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# OAR Box 1865 Prepped by Charmelle Mathews



### Document

Number: 

# 189 ) IX-A-

2

Docket Number: 

# A-83-2 7

Printed 12/3/20083:22:24 PM

Sheet 189of 198P. 2 

# A-83-2 7 IX-A- 2 

# Protection o f Environmen

t

MA P 27(99 1 

# 4 0

PART S 5 3 T O 6 0 Revise d a s of Jul y 1 , 199 0P. 3

^ Environmenta l Protectio n Agenc y § 60.40 b

o f rdanc e

'an d M $ tt h th e Eho d 1 9 fuantity/hea t 'an d dat e *ac h pretreate d shipmen tjwas receive d 5u s quarter;Xh e nant e an d lotatio n o f theifue l Dretreatmen tfacitfty ; an ; th e t^ta l quantit y an d total/nea tc i tenyo f all/fuel s receive d at/th e affec t edyfacilit f

duringyth e preyfe-u s quarter . /(f ) Fo r an y period s foj r whici r opa c ty , sujsu r diqjfld e o r >Utrogo n oxide s

dat a ar e nb ta v erator>o r th e a signe d st

i i f any/6hange s o f /th e emissio ; fect f e: owne r o r cDft y sh : idlcati oper a syste m durin g th e Perio d avaXability/Operaflon s p/th e ne m an d affecjte d facilit y d ofyflat a unavailabilit y i

o f able , fa - men t ad e i n contro l

tfted : 'perio d e con -

y befor e dat a un - compaDe d wi

t tro l s/ste m an d and/followin g th ( av/ilabill l ag) Th e owner ' o r operato r o f the y fected/iacilit y shall^ubmi ta s i statemen tLntticatin^whether : The/require d continuou s moni - ste m calibration , span , an d ctreck s o r othe r perioai c audi l 5 r hav r no tbee n performed , fied . The/dat a usedyC o sho w cpfmpli - o r wa s rums\ obtained ^ i n ac - wit h approve d method s an d lure s o f Uo s par tan d i s repre - o f plan tperformance . (3 ) Th e rnjymnur

n dat^ trequire ) lav e o r hav e no tbee n met ; ' minimurr/aat a requirement s bee n rafti fo r error * tha twe t able . (4/Complianc e wit h tli e stan i ha s iro tbee n achieve d d ] reportin g peri

< (h ) Foi'th e purpose s o f the^report s require d unde r 5,00.7 . period * o f exc j emission s ar e arefine d assai l 6-mbnit e period s durin g which/th e averag e opacit y exceed s th e ajsplicable/opacit y standard ^ unde r 5JW>.42a(b)/Opaci J level s inexcessofin e app l t y standar d and/th e da t ar e t o Jtf e sub i ministrator/ac h calenda r (i ) Th e jflwner or/opera l fecte d facilit y shal l submi t Subpar t Db—Standard s o f Perform - ance fo r Industrial-Commercial - Institutiona l Stea m Generatin g Units

SOURCE : 5 2 F R47842

. Dec

. 16 , 1987

. unles s otherwis e noted

. § 60.40 b Applicabilit y an d delegatio n o f authority . (a ) Th e affecte d facilit y t o whic h thi s subpar tapplie s i s eac h stea m gen - eratin g uni ttha tcommence s construc - tion , modification , o r reconstructio n afte r Jun e 19 , 1984 , an d tha tha s a hea tinpu tcapacit y fro m fuel s com - buste d i n th e stea m generatin g uni to f greate r tha n 2 9 M W (10 0 millio n Btu / hour) . (b ) An y affecte d facilit y meetin g th e applicabilit y requirement s unde r para - grap h (a ) o f

thi s sectio n an d commenc - in g construction , modification , o r re - constructio n afte r Jun e 19 , 1984 , bu t o n o r befor e Jun e 19 , 1986 . i s subjec t t o th e followin g standards : (1 ) Coal-fire d affecte d facilitie s havin g a hea tinpu tcapacit y betwee n 2 9 an d 7 3 M W (10 0 an d 25 0 millio n Btu/hour) , inclusive , ar e subjec tt o th e particulat e matte r an d nitroge n oxide s standard s unde r thi s subpart . (2 ) Coal-fire d affecte d facilitie s havin g a hea tinpu tcapacit y greate r tha n 7 3 M W (25 0 millio n Btu/hour ) an d meetin g th e applicabilit y require - ment s unde r Subpar tD (Standard s o f performanc e fo r fossil-fuel-fire d stea m generators ; § 60.40 ) ar e subjec tt o th e particulat e matte r an d nitroge n oxide s standard s unde r thi s subpar tan d t o th e sulfu r dioxid e standard s unde r Subpar tD ( § 60.43) . (3 ) Oil-fire d affecte d facilitie s havin g a hea tinpu tcapacit y betwee n 2 9 an d 7 3 M W (10 0 an d 25 0 millio n Btu/hour) , inclusive , ar e subjec tt o th e nitroge n oxide s standard s unde r thi s subpart . (4 ) Oil-fire d affecte d facilitie s havin g a hea tinpu tcapacit y greate r 

### 27 5P. 4

§ 60.41 b tha n 7 3 M W (25 0 millio n Btu/hour ) an d meetin g th e applicability require - ments unde r SubpartD (Standard s o f performance fo r fossil-fuel-fire d stea m generators ; 5 60.40 ) ar

e als o subjec tt o th e nitroge n oxide s standard s unde r thi s subpartan d th e particulat e matte r an d sulfu r dioxid e standard s under Subpar

tD ( § 60.42 and § 60.43) . (c ) Affecte d facilitie s whic h als o mee tth e applicability requirements under SubpartJ (Standard s o f per- formance fo r petroleu m refineries ; § 60.104 ) are subjec tt o th e particulat e matte r an d nitroge n oxide s standard s under thi s subpartan d th e sulfu r di - oxid e standard s unde r SubpartJ (§60.104) . (d ) Affecte d facilitie s whic h als o mee tth e applicabilit

y requirements unde r SubpartE (Standard s of per - formance fo r incinerators ; § 60.50 ) are subjec tt o th e nitroge n oxide s an d par- ticulat e matte r standard s unde r thi s subpart . (e ) Steam generatin g unit s meetin g th e applicabilit

y requirement s unde r Subpar tD a (Standard s o

f perform - ance for electri c utilit y stea m generat - in g units ; 5 60.40a ) are no tsubjec tt o thi s subpart . (f ) An y chang e t o an existin g stea m generatin g uni tfo r th e sol e purpos e o f combustin g gase s containin g TR S a s define d unde r §60.28 1 i s no tconsid - ered a modificatio n unde r § 60.1 4 an d th e stea m generatin g uni ti s no tsub - jec tt o thi s subpart . (g ) I n delegatin g implementatio n an d enforcemen tauthorit y t o a Stat e unde r sectio n 111(c ) of

th e Act , th e followin g authoritie s shal l b e retaine d by th e Administrato r an d no ttrans - ferred t o a State . (1 ) Sectio n 60.44b(f) . (2 ) Sectio n 60.44b(g) . (3 ) Sectio n 60.49b(a)(4) . § 60.41 b Definitions . A s use d i n thi s subpart , al l term s no t defined herei n shal l hav e th e meanin g give n them i n th e Ac tan d i n Subpart A o f thi s part . Annual capacity factormean s th e rati o betwee n th e actua l hea tinpu tt o a steam generatin g uni tfro m th e fuel s liste d i n §60.42b(a) , §60.43b(a) . o r § 60.44b(a) , a s applicable , durin g a cal - endar yea r an d th e potentia l hea t 4 0 CF RCh . I (7-1-9 0 Edition) inpu tt o th e stea m generatin g uni t ha d i tbee n operate d fo r 8,76 0 hour s during a calenda r yea r a tth e maxi - mum stead y stat e desig n hea tinpu t capacity . I n th e cas e o

f stea m generat - in g unit s tha tare rente d or leased , th e actua l hea tinpu tshal l b e determine d base d o n th e combine d hea tinpu t fro m al l operation s o

f th e affecte d fa - cilit y i n a calenda r year . Byproduct/waste mean s any liqui d or gaseou s substanc e produced a t chemica l manufacturin g plant s o r pe - troleu m refinerie s (excep tnatural gas , distillat e oil , o r residual oil ) and com - buste d i n a stea m generatin g uni tfo r hea trecovery or fo r disposal . Gaseou s substance s with carbo n dioxid e level s greate r tha n 50 percen tor carbo n monoxid e level s greate r tha n 1 0 per - cen tar e no tbyproduct/wast e fo r th e purpose s o f

thi s subpart . Chemical manufacturing plants mean s industria l plant s whic h are clas - sifie d b y th e Departmen to f Com - merc e unde r Standar d Industrial Clas - sificatio n (SIC ) Code 28 . Coal mean s al l soli d fuel s classifie d a s anthracite , bituminous , subbitumin - ous , o r lignit e b y th e America n Societ y o f Testin g and Material s i n AST M D388-77 . Standar d Specificatio n fo r Classificatio n o

f Coal s b y Rank (IBR

— se e § 60.17) , coal re

f use , an d petroleu m coke . Coal-derive d syntheti c fuels , in - cludin g bu tno tlimite d t o solven tre - fine d coal , gasifie d coal , coal-oi l mix - tures , an d coal-wate r mixtures , ar e als o include d i n thi s definitio n fo r th e purpose s of

thi s subpart . Coal refuse mean s an y byproducto f coa l minin g o r coa l cleanin g oper - ation s wit h a n as h conten tgreate r tha n 50 percent , by weight , an d a heatin g valu e les s tha n 13,90 0 kJ/k g (6,00 0 Btu/lb ) o n a dr

y basis . Combined

cycle system mean s a syste m i n whic h a separate source , suc h a s a ga s turbine , interna l combus - tio n engine , kiln , etc. , provide s ex - haus tga s t o a hea trecover y stea m generatin g unit . Conventional

technology mean s we t flu e ga s desulfurizatio n (FGD ) tech - nology , dr

y FG D technology , atmos - pheri c fluidize d be d combustio n tech - nology , an d oi l hydrodesulfurizatio n technology . 

