0 ppm v 0-300 0 ppm v Infrare d Tota l hydrocarbon s TheimoElectr o (Uni t 2 ) Compu r FI D (Uni t

3 & 4 ) 0-10 0 ppm v FID/Infrare d Hydroge n chlorid e Ecoche mMC 3 0-100 0 ppm v Infrare d Opacit y Teledyn e 0-100 % Whit e ligh t Stac k Flo w PS E 0-20,000 acf m(Uni t 2 & 3 ) 0-55,000 acfm(Uni t

4 ) Pressur e dro p A . Recordkeepin g Veoli arecord s informatio n a s require db y th e Hazardou s Wast e Combusto r MAC T standard , 4 0 CF R63
. Uni t

2 , 3 , 4 , Materia l Processin g Area s 1 an d2 , Bul k Fee dBuilding , La b Pac k Repac k Area , an dal l tank s use dfo r th e storag e o f

liqui dwast e ar e subjec t t o requirement s o f 4 0 CF R6 1 Subpar t F F(Benzen e NESHAP)
. I n additio n t o th e genera l recordkeepin g requirement s summarize di n th e followin g tables , thes e unit s compl y wit hal l applicabl e recordkeepin g requirement s a s require db y 4 0 CF R6 1 Subpar t FF
.

7 4Recorde d Operatin g Parameter s
63.1200 , 63.10(b ) an d(c ) General
. Informatio n require dto documen t an dmaintai n complianc e wit hthe regulation s o f

subpart EEE , includin g dat arecorde db y continuou s monitorin g system s (CMS) , an dcopie s o f al l notifications , reports , plans , an dother document s submitte dt o th e Administrator
. 63.1206(b)(5)(ii ) Documentatio n tha t achang e wil l no t

adversel y affec t

complianc e wit hthe emissio n standard s o r operatin g requirements
. 63.1206(b)(ll ) Calculatio n o f hazardou s waste residenc e time
. 63.1206(c)(2 ) Startup , shutdown , an dmalfunctio n plan
. 63.1206(c)(2)(v)(A ) Documentatio n o f you r investigatio n an devaluatio n o f excessiv e exceedance s durin g malfunctions
. 63.1206(c)(3)(v ) Correctiv e measure s fo r an y automati c waste fee dcutoff tha t result s i na n exceedanc e o f

a n emissio n standar do r operatin g parameter limit
. 63.1206(c)(3)(vii ) Documentatio n an dresult s o f the automati c waste fee dcutoff operabilit y testing
. 63.1206(c)(4)(ii ) Emergenc y safet y ven t operatin g plan
. 63.1206(c)(4)(iii ) Correctiv e measure s fo r an y emergenc y safet y ven t opening
. 63.1206(c)(5)(ii ) Metho duse dfo r contro l o f

combustio n syste mleaks
. 63.1206(c)(6 ) Operato r trainin g an dcertificatio n program . 63.1209(c)(2 ) Feedstrea manalysi s plan
. 63.1209(q ) Documentatio n o f change s i n mode s o f

operation
. 63.1211(c ) Documentatio n o f compliance
. Th e followin g operatin g parameter s fo r Unit s 2 , 3 , an d4 ar e automaticall y recorde dever y 1 5 second s int o th e compute r system . Recorde d Operatin g Parameter s Unit s 2 an d 3 Dat a Recorde d Relate d t o Operatin g Paramete r Primar y Combustio n Chambe r Temperatur e Primar y Combustio n Chambe r Temperatur e Secondar y Combustio n Chambe r Temperatur e Secondar y Combustio n Chambe r Temperatur e Stac k 0 2 Correcte d C E M Stac k C O Correcte d C E M Stac k Opacit y C E M Stac k Flo w Stac k Flo w Rat e Spa y Drye r