### 27 6r ! , - , * i !»sflre5?«i»- " P. 5

Environmenta l Protectio n Agenc y Distillate oil

mean s fue l oil s tha t contai n 0.0

5 weigh tpercen tnitroge n o r les s and compl y with th e specifica tion s fo r fue l oi l numbers 1 an d 2, a s define d by th e America n Society o

f Testin g and Material s i n AST M D396 - 78 , Standard Specification s fo r Fue l Oil s (incorporate d b y reference—see § 60.17) . Dry flue gas desulfurization technology mean s a sulfu r dioxid e contro l syste m tha ti s locate d downstrea m o f th e stea m generatin g uni tan d re moves sulfu r oxide s fro

m th e combus tio n gase s o

f th e steam generatin g uni tb y contactin g th e combustio n gase s with a n alkalin e slurr y o r solu tio n an d formin g a dr

y powder materi al . Thi s definitio n include s device s where th e dr

y powder material i s sub sequentl y converte d t o anothe r form . Alkalin e slurrie s or solution s used i n dr y flu e ga s desulfurizatio n technolo g y includ e bu tare no tlimite d t o lim e an d sodium . Duct burnermean s a device tha t combusts fue l and tha ti s place d i n th e exhaus tductfrom anothe r source , suc h a s a stationar y ga s turbine , inter na l combustio n engine , kiln , etc. , t o allo w th e firin g of

additional fuel t o hea tth e exhaus tgase s before th e ex haus tgase s ente r a hea trecover y steam generatin g unit . Emerging technology mean s an y sulfu r dioxid e contro l syste m tha ti s no tdefine d a s a conventiona l technol ogy unde r thi s section , and fo r whic h th e owne r o r operato r o f th e facility ha s applie d t o th e Administrato r and receive d approva

l t o operate a s an emergin g technolog y unde r § 60.49b(a)(4) . Federally enforceable mean s al l limi tation s an d condition s tha tare en forceabl e b y th e Administrator , in cludin g th e requirements of 4 0 CF R parts 6 0 and 61 , requirements withi n any applicabl e Stat e Implementatio n Plan , an d an y permi trequirements es tablishe d unde r 40 CFR52.2 1 or unde r 4 0 CF R51.1 8 an d 40 CFR51.24 . Fluidized bed combustion technology mean s combustio n of

fue l i n a bed or serie s of bed s (includin g bu tno tlimit e d t o bubblin g be d unit s and circulat in g bed units ) of

limeston e aggregat

e (o r othe r sorben tmaterials ) i n whic h thes e material s are force d upwar d b y § 60.41 b th e flow o

f combustio n air an

d th e gaseou s products o

f combustion . Fuel pretreatment

means a proces s tha tremove s a portio n o f th e sulfu r i n a fue l before combustio n o f th e fue l i n a stea m generatin g unit . Full capacity mean s operatio n o f th e stea m generatin g uni ta t9 0 percen to r mor e o f th e maximum steady-stat e desig n hea tinpu tcapacity . Heat input mean s hea tderived fro

m combustio n o

f fue l i n a steam generat in g uni tan

d doe s no tinclud e th e hea t inpu tfro m preheate d combustio n air , recirculate d flu e gases , o r exhaus t gase s fro m othe r sources , such as gas turbines , interna l combustio n engines , kilns , etc . Heac release rate mean s th e stea m generatin g uni tdesig n hea tinpu tca pacit y (i n M W o r Btu/hour ) divided b y th e furnac e volum e (i n cubi c meter s or cubi c feet) ; th e furnac e volum e i s tha tvolum e bounded by th e fron tfurnac e wall wher e th e burne r i s located , th e furnac e sid e waterwall , and extendin g t o th e leve l jus tbelo w or i n fron to

f th e firs tro

w o f convec tio n pas s tubes . Heat transfermedium mean s an y material tha ti s use d t o transfe r hea t fro m on e poin tt o anothe r point . High heat

release rate mean s a hea t releas e rate greate r tha n 730,000 J / sec-m 3 (70,00 0 Btu/hour-ft s ) . Lignite mean s a typ e o

f coa l classi fie d a s lignit e A o r lignit e B b y th e America n Society o

f Testin g and Ma

terial s i n AST

M D388-77 , Standar d Specificatio n fo r Classificatio n of Coal s b y Rank (IBR—see § 60.17) . Low heat release rate mean s a hea t releas e rat e o f

730,000 J/sec-m 3 (70,00 0 Btu/hour-ft 3 ) or less . Mass-feed

stokersteam generating unit mean s a stea m generatin g uni t wher e soli d fue l i s introduce d directl y int o a retor to r i s fe d directl y ont o a grate wher e i ti s combusted . Maximum heat

input capacity mean s th e ability o

f a steam generat in g uni tt o combus ta state d maximum amoun to f fue l o n a stead y stat e basis , a s determine d b y th e physical desig n an d characteristic s o

f th e steam gener atin g unit . Municipal-type solid

waste mean s refuse , mor

e tha n 50 percen to

f whic h i s waste consistin g o

f a mixtur e o

f 27 7P. 6

§ 60.41 b paper, wood , yar

d wastes , foo d wastes , plastics , leather , rubber , an d othe r combustibl e materials , and noncom - bustibl e material s suc h a s glas s an d rock. Natural gas mean s (1 ) a naturall y occurring mixtur e o

f hydrocarbo n an

d nonhydrocarbo n gase s foun d i n geo - logi c formation s beneat h th e earth' s surface , o f whic h th e principal constit - uen ti s methane ; o r (2 ) liqui d petrole - u m gas , a s define d by th e America n Society fo r Testin g an d Material s i n AST M D1835-82 , "Standard Specifica - tio n for Liquid Petroleu m Gases " (IBR—se e § 60.17) . Noncontinental

area mean s th e Stat e o f Hawaii , th e Virgi n Islands , Guam , American Samoa , th e Commonwealt h o f Puert o Rico , or th e Norther n Marian a Islands . Oil mean s crud e oi l o r petroleu m o r a liqui d fue l derive d from crud e oi l o r petroleum , includin g distillat e an d re - sidua l oil . Petroleum refinery mean s industrial plant s a s classifie d b y th e Departmen t o f Commerc

e unde r Standar d Indus - trial Classificatio n (SIC ) Cod e 29 . Potential sulfurdioxide emission rate mean s th e theoretica l sulfu r diox - ide emission s (ng/J , lb/millio n Bt u hea tinput ) tha twoul d resul tfro m combustin g fue l i n a n uncleane d stat e an d withou tusin g emissio n contro l systems . Process heatermean s a devic e tha ti s primarily use d t o hea ta materia l t o initiat e o r promote a chemica l reac - tio n i n whic h th e materia l participate s a s a reactan to r catalyst . Pulverized

coal-fired

steam generating unit mean s a stea m generatin g uni ti n whic h pulverize d coa l i s intro - duced int o a

n ai r strea m tha tcarrie s th e coal t o th e combustio n chambe r o f th e stea m generatin g uni twher e i ti s fire d i n suspension . Thi s include s bot h conventional pulverize d coal-fire d and micropulverize d coal-fire d stea m gen - eratin g units . Residual oil mean s crud e oil , fue l oi l numbers 1 and 2 tha thav e a nitroge n conten tgreate r tha n 0.05 weigh tper - cent , an d al l fue l oi l number s 4 , 5 and 6 , a s define d b y th e American Society o f Testin g an d Material s i n AST M D396-78 , Standar d Specification s fo r Fue l Oil s (IBR—see § 60.17) . 4 0 CF R Ch . I (7-1-9 0 Edition ) Spreaderstokersteam generating unit mean s a stea m generatin g uni ti n which soli d fue l i s introduce d t o th e combustio n zon e b

y a mechanis m tha t throw s th e fue l ont o a grat e from above . Combustio n take s plac e both i n suspensio n and o n th e grate . Steam generating unit mean s a device tha tcombusts any fuel o r by - product/wast e t o produce steam o r t o hea twate r or any othe r hea ttransfe r medium . Thi s term include s an y mu - nicipal-typ e soli d waste incinerato r with a hea trecover

y steam generatin g uni tor an y stea m generatin g uni ttha t combusts fue l an d i s par to f a cogen - eratio n syste m or a combined cycl e system . Thi s term doe s no tinclud e proces s heater s a s the y ar e define d i n this subpart . Steam generating unit

operating day mean s a 24-hou r perio d betwee n 12:0 0 midnigh tand th e followin g midnigh t durin g whic h an y fue l i s combuste d a t any tim e i n th e stea m generatin g unit . I ti s no tnecessary fo r fue l t o b e com - buste d continuousl y fo r th e entir e 24 - hou r period . Very low sulfuroil

mean s a n oi l tha t contain s n o more tha n 0. 5 weigh tper - cen tsulfu r or that , whe n combuste d withou tsulfu r dioxid e emissio n con - trol , ha s a sulfu r dioxid e emissio n rat e equa l t o or les s tha n 21 5 ng/ J (0. 5 lb / millio n Btu ) hea tinput . Wet flue gas desulfurization technology mean s a sulfu r dioxid e contro l syste m tha ti s locate d downstrea m o f th e stea m generatin g uni tand re - move s sulfu r oxide s from th e combus - tio n gase s o

f th e steam generatin g uni tb y contactin g th e combustio n ga s wit h an alkalin e slurr

y or solutio n an d formin g a liqui d material . Thi s defini - tio n applie s t o device s where th e aque - ou s liqui d materia l produc to f thi s contac ti s subsequentl y converte d t o othe r forms . Alkalin e reagents use d i n we tflu e ga s desulfurizatio n technolo - g y include , bu tare no tlimite d to , lime , limestone , an d sodium . Wet scrubber system mean s an y emissio n contro l devic e tha tmixe s a n aqueou s strea m or slurry with th e ex - haus tgase s from a stea m generatin g uni tt o contro l emission s o f particulat e matte r o r sulfu r dioxide . Wood mean s wood , wood residue , bark, o r an y derivativ e fue l o r residu e ^