Adsorbe r

Outlet Tem p Baghous e Inle t Temperatur e Pumpabl e Hazardou s Wast e Fee d Pumpabl e / Tota l Wast e Fee dRat e Soli dHazardou s Wast e Fee d Pumpabl e / Tota l Wast e Fee dRat e Hazardou s Wast e Chlorin e Conten t Chlorin e Fee dRat e Hazardou s Wast e Arsenic , Berylliu man d

Chromiu mConten t Lo w Volatil e Metal s Fee dRat e

7 5Recorde d Operatin g Parameter s Unit s 2 an d 3 Hazardou s Wast e Cadmiu man dLea dConten t Sem i Volatil e Metal s Fee dRat e Hazardou s Wast e Mercur y Conten t Mercur y Fee dRat e As hConten t

o f Hazardou s Wast e As hFee dRat e Recorde d Operatin g Parameter s Uni t4 Dat aRecorde d Relate d t o Operatin g Paramete r Primar y Combustio n Chambe r Temperatur e Primar y Combustio n Chambe r Temperatur e Secondary Combustio n Chambe r Temperatur e Secondar y Combustio n Chambe r Temperatur e Stac k 0 2Correcte d C E M Stac k C O Correcte d C E M Stac k Opacit y C E M Stac k Flo w Stac k Flo w Rat e Spra y Drye r

Absorbe r

Outlet Temperatur e Baghous e Inle t Temperatur e Pumpabl e Hazardou s Wast e Fee d Pumpabl e / Tota l Wast e Fee dRat e Soli dHazardou s Wast e Fee d Pumpabl e / Tota l Wast e Fee dRat e Hazardou s Wast e Chlorin e Conten t Chlorin e Fee dRat e Hazardou s Wast e Arsenic , Berylliu man d

Chromiu mConten t Lo w Volatil e Metal s Fee dRat e Hazardou s Wast e Cadmiu man dLea d

Conten t Sem i Volatil e Metal s Fee dRat e Hazardou s Wast e Mercur y Conten t Mercur y Fee dRat e As hConten t

o f Hazardou s Wast e As hFee dRat e Carbo n Injectio n Flo w Carbo n Injectio n Fee dRat e

Additiona l Recordkeepin g Recorde d Paramete r Metho d Frequenc y Units 2, 3 and 4 Variou s - See table s abov e Compute r Syste m/

CE M Ever y 1 5 Second s Inspectio n A s Require db y 4 0 CF R6 1 Subpart F F Quarterl y Inspectio n Certificatio n Quarterl y Spray Drye rAbsorbe r(SDA ) fo rUni t2, SD A fo rUni t3 and SD A forUni t4 Chlorin e Fee d Programmabl e Logi c Controlle r Pe r Charg e Outle t Temperatur e Thermocoupl e Continuou s Inle t Temperatur e Thermocoupl e Continuou s H C l Extractiv e NDI R Continuou s Lim e Flo w Magneti c Continuou s Baghous e fo rUni t2, Baghouse forUni t3 an d Baghouse fo rUni t4 Stac k Ga s Flo w Annuba r Flowmete r Continuou s Pressur e Dro p Delt aP Transmitte r Continuou s Opacit y Whit e Ligh t Monito r Continuou s 7 6Additiona l Recordkeepin g Materia l Processing Are a1 an d Materia l Processin g Are a2 Throughpu t Operation s Lo g Dail y La b Pac kRepac k Throughpu t Operation s Lo g Dail y Dru m Crushe r Throughpu t Wast e Trackin g Continuou s Bul kFee d Buildin g Wor k Practice s / Operation s Visua l Inspectio n an dInspectio n Lo g Dail y Syste mConditio n Visua l Inspectio n Quarterl y Inspectio n A s Require db y 4 0 CF R6 1 Subpart F F Quarterl y Inspectio n Certificatio n Quarterl y Carbo n Adsorptio n Syste m forBul kFee d Buildin g Exhaus t VO M EP AMetho d2 1 pe r 4 0 CF R6 1 Subpar

t F F Dail y Syste mConditio n Inspectio n Visua l Inspectio n pe r 4 0 CF R6 1 Subpart F F Quarterl y Inspectio n Certificatio n Quarterl y Boile r1 Amoun t an dTyp e o f