### 27 8i t :-J3""HFW3S*r* : * P. 7

% Environmenta l Protectio n Agenc y

thereof , i n any form , including , but no tlimite d to , sawdust , sanderdust , woo d chips , scraps , slabs , millings , shavings , and processe d pellet s made fro m wood or othe r fores tresidues . [5 2 F R47842 , Dec . 16 . 1987 , a s amende d a t 5 4 F R51819 , Dec . 18.1989] § 60.42 b Standar

d fo r sulfu r dioxide . (a ) Excep ta s provided i n paragraph s (b) . (c) , (d) , o

r (j ) o f this section , o n an d afte r th e date o n whic h th e per - formanc e tes ti s complete d or require d t o b e complete d unde r § 60. 8 o f this part , whicheve r date come s first , n o owne r or operato r o

f a n affecte d facili - t y tha tcombusts coal or oi l shal l caus e t o b e discharge d int o th e atmospher e an y gase s tha tcontai n sulfu r dioxid e i n exces s o f 1 0 percen t(0.10 ) o

f th e po - tential sulfu r dioxid e emissio n rat e (9 0 percentreduction ) an d tha tcontai n sulfur dioxid e i n exces s o f th e emis - sion limi tdetermine d accordin g t o th e following formula : E.=(KA+K

fc Hb)/<H.+H„

> where : E , i s th e sulfu r dioxid e emissio n limit , i n ng/ J o r lb/millio n Bt u hea tinput . K . i s 52 0 ng/ J (o r 1. 2 lb/millio n Btu) . K „ i s 34 0 ng/ J (o r 0.8 0 lb/million Btu) . H , i s th e hea tinpu tfro m the combustio

n o f coal , i n J (millio n Btu) , H „ i s th e hea tinpu tfro m th e combustio

n o f oil, i n J (millio n Btu) . Onl y th e hea tinpu tsupplie d t o th e affected facilit

y fro m th e combustio n o

f coa l an d oi l i s counte d unde r thi s sec - tion . N o credi ti s provide d fo r th e hea t inpu tt o th e affecte d facilit y fro m th e combustion o

f natura l gas , wood , mu - nicipal-typ e soli d waste , o r othe r fuel s o r hea tinpu tt o th e affecte d facility fro m exhaus tgase s fro m anothe r source, suc h a s ga s turbines , interna l combustio n engines , kilns , etc . (b ) On an d afte r th e dat e o n whic h th e performance tes ti s complete d or require d t o b e complete d unde r § 60. 8 o f thi s part , whicheve r come s first , n o owne r or operato r o

f a n affecte d facili - t y tha tcombusts coal refus e alon e i n a fluidized be d combustio n stea m gener - atin g uni tshal l caus e t o b e discharge d int o th e atmospher e any gase s tha t contai n sulfu r dioxid e i n exces s o f 2 0 Percen to f th e potentia l sulfu r dioxid e emissio n rat e (8 0 percen treduction ) an d tha tcontai n sulfu r dioxid e i n § 60.42 b exces s o f 52 0 ng/ J (1. 2 lb/millio n Btu ) hea tinput . I

f coal o r oi l i s fired with coa l refuse , th e affecte d facilit y i s sub - jec tt o paragrap h (a ) o

r (d ) o f thi s sec - tion , a s applicable . (c ) O n and afte r th e date o n which th e performanc e tes ti s complete d o r i s require d t o b e complete d under § 60. 8 o f thi s part , whicheve r come s first , n o owne r or operato r o f a n affecte d facility tha tcombusts coa l o r oil , eithe r alon e or i n combinatio n with an y othe r fuel , and tha tuse s an emergin g technolog y fo r th e contro l o f sulfu r dioxid e emissions , shal l caus e t o b e discharge d int o th e atmospher e an y gase s tha tcontai n sulfu r dioxid e i n exces s o f 50 percen to

f th e potentia l sulfu r dioxid e emissio n rate (5 0 per - cen treduction ) and tha tcontai n sulfu r dioxid e i n exces s o f th e emis - sio n limi tdetermine d accordin g t o th e followin g formula : E,=(Kja

c +K

- H d )/H«+H

d ) where : E . i s the sulfu

r dioxid e emissio n limit , expresse d i n ng/ J (lb/mlllio

n Btu ) hea t input , K . i s 26 0 ng/ J (0.6 0 lb/millio n Btu) . K « i s 17 0 ng/ J (0.4 0 lb/mlllion Btu) , E.. i s th e hea tinpu tfro m th e combustio

n o f coal , J (millio n Btu) , HA is th e hea

tinpu tfro m th e combustio

n o f oil . J (millio

n Btu) . Only th e hea tinpu tsupplie d t o th e affecte d facility fro m th e combustio n o f coa l an d oi l i s counte d unde r this sec - tion . N o credi ti s provided fo r th e hea t inpu tt o th e affecte d facility fro m th e combustio n o

f natura l gas , wood , mu- nicipal-typ e soli d waste , or othe r fuels , o r from th e hea tinpu tt o th e affecte d facility fro m exhaus tgase s fro m an - othe r source , suc h a s ga s turbines , in - ternal combustio n engines , kilns , etc . (d ) O n an d afte r th e dat e o n whic h th e performanc e tes ti s complete d or required t o b e complete d under §60.8 o f thi s part , whicheve r come s first , n o owner o r operato r o

f a n affecte d facili - t y liste d i n paragraph s (d ) (1) , (2) , o r (3 ) o f thi s sectio n shal l caus e t o b e dis - charge d int o th e atmospher e an y gase s tha tcontai n sulfu r dioxid e i n exces s o f 52 0 ng/ J (1. 2 lb/millio n Btu ) hea tinpu ti

f th e affecte d facility com - busts coal , o r 21 5 ng/ J (0. 5 lb/millio n Btu ) hea tinpu tlf

th e affecte d facility combusts oi l othe r tha n ver y low 

### 27 9 40-U 0 O — 1

0

# I P. 8

§ 60.43 b sulfu r oil . Percen treductio n require - ments ar e no tapplicabl e t o affecte d facilitie s unde r thi s paragraph . (1 ) Affecte d facilitie s tha thav e a n annua l capacit y facto r fo r coa

l an d oi l o f 3 0 percen t(0.30 ) o r les s an d ar e sub - jec tt o a Federall y enforceabl e permi t limitin g th e operatio n o f th e affecte d facilit y t o an annual capacit y facto r for coa l and oi l o

f 3 0 percen t(0.30 ) o

r less ; (2 ) Affecte d facilitie s locate d i n a noncontinenta l area ; o r (3 ) Affecte d facilitie s combustin g coa l o r oil , alon e or i n combinatio n with any othe r fuel , i n a ductburner a s par to f a combine d cycl e syste m where 30 percen t(0.30 ) o r les s o f th e hea tinpu tt o th e stea m generatin g uni ti s from combustio n o f coal an d oi l i n th e ductburne r an d 7 0 percen t (0.70 ) or mor

e o f th e hea tinpu tt o th e stea m generatin g uni ti s from th e ex - haus tgase s enterin g th e ductburner . (e ) Excep ta s provide d i n paragrap h (f ) o f this section , complianc e with th e emissio n limits , fue l oi l sulfu r limits , and/o r percen treductio n require - ment s unde r thi s sectio n are deter - mine d o n a 30-da

y rollin g average basis . (f ) Excep ta s provided i n paragrap h (j)(2 ) o f thi s section , complianc e with th e emissio n limit s or fue l oi l sulfu r limit s unde r thi s sectio n i s determine d o n a 24-hou r averag e basi s fo r affecte d facilitie s tha t(1 ) hav e a Federall y en - forceabl e permi tlimitin g th e annual capacit y facto r fo r oi l t o 1 0 percen to r less , (2 ) combus tonl y ver y lo w sulfu r oil , an d (3 ) do no tcombus tan y othe r fuel . (g ) Excep ta s provide d i n paragrap h (i ) o f thi s section , th e sulfu r dioxid e emissio n limit s an d percen treductio n requirements unde r thi s sectio n appl y a tal l times , includin g period s o f start - up , shutdown , an d malfunction . (h ) Reduction s i n th e potentia l sulfu r dioxid e emissio n rat e throug h fue l pretreatmen tar e no tcredite d towar d th e percen treductio n require - men tunde r paragrap h (c ) o f thi s sec - tio n unless : (1 ) Fue l pretreatmen tresult s i n a 50 percen tor greate r reductio n i n poten - tia l sulfu r dioxid e emission s and (2 ) Emission s fro m th e pretreate d fue l (withou tcombustio n o r pos tcom - 4 0 CF R Ch . I (7-1-9 0 Edition ) bustio n sulfu r dioxid e control ) ar e equal t o o

r les s tha n th e emissio n limit s specifie d i n paragrap h (c ) o f thi s section . (i ) A n affecte d facility subjec tto paragrap h (a) , (b) , o

r (c ) o f thi s sec - tio n may combus tver

y low sulfu r oi l o r natura l ga s whe n th e sulfu r dioxid e contro l syste m i s no tbein g operate d becaus e o

f malfunctio n o

r mainte - nanc e o f th e sulfu r dioxid e contro l system . (j ) Percen treductio n requirement s are no tapplicabl e t o affecte d facilitie s combustin g onl y ver

y lo w sulfu r oil . Th e owne r or operato r o f a n affecte d facility combustin g ver

y lo w sulfu r oil shal l demonstrat e tha tth e oi l meets th e definitio n o

f ver y low sulfu r oi l by : (1 ) Followin g th e performance testin g procedure s a s described i n § 60.45b(c) or § 60.45b(d) , and followin g th e moni - torin g procedure s a s describe d i n § 60.47b(a ) o r § 60.47b(b ) t o determin e sulfu r dioxid e emissio n rate o r fue l oi l sulfu r content ; or (2 ) maintainin g fuel receipt s a s describe d i n § 60.49b(r) . \ [5 2 F R47842 . Dec . 16 , 1987 . a s amende d a t 5 4 F R51819 . Dec . 18.1989] § 60.43 b Standar

d fo r particulat

e matter. . • (a ) O n an d afte r th e date o n which. , th e initia l performance tes ti s com- plete d o r i s require d t o b e complete d unde r § 60. 8 o

f thi s part , whichever , come s first , n o owne r or operato r o f a n affecte d facility whic h combusts coa l o r combust s mixture s o f coa l with " othe r fuels , shal l caus e t o b e dis- . charge d int o th e atmospher e from, tha taffecte d facility an y gase s tha £ contai n particulat e matte r i n exces s o t th e followin g emissio n limits : v (1 ) 2 2 ng/ J (0.05 lb/millio n Btu) . hea tinput , :-^ (i ) I f th e affecte d facility combusts , onl y coal , o r i y (ii ) If th e affecte d facility combusts : coa l an d othe r fuel s and ha s a n annual , capacity facto r fo r th e othe r fuels - c £ 1 0 percen t(0.10 ) or less . -*M. (2 ) 4 3 ng/ J (0.1 0 lb/millio n Bti& J hea tinpu tif

th e affecte d facility coo p bust s coa l an d othe r fuel s an d ha s M y annua l capacity facto r fo r th e othd p fuel s greate r tha n 10 percen t(0.1 C an d i s subjec tt o a federall y enfo r bl e requiremen tlimitin g operatio n 28 0P. 9

Environmenta l Protectio n Agenc y th e affecte d facility t o a n annual capacit y facto r greate r tha n 1 0 percen t (0.10) fo r fuel s othe r tha n coal . (3 ) 8 6 ng/ J (0.2 0 lb/millio n Btu ) heatinpu ti

f th e affecte d facility com bust s coa l or coal and othe r fuel s an d (i ) Ha s an annual capacit

y facto r fo r coa l o r coa l and othe r fuel s o

f 30 per cent(0.30 ) or less , (ii ) Has a maximum hea tinpu tca pacit y o f 7 3 M W (25 0 millio n Btu / hour ) o r less , (iii ) Ha s a federall y enforceabl e re quiremen tlimitin g operatio n o

f th e affected facility t o a n annual capacit y facto r o f 3 0 percen t(0.30 ) or les s fo r coa l o r coa l and othe r soli d fuels , an d (iv) Constructio n o

f th e affecte d fa cilit y commenced afte r Jun e 19 , 1984 , an d before Novembe r 25 , 1986 . (b ) O n and afte r th e date o n which th e performance tes ti s complete d o r require d t o b e complete d unde r 60. 8 o f thi s part, whicheve r date come s first , n o owne r or operato r o

f a n affecte d fa cilit y tha tcombusts oi l (o r mixture s o f oi l wit h othe r fuels ) and use s a con ventiona l o r emergin g technolog y t o reduc e sulfu r dioxid e emission s shal l cause to b e discharge d int o th e atmos pher e fro m tha taffecte d facility any gase s tha tcontai n particulat e matte r i n exces s o

f 4 3 ng/ J (0.1 0 lb/millio n Btu) hea tinput . (c) O n and afte r th e date o n whic h th e initial performanc e tes ti s com plete d or i s require d t o b e complete d unde r § 60. 8 o

f thi s part , whicheve r dat e come s first , no owne r o r operato r o f a n affecte d facilit y tha tcombusts wood , or wood with othe r fuels , excep t coal, shal l caus e t o b e discharge d from tha taffecte d facilit y an y gase s tha t contai n particulate matte r i n exces s o f th e followin g emissio n limits : (1 ) 4 3 ng/ J (0.1 0 lb/millio n Btu ) hea tinpu ti f th e affecte d facility ha s a n annua l capacity facto r greate r tha n 3 0 percent(0.30 ) fo r wood . (2) 86 ng/ J (0.2 0 lb/millio n Btu ) hea tinpu ti f (i ) Th e affecte d facility ha s a n annua l capacit y facto r o

f 30 percen t (0.30 ) o r les s fo r wood , (ii ) i s subjec tt o a federall y enforcea bl e requirementlimitin g operatio n o f th e affecte d facilit y t o a n annual ca pacit y facto r o

f 3 0 percen t(0.30 ) o r tess for wood , an d § 60.43 b (iii ) Has a maximum hea tinpu tcapacit y o f 7 3 M W (25 0 millio n Btu / hour ) or less . (d ) On and afte r th e date o n which th e initia l performanc e tes ti s com plete d o r i s require d t o b e complete d unde r § 60. 8 o

f thi s part, whicheve r date come s first , n o owne r o r operato r o f an affecte d facility tha tcombusts municipal-typ e soli d waste or mixture s o f municipal-typ e soli d wast e wit h othe r fuels , shal l caus e t o be dis charge d int o th e atmospher e fro m tha taffecte d facility any gase s tha t contai n particulat e matte r i n exces s o f th e followin g emissio n limits : (1 ) 4 3 ng/ J (0.1 0 lb/millio n Btu ) hea tinput , (i ) I f th e affecte d facility combust s onl y municipal-typ e soli d waste , or (ii ) I f th e affecte d facility combust s municipal-typ e soli d waste an d othe r fuel s and ha s an annual capacit y facto r fo r th e othe r fuel s o f 1 0 percen t (0.10 ) o r less . (2 ) 86 ng/ J (0.2 0 lb/millio n Btu ) hea tinpu ti

f th e affecte d facilit

y com busts municipal-typ e soli d wast e or municipal-typ e soli d waste an d othe r fuels ; and (i ) Has an annual capacit y facto r fo r municipal-typ e soli d waste an d othe r fuel s o f 30 percen t(0.30 ) or less , (ii ) Has a maximu m hea tinpu tca pacit y o f 7 3 M W (25 0 millio n Btu / hour ) or less , (iii ) Has a federall y enforceabl e re quiremen tlimitin g operatio n o f th e affecte d facility t o an annual capacit y facto r o f 30 percen t(0.30 ) for munici pal-typ e soli d waste , or municipal-typ e soli d waste and othe r fuels , an d (iv ) Constructio n o

f th e affecte d fa cility commence d afte r Jun e 19 , 1984, . bu tbefore Novembe r 25,1986 . (e ) Fo r th e purpose s o

f thi s section , th e annual capacity facto r i s deter mine d b y dividin g th e actual hea t inpu tt o th e stea m generatin g uni t during th e calenda r yea r fro m th e combustio n o

f coal , wood , o

r munici pal-typ e soli d waste , an d othe r fuels , a s applicable , b y th e potentia l hea t inpu tt o th e stea m generatin g uni ti f th e stea m generatin g uni thad bee n operate d fo r 8,760 hour s a tth e maxi mu m desig n hea tinpu tcapacity . (f ) O n and afte r th e date o n which th e initia l performanc e tes ti s com 

### 28 1P.1 0

§ 60.44 b plete d or i s require d t o b e complete d unde r 60. 8 o

f thi s part , whicheve r date come s first , n o owne r o r operato r o f a n affecte d facility tha tcombusts coal , oil , wood , o r mixture s o f thes e fuel s with any othe r fuel s shal l caus e t o b e discharge d int o th e atmospher e any gase s tha texhibi tgreate r tha n 2 0 per cen topacit

y (6-minute average) , excep tfo r on e 6-minut e perio d pe r hou r o f no tmore tha n 2