Fue l Use d Natura l Ga s Mete r Monthl y Startup , Shutdow n Malfunctio n tim e an d duratio n Operatin g recor d Pe r Occurrenc e Tune-u p Record s Maintenanc e record s an dRepor t Annua l Energ y Assessmen t Repor t Onc e Tan k2, 4, 6

, 8,10 , 20 , 30,40 , 50 , 6 0 Throughpu t Wast e Trackin g Continuou s

Carbon Caniste r2, 4, 6 , 8,10 , 20,30 , 40, 50, 6 0 Exhaus t VO M E P AMetho d2 1 20 % desig n carbo n replacemen t

interva l Conditio n o f

Close dVen t Syste m Visua l Inspectio n Quarterl y Inspectio n A s Require db y 4 0 CF R6 1 Subpart F F Quarterl y Inspectio n Certificatio n Quarterl y Tan k300,302,304,306 , 308, 310, 312, 314 Throughpu t Wast e Trackin g Continuou s Conditio n o f

Close dVen t Syste m Visua l Inspectio n Quarterl y Carbo n Caniste r300, 302,304 , 306,308,310 , 312,31 4 Exhaus t VO M E P AMetho d2 1 20 % desig n carbo n replacemen t

interva l Conditio n o f

Close dVen t Syste m Visua l Inspectio n Quarterl y

7 7Additiona l Recordkeepin g Inspectio n A s Require db y 4 0 CF R6 1 Subpar t F F Quarterl y Inspectio n Certificatio n Quarterl y Tan k39 0 Throughpu t Supplie r invoice s Purchas e frequenc y Emergency Generators Hour s o f operatio n an d descriptio n o f

us e Non-resettabl e hou r mete r Pe r

Occurrenc e Startup , Shutdow n Malfunctio n tim e an d duratio n Operatin g recor dan dmaintenanc e record s Pe r Occurrenc e
Veoli autilize s a n extensiv e preventativ e maintenanc e (PM ) progra mt o kee p equipmen t operationa l an dpreven t breakdown s an dfailures
. Thi s include s aspect s suc ha s documentin g detaile dmaintenanc e historie s o n equipment , routin e inspection , an dlubricatio n program s fo r high-wea r

equipmen t

an dnon-destructiv e testin g o f pipin g an dvessel s usin g technique s lik e ultrasoun dt o asses s integrity
. Th e frequenc y o f thes e activitie s varie s dependin g upo n th e equipment , P M activity , an dth e incinerator' s shutdow n schedule
. B . Reportin g Requirement s Veoli areport s informatio n a s require db y th e Hazardou s Wast e Combusto r MAC T standard , 4 0 CF R63
. Uni t

2 , 3 , 4 , Materia l Processin g Are a1 an d2 , Bul k Fee dBuilding , La b Pac k Repac k Are aan dal l tank s tha t ar e use dfo r

th e storag e o f

liqui dwast e ar e als o subjec t t o requirement s o f

4 0 CF R6 1 Subpar t F F(Benzen e NESHAP)
. I n additio n t o th e genera l reportin g requirement s summarize di n th e followin g tables , thes e unit s compl y wit hal l applicabl e reportin g requirement s a s require db y 4 0 CF R6 1 Subpar t FF
. Genera l Reportin g Requirement s Referenc e Repor t 63.10(d)(4 ) Complianc e progres s reports , i f require da

s aconditio n o f

a n extension o f

th e complianc e date grante dunde r Sec
. 63.6(i)
. 63.10(d)(5)(i ) Periodi c startup , shutdown , an dmalfunctio n reports . 63.10(d)(5)(h ) Immediat e startup , shutdown , an dmalfunctio n reports . 63.10(e)(3 ) Excessiv e emission s an dcontinuou s monitorin g syste m