7 percen t opacity . (g ) Th e particulat e matte r an d opac ity standard s appl y a tal l times , excep t durin g period s o

f startup , shutdow n or malfunction . -[5 2 F R47842 , Dec . 16 . 1987 . a s amende d a t 5 4 F R51819 . Dec . 18 . 1989 ] § 60.44 b Standar

d fo r nitroge n oxides . (a ) Excep ta s provide d under para grap h (k ) o

f thi s section , o n an

d afte r th e date o n whic h th e initia l perform anc e tes ti s complete d or i s required t o b e complete d unde r § 60. 8 o f this part , whicheve r date come s first , n o owne r or operato r o

f a n affecte d facility tha t i s subjec tt o th e provision s o f thi s sec tio n and tha tcombusts onl y coal , oil , o r natura l ga s shal l caus e t o b e dis charge d int o th e atmospher e from tha taffecte d facility an y gase s tha t contai n nitroge n oxide s (expresse d a s NOi ) i n exces s o

f th e followin g emis sio n limits :

Fuel/Stea m generatin g uni t typ e

(1 ) Natura l ga s an d distillate od . except (4) : (I ) Lo wheat releas e rat e 0 0 Hig h heat releas e rat e (2 ) Residua l oil : 0 ) Lo wheat ralaai n rat e 0 0 Hig h heat releas e rat e (3 ) Coal : 0 ) Mass-fen d stoke r 0 0 Spreade r stoke r an d fluidized be d ffO Pufwt-t d coa l 0Y ) Uonrt

e except (v

) (v ) Lignit e mine d i n Nort h Dakota . Sout h Dakota , o r Montan a an d combuste d i n a sla g *a p «i»naci » (v Q Coal-derive d syntheti c fuel s (4 ) Duc t burne r use d i n a combine d cycl e system : 0 ) Natura l ga s an d dktiillate oi l 0 0 Residua l o i NitroQo n oxkt e 6nvMi0f i (vnit

s no/Jflb / muo n Btu ) (expresse d a s NO. ) heat input

4 3 (0.10 ) 86(0.20 ) 13 0 (0.30 ) 17 0 (0.40 ) 21 0 (0.50 ) 26 0 (0.60 ) 30 0 (0.70 ) 26 0 (0.60 )

34 0 (O.SO

) 21 0 (O.SO

)

8 6 (0.20 ) 17 0 (0.40 ) 4 0 CF R Ch . I (7-1-9 0 Edition ) (b ) Excep tas provide

d unde r para grap h (k ) o

f thi s section , o n an d afte r th e date o n whic h th e initia l perform anc e tes ti s complete d o

r i s require d t o b e complete d under § 60. 8 o f thi s part , whicheve r date come s first , n o owner or operato r o

f a n affecte d facility tha t simultaneousl y combust s mixture s o

f coal , oil , o

r natural gas shal l caus e t o b e discharge d int o th e atmospher e from tha taffecte d facility an y gase s tha tcontai n nitroge n oxide s i n exces s o f a limi tdetermine d b

y us e o f th e fol lowin g formula : E „ = [(EL

r > H r> )+(EL t o H re )+(EL c H«)] / (K n +'a„+Ii < ) where : E , i s the nitroge

n oxide s emissio n limi t(expresse d a s NO,) , ng/

J (lb/millio

n Btu ) EL „ i s the appropriat

e emissio n limi tfro m paragrap h (a)(1 ) fo r combustio

n o f natura l ga s o r distillat e oil, ng/ J (lb/millio

n Btu ) H n i s the hea tinpu tfro m combustio

n o f natura l ga s o r distillat e oil , FTj, ^ is the appropriat

e emissio n limi tfro m paragrap h (a)(2 ) fo r combustio

n o f residua l oil , H r e is th e hea

tinpu tfro m combustio

n o f residua l oil , EL , i s the appropriat

e emissio n limi tfro m paragrap h (a)(3 ) fo r combustio

n o f coal , an d Km i s th e hea tinpu tfro m combustio

n o f coal. (c ) O n and afte r th e date o n which th e initia l performance tes ti s com plete d o r i s required t o b e complete d unde r § 60. 8 o

f this part , whicheve r come s first , n o owner o

r operato r o

f a n affecte d facility tha tsimultaneousl y combust s coal o r oil , o r a mixtur e o f thes e fuel s with natural gas . an d wood , municipal-typ e soli d waste , o r an y othe r fue l shal l caus e t o b e discharge d int o th e atmospher e an y gase s tha t contai n nitroge n oxide s i n exces s o f th e emissio n limi tfo r th e coa l or oil , or mixtur e o

f thes e fuel s wit h natural ga s combuste d i n th e affecte d facility , a s determine d pursuan tt o paragraph ' (a ) o r (b ) o

f this section , unles s th e af * fecte d facility ha s an annual capacit y facto r fo r coa l or oil . or mixtur e o t thes e fuel s wit h natural ga s o f 1 0 per- , cen t(0.10 ) o r les s an

d i s subjec tt o ft federall y enforceabl e requirement ; tha tlimit s operatio n o

f th e facility t a a n annual capacit

y facto r o

f 1 0 per t - ^

28 2P.1 1



# n Environmenta l Protectio n Agency

cen t(0.10 ) or les s fo r coal , oil , o r a mixtur e o

f thes e fuel s with natural gas . (d ) O n and afte r th e date on which th e initia l performanc e tes ti s com - plete d o r i s require d t o b e complete d unde r § 60. 8 o

f thi s part , whicheve r dat e come s first , n o owne r or operato r o f a n affecte d facility tha tsimulta - neousl y combusts natural ga s wit h wood , municipal-typ e soli d waste , o r othe r soli d fuel , excep tcoal , shal l caus e t o b e discharge d int o th e atmos - phere from tha taffecte d facility an y gase s tha tcontai n nitroge n oxide s i n exces s o f 13 0 ng/ J (0.3 0 lb/millio n Btu ) hea tinpu tunles s th e affecte d fa - cilit y ha s a n annual capacit

y facto r fo r natural ga s of

1 0 percen t(0.10 ) o r les s an d i s subjec tt o a federall y enforcea - bl e requiremen ttha tlimit s operatio n o f th e affecte d facility t o a n annual capacit y facto r o

f 1 0 percen t(0.10 ) o

r les s fo r natural gas . (e ) On an d afte r th e dat e o n which th e initia l performanc e tes ti s com - plete d or i s require d t o b e complete d under §60. 8 o

f thi s part , whicheve r dat e come s first , n o owne r or operato r o f a n affecte d facility tha tsimulta - neousl y combusts coal , oil , or natural ga s with byproduct/wast e shal l caus e to b e discharge d int o th e atmospher e fro m tha taffecte d facility any gase s tha tcontai n nitroge n oxide s i n exces s o f a n emissio n limi tdetermine d by th e followin g formul a unles s th e affecte d facilit y ha s a n annua l capacit y facto r for coal , oil , an d natural ga s o f 10 per - cent(0.10 ) o r les s an d i s subjec tt o a federally enforceabl e requiremen t which limit s operatio n of th e affecte d facilit y t o an annual capacit

y facto r o f 1 0 percen t(0.10 ) o r less : E.= [(EL „ H r ,)+(EL r e H„) + (EL

, H,)] / (B^+H^+H. ) where : E. i s th e nitrogen oxide s emission limi t(ex - presse d as NOi) . ng/

J (lb/millio n Btu ) EL,, i s th e appropriat

e emission limi tfro

m paragrap h (a)(1 ) for combustion o f natura l ga s or distillate oil , ng/

J (lb/millio n Btu) . R n i s th e hea tinputfro

m combustion o

f natura l gas , distillate oi l an

d gaseous by- product/waste , ng/J (lb/millio n Btu) . EL n i s th e appropriat

e emissio n limi tfro

m paragrap h (a)(2 ) fo r combustion o f residua l oil . ng/J (lb/millio n Btu ) § 60.44 b H r o i s th e heatinputfro

m combustio

n o f residua l oil and/o r liqui

d byproduct

/ waste . EL < i s th e appropriat

e emissio n limitfro

m paragrap h (a)(3 ) fo

r combustio

n o f coal , an d H ci s th e hea tinputfro

m combustio

n o f coal . (f ) An y owne r o r operato r o

f a n affecte d facility tha tcombust s byprod uct/wast e with eithe r natura l ga s or oi l ma y petitio n th e Administrato r withi n 18 0 day s o f th e initial startu p o f th e affecte d facility t o establis h a nitroge n oxide s emissio n limi twhic h shal l apply specificall y to tha taffect - ed facility whe n th e byproduct/wast e i s combusted . Th e petitio n shal l in - clud e sufficien tan d appropriat e data , a s determine d by th e Administrator , suc h a s nitroge n oxide s emission s fro m th e affecte d facility , waste composi - tio n (includin g nitroge n content) , an d combustio n condition s t o allo w th e Administrato r t o confir

m tha tth e af

fecte d facility i s unabl e t o compl y with th e emissio n limit s i n paragrap h (e ) o f thi s sectio n an

d t o determin e th e appropriat

e emissio n limi tfo r th e affecte d facility . (1 ) Any owne r or operato r o f an affecte d facility petitionin g for a facili ty-specifi c nitroge n oxide s emissio n limi tunde r thi s sectio n shall : (i ) Demonstrat e complianc e with th e emissio n limit s fo r natural gas and dis - tillat e oi l i n paragrap h (a)(1 ) o f thi s sectio n o r fo r residual oi l i n paragrap h (a)(2 ) o f thi s section , a s appropriate , by conductin g a 30-da

y performanc e tes ta s provided i n 8 60.46b(e) . Durin g th e performanc e tes tonl y natura l gas , distillat e oil , or residua l oi l shal l b e combuste d i n th e affecte d facility ; an d (ii ) Demonstrat e tha tth e affecte d facility i s unabl e t o comply with th e emissio n limit s fo r natural gas and dis - tillat e oi l i n paragrap h (a)(1 ) o f thi s sectio n or fo r residual oi l i n paragrap h (a)(2 ) o f thi s section , a s appropriate , whe n gaseou s or liqui d byproduct / waste i s combuste d i n th e affecte d fa - cility unde r th e sam e condition s an d usin g th e sam e technologica l syste m o f emissio n reductio n applie d whe n demonstratin g complianc e under para- grap h (f)(l)(i ) o

f thi s section . (2 ) Th e nitroge n oxide s emissio n limit s fo r natura l ga s or distillat e oi l i n 28 3P.1 2

§ 60.45 b paragrap h (a)(1 ) o

f thi s sectio n o

r fo r residua l oi l i n paragrap h (a)(2 ) o f thi s section , a s appropriate , shal l b e appli cabl e t o th e affecte d facility unti l and unles s th e petitio n i s approved b y th e Administrator . I

f th e petitio n i s ap proved b y th e Administrator , a facili ty-specifi c nitroge n oxide s emissio n limi twil l b e establishe d a tth e nitro gen oxide s emissio n leve l achievabl e whe n th e affecte d facility i s combustin g oi l o r natura l ga s an d byproduct / wast e i n a manne r tha tth e Adminis trato r determine s t o b e consisten t with minimizin g nitroge n oxide s emis sions . (g ) An y owne r or operato r o

f a n affecte d facility tha tcombusts hazard ou s waste (a s define d b y 4 0 CF Rpar t 26 1 o r 4 0 CF Rpar t761 ) with natural gas or oi l ma

y petitio n th e Administra to r withi n 18

0 day s of th e initia l start u p o f th e affecte d facility fo r a waiver fro m complianc e wit h th e nitroge n oxide s emissio n limi twhic h applie s specificall y t o tha taffecte d facility . Th e petitio n mus tinclud e sufficien t an d appropriat

e data , a s determine d b y th e Administrator , o n nitroge n oxide s emission s from th e affecte d fa cility , waste destructio n efficiencies , waste compositio n (includin g nitroge n content) , th e quantity o f specifi c waste s t o b e combuste d and combus tio n condition s t o allo w th e Adminis trato r t o determin e i

f th e affecte d fa cility i s abl e t o compl y with th e nitro ge n oxide s emissio n limit s required b y this section . Th e owne r or operato r o f th e affecte d facility shal l demonstrate tha twhe n hazardou s waste i s com buste d i n th e affecte d facility , therma l destructio n efficienc y requirements fo r hazardou s wast e specifie d i n a n ap plicabl e federall y enforceabl e require - > . men tpreclud e complianc e with th e ni - \ troge n oxide s emissio n limit s o f thi s section . Th e nitroge n oxide s emissio n limit s fo r natura l ga s or distillat e oi l i n paragrap h (a)(1 ) o

f thi s sectio n or fo r residual oi l i n paragrap h (a)(2 ) o f thi s section , a s appropriate , are applicabl e t o th e affecte d facility unti l an d unles s th e petitio n i s approved by th e Administrator . (Se e 40 CF R761.70 fo r regulation s applicabl e t o th e inciner atio n of material s containin g polychlo rinate d biphenyl s (PCB's). ) 4 0 CF R Ch . I (7-1-9 0 Edition ) (h ) Fo r purpose s o

f paragrap h (i ) o

f thi s section , th e nitroge n oxid e stand ard s unde r this sectio n apply a tal l time s includin g period s o f startup , shutdown , o

r malfunction . (i ) Excep ta s provided unde r paragrap h (j ) o

f thi s section , complianc e with th e emissio n limit s unde r this sectio n i s determine d o n a 30-da y roll in g averag e basis . (j ) Compliance with th e emissio n limit s unde r thi s sectio n i s determine d o n a 24-hou r average basi s for th e ini tia l performanc e tes tan d o n a 3-hou r averag e basi s fo r subsequen tperform anc e test s fo r any affecte d facilitie s that : (1 ) Combust, alon e or i n combina tion , onl y natural gas , distillat e oil , o r residual oi l with a nitroge n conten to f 0.3 0 weigh tpercen tor less ; (2 ) Hav e a combine d annual capacit y facto r o f 1 0 percen tor les s fo r natural gas , distillat e oil , and residua l oi l with a nitroge n conten to

f 0.30 weigh tper cen to r less ; and (3 ) Ar e subjec tt o a Federall y en forceabl e requiremen tlimitin g oper atio n o f th e affecte d facility t o th e firin g o f natural gas , distillat e oil , and/o r residual oi l with a nitroge n conten tof

0.3 0 weigh tpercen to r les s an d limitin g operatio n o f th e affecte d facilit y t o a combine d annual capacit y facto r o f 10 percen tor les s fo r natural gas . distillat e oil , an

d residua l oi l and a nitroge n conten tof

0.30 weigh tper cen to r less . (k ) Affecte d facilitie s tha tmee tth e criteri a describe d i n paragraph s (j ) (1) , (2) , an d (3 ) o

f this section , an d tha t hav e a hea tinpu tcapacit y o f 7 3 MW ^ (25 0 millio n Btu/hour ) or less , are no t subjec tt o th e nitroge n oxide s emis sio n limit s unde r thi s section . - ' . [5 2 F R47842 . Dec . 16 , 1987 . a s amende d a t 5 4 F R51825 , Dec . 18 . 1989 ] ; ? r § 60.45 b Complianc e an d performanc e tes t method s an d procedure s fo r sulfu r <U '

_ , oxide . ". •'• ? (a ) Th e sulfu r dioxid e emission ^ standard s unde r § 60.42 b appl y a talj { times . (b ) I n conductin g th e performanc test s require d unde r § 60.8 , th e own e o r operato r shal l us e th e method s an d procedure s i n Appendix A o f thi s p a 

### 28 4

# t Environmenta l Protectio n Agenc y o r th e method s an d procedure s a s specifie d i n thi s section , excep ta s pro - vide d i n § 60.8(b) . Sectio n 60.8(f ) doe s no tappl y t o thi s section . Th e 30-da y notic e require d i n § 60.8(d ) applie s onl y t o th e initia l performanc e tes t unles s otherwis e specifie d b y th e Ad - ministrator . (c ) Th e owne r o r operato r o f a n affecte d facilit y shal l conduc tperform anc e test s t o determin e complianc e wit h th e percen to f

potentia l sulfu r di - oxid e emissio n rat e ( % P. ) an d th e sulfu r dioxid e emissio n rat e (E. ) pur - suan tt o § 60.42 b followin g th e proce - dure s liste d below , excep ta s provide d unde r paragrap h (d ) o f thi s section . (1 ) Th e initia l performanc e tes tshal l b e conducte d ove r th e firs t3 0 consecu - tiv e operatin g day s o f

th e stea m gen - eratin g unit . Complianc e wit h th e sulfu r dioxid e standard s shal l b e de - termine d usin g a 30-da y average . Th e firs toperatin g da y include d i n th e ini - tia l performanc e tes tshal l b e sched - ule d withi n 3 0 day s afte r achievin g th e maximu m productio n rat e a twhic h th e affecte d facilit y wil l b e operated , bu tno tlate r tha n 18 0 day s afte r ini - tia l startu p o f

th e facility . (2 ) l f onl y coa l o r onl y oi l i s com - busted , th e followin g procedure s ar e used : (i ) Th e procedure s i n Metho d 1 9 ar e use d t o determin e th e hourl y sulfu r dioxid e emissio n rat e (En, ) an d th e 30 - da y averag e emissio n rat e (E*,) . Th e hourl y average s use d t o comput e th e 30-da y average s ar e obtaine d fro m th e continuou s emissio n monitorin g syste m o f

5 60.47 b (a ) o r (b) . (ii ) Th e percen to f

potentia l sulfu r dioxid e emissio n rat e ( % P. ) emitte d t o th e atmospher e i s compute d usin g th e followin g formula : % P. = 10 0 d- % R,/100)(l- % R./100 ) where : % R , I s th e sulfu r dioxid e remova l efficienc y o f th e control devic

e as determine

d b y Method 19, I

n percent. % R ti s th e sulfu r dioxid e remova l efficienc y o f fuel pretreatmentas determine d b y Method 19, i n percent. (3 ) I f coa l o r oi l i s combuste d wit h othe r fuels , th e sam e procedure s re - quire d i n paragrap h (c)(2 ) o f thi s sec - tio n ar e used , excep ta s provide d i n th e following : § 60.45 b (i ) A n adjuste d hourl y sulfu r dioxid e emissio n rat e (E h0 ° ) i s use d i n Equatio n 19-1 9 o f Metho d 1 9 t o comput e a n ad - juste d 30-da y averag e emissio n rat e (E.„°) . Th e E h 0 i s compute d usin g th e followin g formula : Eh.* - lE^-E ^ 1-X k )]/X * where : Eh, " i s th e adjusted hourl

y sulfur dioxide emissio n rate , ng/

J (lb/millio n Btu) . Eh o i s th e hourly sulfur dioxide emission rate , ng/ J (lb/millio n Btu) . E . i s th e sulfu r dioxide concentration in fuel s othe r tha n coa

l an d oi l combuste

d i n th e affecte d facility , a

s determine

d b y th e fue l sampling an

d analysi s proce- dure s in Method 19

, ng/ J (lb/millio n Btu) . Th e value E . fo

r eac h fue l lo ti s use d for each hourl

y averag e durin g th e tim e tha tth e lo ti s bein

g combusted . X k i s th e fractio n o

f total hea

tinputfro

m fuel combustion derive

d fro m coal , oil , or coa l an d oil , a s determine

d b y appli - cabl e procedure

s i n Metho

d 19 . (ii ) T o comput e th e percen to f po - tentia l sulfu r dioxid e emissio n rat e ( % P.) , a n adjuste d % R , ( % R,° ) i s com - pute d fro m th e adjuste d E M ° fro m paragrap h (b)(3)(i ) o f

thi s sectio n an d a n adjuste d averag e sulfu r dioxid e inle trat e (En 0 ) usin g th e followin g for - mula : % RV=10 0 (1.0-E.VEa 0 ) T o comput e E^° , a n adjuste d hourl y sulfu r dioxid e inle trat e (E w ° ) i s used . Th e Em