performanc e report

an dsummary report . 63.1206(c)(2)(ii)(B ) Startup , shutdown , an dmalfunctio n plan
. 63.1206(c)(3)(vi ) Excessiv e exceedance s reports . 63.1206(c)(4)(iv ) Emergenc y safet y ven t openin g reports . Reportin g Requirement s Reportin g Requiremen t Repor tTitl e Frequenc y Uni t2, Uni t3 and Uni t4 Emissio n Inventory Annua l Emission s Repor t Annua l Visua l Inspection s an d Monitorin g Quarterl y inspectio n certificatio n as Require db y 4 0 CF R6 1 Subpar t F F Quarterl y

7 8Reportin g Requirement s Inspectio n as require db y 4 0 CF R61.35 7 Annua l Inspectio n Summar y Annua l La b Pac kRepac k Emissio n Inventory Annua l Emission s Repor t Annua l Dru m Crushe r Emission s Inventory Annua l Emission s Repor t Annua l

Materia l Processing Are a1 an d Materia l Processin g Are a2 Emissio n Inventory Annua l Emission s Repor t Annua l Bul kFee d Buildin g Inspection s as require db y 4 0 CF R61.35 7 Annua l Inspectio n Summar y Annua l Emission s Inventory Annua l Emission s Repor t Annua l Visua l Inspection s an d Monitorin g Quarterl y inspectio n certificatio n as Require db y 4 0 CF R6 1 Subpar t F F Quarterl y Carbo n Adsorptio n Syste m fo rBul kFee d Buildin g Inspection s as require db y 4 0 CF R61.35 7 Annua l Inspectio n Summar y Annua l Visua l Inspection s an d Monitorin g Quarterl y inspectio n certificatio n a s Require db y 4 0 CF R6 1 Subpar t F F Quarterl y Boile r1 an d Propose d Boile r2 Emissio n Inventory Annua l Emission s Repor t Annua l Complianc e Report Annua l Complianc e Report Annua l Tan k2,4 , 6

, 8,10 , 20,30 , 40 , 50, 6 0 Emissio n Inventory Annua l Emission s Repor t Annua l Inspection s as require db y 4 0 CF R61.35 7 Annua l Inspectio n Summar y Annua l Visua l Inspection s an d Monitorin g Quarterl y inspectio n certificatio n as Require db y 4 0 CF R6 1 Subpar t F F Quarterl y Carbon Caniste r2

, 4, 6 , 8,10 , 20,30 , 40 , 50 , 6 0 Inspection s as require db y 4 0 CF R61.35 7 Annua l Inspectio n Summary Annua l Visua l Inspection s an d Monitorin g Quarterl y inspectio n certificatio n as Require db y 4 0 CF R6 1 Subpar t F F Quarterl y Tan k300,302,304,306 , 308, 310,312,31 4 Emissio n Inventory Annua l Emission s Report Annua l Inspection s as require db y 4 0 CF R61.35 7 Annua l Inspectio n Summary Annua l Visua l Inspection s an d Monitorin g Quarterl y inspectio n certificatio n as Require db y 4 0 CF R6 1 Subpar t F F Quarterl y Carbo n Caniste r300,302 , 304, 306,308,310 , 312,31 4 Inspection s a s require db y 4 0 CF R61.35 7 Annua l Inspectio n Summar y Annua l Visua l Inspection s an d Monitorin g Quarterl y inspectio n certificatio n as Require db y 4 0 CF R6 1 Subpar t F F Quarterl y Tan k39 0 Emission s Inventory Annua l Emission s Repor t Annua l

7 9Veoli areport s t o the IEP A eac hoccurrenc e o f a n AWFC O du e t o the combustio n zon e pressur e bein g greate r tha n allowabl e setpoint s whe n evidenc e o f visibl e emission s durin g th e AWFC O exists
. I n addition , an y failur e t o perfor mth e wor k practic e standard s fo r th e emergenc y generator s wil l b e reported
.

8 0