0 i s compute d usin g th e follow - in g formula : Et?-- [Eu-EwU -X»)]/X * where : Eh, ° i s th e adjusted hourl

y sulfur dioxid e inle trate , ng/

J (lb/mlllio n Btu) . Eh i i s th e hourly sulfur dioxide Inle trate , ng/ J (lb/mlllio n Btu) . (4 ) Th e owne r o r operato r o f a n affecte d facilit y subjec tt o paragrap h (b)(3 ) o f thi s sectio n doe s no thav e t o measur e parameter s E , o r X ki f th e owne r o r operato r elect s t o assum e tha tX k =1.0 . Owner s o r operator s o f affecte d facilitie s wh o assum e X k =1. 0 shal l (i ) Determin e % P , followin g th e procedure s i n paragrap h (c)(2 ) o f thi s section , an d (ii ) Sulfu r dioxid e emission s (E. ) ar e considere d t o b e i n complianc e wit h sulfu r dioxid e emissio n limit s unde r S 60.42b . 

### 28 5P. M

§ 60.45 b (5 ) Th e owne r o r operato r o f a n affecte d facility tha tqualifie s unde r th e provision s of

5 60.42b(d ) doe s no thav e t o measure parameter s E , or X kunde r paragrap h (b)(3 ) o

f thi s sectio n i

f th e owner or operato r o

f th e affecte d fa - cility elect s t o measur e sulfu r dioxid e emissio n rate s o f

th e coa l or oi l follow - in g th e fue l samplin g an d analysi s pro - cedure s unde r Metho d 19 . (d ) Excep ta s provide d i n paragrap h (j) , th e owne r or operato r o f a n affect - e d facility tha tcombusts onl y ver y low sulfu r oil , ha s a n annual capacit y facto r fo r oi l o

f 10 percen t(0.10 ) o

r less , an d i s subjec tt o a Federall y en - forceabl e requiremen tlimitin g oper - atio n of th e affecte d facility t o an annual capacit

y facto r fo r oi l o

f 10 percen t(0.10 ) or les s shall : (1 ) Conductth e initia l performance tes tover 2

4 consecutiv e stea m generat - in g uni toperatin g hour s a tful l load ; (2 ) Determin e complianc e with th e standard s afte r th e initia l perform - anc e tes tbase d o n th e arithmeti c aver - ag e o f th e hourl y emission s data durin g eac h stea m generatin g uni top - eratin g da

y i f a continuou s emissio n measuremen tsyste m (CEMS ) i s used , or based o n a dail y averag e i f Metho d 6B or fue l samplin g an d analysi s pro - cedure s unde r Metho d 1 9 are used . (e ) Th e owne r o r operato r o f a n affecte d facility subjec tt o § 60.42b(d)(l ) shal l demonstrat e th e maximum desig n capacity of

th e stea m generat - in g uni tb y operatin g th e facility a t maximum capacity fo r 2 4 hours . Thi s demonstratio n wil l b e made durin g th e initia l performanc e tes tand a subse - quen tdemonstratio n may b e request - ed a tan y othe r time . I f th e 24-hou r averag e firin g rate fo r th e affecte d fa - cilit y i s les s tha n th e maximu m desig n capacit y provided b y th e manufactur - e r o f th e affecte d facility , th e 24-hou r averag e firin g rat e shal l b e use d t o de - termin e th e capacit

y utilizatio n rate fo r th e affecte d facility , otherwis e th e maximu m desig n capacit

y provided by th e manufacture r i s used . (f ) Fo r th e initia l performance tes t require d unde r 9 60.8 , complianc e wit h th e sulfu r dioxid e emissio n limit s an d percen treductio n requirements unde r

. 60.42 b i s base d o n th e averag e emis - sio n rate s an d th e averag e percen tre - ductio n fo r sulfu r dioxid e fo r th e firs t 4 0 CF RCh. I (7-1-9 0 Edition) 30 consecutiv e stea m generatin g uni t operatin g days , excep ta s provided unde r paragrap h (d ) o

f thi s section . Th e initia l performance tes ti s th e onl y tes tfo r whic h a tleas t3 0 day s prio r notic e i s required unles s other - wis e specifie d by th e Administrator . Th e initia l performance tes ti s t o b e schedule d s o tha tth e firs tstea m gen - eratin g uni toperatin g da y o f th e 3 0 successiv e stea m generatin g uni toper - atin g day s i s complete d withi n 30 day s afte r achievin g th e maximu m produc - tio n rat e a twhic h th e affecte d facility wil l b e operated , bu tno tlate r tha n 18 0 day s afte r initia l startu p o f th e fa - cility . Th e boile r load durin g th e 30 - da y perio d doe s no thav e t o b e th e maximu m desig n load , bu tmus tb e representativ e o

f futur e operatin g con - dition s an d includ e a tleas ton e 24 - hou r perio d a tful l load . (g ) Afte r th e initia l performance tes t require d unde r S 60.8 . complianc e with th e sulfu r dioxid e emissio n limit s an d percen treductio n requirements unde r S 60.42b i s base d o n th e averag e emis - sio n rate s an d th e averag e percen tre - ductio n fo r sulfu r dioxid e fo r 3 0 suc - cessiv e stea m generatin g uni toperat - in g days , excep ta s provided under paragrap h (d) . A separate perform - anc e tes ti s complete d a tth e en d o f eac h stea m generatin g uni toperatin g da y afte r th e initia l performanc e test , an d a ne w 30-da

y averag e emissio n rat e an d percen treductio n fo r sulfu r dioxid e ar e calculate d t o sho w compli - anc e with th e standard . (h ) Excep ta s provided unde r para- grap h (i ) o

f thi s section , th e owne r o r operato r o

f a n affecte d facility shal l us e al l vali d sulfu r dioxid e emission s ; dat a i n calculatin g % P , and E* , under 1 paragrap h (c) , o

f this sectio n whethe r ^ o r no tth e minimu

m emission s data re - i quirement s unde r S 60.46b arei l achieved . All vali d emission s data , m-J ! eludin g vali d sulfu r dioxide s emissio n f dat a collecte d durin g period s o f start* ! up , shutdow n an

d malfunction , shatt

j b e use d i n calculatin g % P . an d E ^ pursuan tt o paragrap h (c ) of thi s tion . (i ) Durin g period s o

f malfunctio n maintenanc e o

f th e sulfu r dioxid e tro l system s whe n oi l i s combuste d provide d unde r 5 60.42b(i) , emissi i dat a ar e no tuse d t o calculat e % P . 

### 28 6f.W» 3 T^p? » P.1 5



# 1 Environmenta l Protectio n Agenc y

E , unde r § 60.42

b (a) , (b ) or (c) , howev - er , th e emission s data are use d t o de - termin e complianc e with th e emissio n limi tunde r § 60.42b(i) . (j ) Th e owner or operato r o f a n affecte d facility tha tcombusts ver y lo w sulfu r oi l i s no tsubjec tt o th e compli - ance an d performanc e testin g require - ment s o f thi s sectio n i

f th e owner or operato r obtain s fue l receipts as de - scribed i n § 60.49b(r) . [5 2 F R47842 , Dec . 16 . 1987 , a s amende d a t 5 4 F R51820 . 51825 . Dec . 18 , 1989 ] § 60.46 b Complianc e an d performanc e tes t method s an d procedure s fo r particulat e matte r an d nitroge n oxides . (a ) Th e particulat e matte r emissio n standard s and opacit

y limit s unde r § 60.43b appl y a tal l time s excep t during period s o

f startup , shutdown , o r malfunction . Th e nitroge n oxide s emissio n standard s unde r § 60.44 b appl y a tal l times . (b ) Compliance wit h th e particulate matte r emissio n standard s unde r § 60.43b shal l b e determine d throug h performance testin g a s describe d i n paragraph (d ) o

f thi s section . (c ) Complianc e with th e nitroge n oxide s emissio n standard s unde r § 60.44 b shal l b e determine d throug h performance testin g unde r paragrap h (e ) o r (f) , o r unde r paragraph s (g ) an d (h ) o f thi s section , a s applicable . (d ) T o determin e complianc e with th e particulat e matte r emissio n limit s an d opacit y limit s unde r § 60.43b , th e owne r or operato r o

f a n affecte d facili - t y shal l conduc ta n initia l perform - anc e tes ta s require d unde r 5 60. 8 usin g th e followin g procedure s an d reference methods : (1 ) Metho d 3 B i s use d fo r ga s analy - si s whe n applyin g Metho d 5 o r Metho d 17 . (2 ) Metho d 5 , Metho d 5B , o r Metho d 1 7 shal l b e use d t o measur e th e con - centratio n o

f particulat e matte r a s fol - lows : (i ) Metho d 5 shal l b e use d a taffect - e d facilitie s withou twe tflu e gas desul - furizatio n (FGD ) systems ; and (ii ) Metho d 1

7 may b e use d a tfacili - tie s with o r withou twe tscrubbe r sys - tems provide d th e stac k ga s tempera - tur e doe s no texcee d a temperatur e o f 18 0 * C (32 0 *F) . Th e procedure s o f sec - tion s 2. 1 an d 2. 3 of

Metho d SB ma

y b e § 60.46 b use d i n Metho d 1

7 onl y i f i ti s used afte r a we tFG D system . D o no tus e Metho d 1

7 afte r we tFGD system s i f th e effluen ti s saturate d o r lade n wit

h wate r droplets . (iii ) Metho d 5B i s t o be use d only afte r we tFG D systems . (3 ) Metho d 1 i s use d t o selec tth e samplin g sit e an d th e number o f tra - vers e samplin g points . Th e samplin g tim e fo r eac h ru n i s a tleas t12 0 min - ute s an d th e minimu

m samplin g volum e i s 1.

7 dsc m (6 0 dscf

) excep t tha tsmalle r samplin g time s o r vol - ume s may b e approved by th e Admin - istrato r whe n necessitate d b y proces s variable s o r othe r factors . (4 ) Fo r Metho d 5 , th e temperatur e o f th e sampl e ga s i n th e prob e an d filte r holde r i s monitore d an d i s main - taine d a t16

0 * C (32 0 'F) . (5 ) Fo r determinatio n o

f particulate matte r emissions , th e oxyge n o r carbo n dioxid e sampl e i s obtaine d si - multaneousl y with eac h run o f Metho d 5 , Metho d 5 B o

r Metho d 1

7 by traversin g th e duc ta tth e sam e sam - plin g location . (6 ) Fo r eac h run usin g Metho d 5 , Metho d 5 B o r Metho d 17 , th e emissio n rate expresse d i n nanogram s per joul e hea tinpu ti s determine d using : (i ) Th e oxyge n o

r carbo n dioxid e measurement s an d particulat e matte r measurement s obtaine d unde r thi s sec - tion , (ii ) Th e dr

y basi s F factor , an

d (iii ) Th e dr

y basi s emissio n rate cal - culatio n procedure containe d i n Metho d 1 9 (Appendi x A) . (7 ) Metho d 9 i s use d fo r determinin g th e opacity of

stac k emissions . (e ) T o determin e complianc e with th e emissio n limit s fo r nitroge n oxide s require d unde r § 60.44b , th e owne r or operato r o

f a n affecte d facility shal l conduc tth e performance tes ta s re - quire d unde r § 60. 8 usin g th e continu - ou s syste m fo r monitorin g nitroge n oxide s unde r § 60.48(b) . (1 ) Fo r th e initia l complianc e test , nitroge n oxide s fro

m th e steam gener - atin g uni tare monitore d fo r 3 0 succes - siv e stea m generatin g uni toperatin g day s an d th e 30-da

y average emissio n rat e i s use d t o determin e complianc e with th e nitroge n oxide s emissio n standard s unde r § 60.44b . Th e 30-da y averag e emissio n rate i s calculate d as 

### 28 7

# I P.1 6

§ 60.46 b th e averag e o

f al l hourl y emission s dat a recorde d b y th e monitorin g syste m durin g th e 30-da

y tes tperiod . (2 ) Followin g th e dat e o n whic h th e initia l performanc e tes ti s complete d o r i s require d t o b e complete d unde r § 60. 8 o f thi s part , whicheve r date come s first : th e owner o r operato r of a n affecte d facility which combusts coal or whic h combusts residual oi l havin g a nitroge n conten tgreate r tha n 0.30 weigh tpercen tshal l deter min e complianc e with th e nitroge n oxide s emissio n standard s unde r § 60.44b o n a continuou s basi s throug h th e us e o

f a 30-da y rollin g averag e emissio n rate . A ne w 30-da y rollin g av erag e emissio n rat e i s calculate d eac h stea m generatin g uni toperatin g da y a s th e averag e o

f al l o f th e hourl y ni troge n oxide s emissio n data fo r th e precedin g 30 stea m generatin g uni top eratin g days . (3 ) Followin g th e date o n whic h th e initia l performanc e tes ti s complete d o r i s require d t o b e complete d unde r §60. 8 of thi s part , whicheve r dat e come s first , th e owne r or operato r o f a n affecte d facilit y whic h ha s a hea t inpu tcapacit

y greate r tha n 7

3 M W (25 0 millio n Btu/hour ) an d whic h combusts natura l gas . distillat e oil , or residual oi l havin g a nitroge n conten t o f 0.3 0 weigh tpercen to r les s shal l de termin e complianc e with th e nitroge n oxide s standard s unde r 5 60.44 b o n a continuou s basi s throug h th e us e o f a 30-da y rollin g averag e emissio n rate . A new 30-da

y rollin g averag e emissio n rat e i s calculate d eac h stea m generat in g uni toperatin g da

y a s th e averag e o f al l of th e hourl y nitroge n oxide s emissio n dat a fo r th e precedin g 30 stea m generatin g uni toperatin g days . (4 ) Followin g th e dat e o n whic h th e initia l performanc e tes ti s complete d o r require d t o b e complete d unde r 8 60. 8 of thi s part , whicheve r dat e come s first , th e owne r or operato r o f a n affecte d facilit y whic h ha s a hea t inpu tcapacit

y o f 73 M W (25 0 millio n Btu/hour ) o r les s an d whic h combusts natura l gas , distillat e oil , o r residual oi l havin g a nitroge n conten tof 0.3 0 weigh tpercen to r les s shal l upo n re ques tdetermin e complianc e with th e nitroge n oxide s standard s unde r § 60.44b throug h th e us e of a 30-da y performanc e test . Durin g period s 4 0 CF R Ch . I (7-1-9 0 Edition ) whe n performance test s are no trequested , nitroge n oxide s emission s data collecte d pursuan tto § 60.48b(g)(l ) or § 60.48b(g)(2 ) ar e use d t o calculat e a 30-da

y rollin g average emissio n rat e o n a dail y basi s an d use d t o prepare exces s emissio n reports , but wil l no tb e use d t o determin e compli anc e wit h th e nitroge n oxide s emissio n standards . A new 30-da

y rollin g aver

ag e emissio n rat

e i s calculate d each stea m generatin g uni toperatin g da y a s th e averag e o

f al l o f th e hourl y ni troge n oxide s emissio n data fo r th e precedin g 3

0 steam generatin g uni top eratin g days . (5 ) I f th e owner or operato r o f an affecte d facility whic h combusts residua l oi l doe s no tsampl e an d analyz e th e re sidua l oi l fo r nitroge n content , a s spec ifie d i n §60.49b(e) , th e requirements o f paragrap h (iii ) o

f thi s sectio n appl

y an d th e provision s o

f paragrap h (iv ) o

f thi s sectio n ar

e inapplicable . (f ) T o determin e complianc e wit h th e emissio n limi tfo r nitroge n oxide s require d b y § 60.44b(a)(4 ) fo r duc t burner s use d i n combined cycl e sys tems , th e owne r o r operato r of a n affecte d facility shal l conduc tth e performanc e tes trequired unde r 5 60. 8 . usin g th e nitroge n oxide s an d oxygen ! measuremen tprocedure s i n 4 0 CFR ? part60 Appendix A , Metho d 2d. | Durin g th e performance test , on e samplin g sit e shal l b e locate d a s clos e as i practicabl e t o th e exhaus tof th e tuf- | bine , a s provide d by sectio n 6.1. 1 o/ i Metho d 20 . A secon d samplin g s$ $ shal l b e locate d a tth e outle tt o stea m generatin g unit . Measuremen t o f nitroge n oxide s an d oxyge n sha U jgjj j take n a tbot h samplin g site s d i th e performanc e test . Th e nitrogen j oxide s emissio n rate from th e co s bine d cycl e syste m shal l b e calcula t b y subtractin g th e nitroge n oxi d emissio n rat e measure d a tth e plin g sit e a tth e outle tfro m th e bin e fro m th e nitroge n oxide s emissiq rat e measure d a tth e samplin g site t th e outle tfro m th e stea m gene r unit . (g ) Th e owne r o r operato r o f a n fecte d facility describe d i n 5 60.44 1 o r §60.44b(k ) shal l demonstrat e maximum hea tinpu tcapacity of stea m generatin g uni tb y or , th e facility a tmaximu

m capacity : ^ 

### 28 8P.1 7

Environmenta l Protectio n Agency 2 4 hours

. Th e owne r

o r operato r o f a n affecte dfacility shal l determin e th e maximu mhea t

inpu t capacit y usin g th e hea t los s metho ddescribe di n Sec

tion s 5 an d7. 3 o

f th e ASME Power Test Codes 4. 1 (se e IB R5 60.17(h))

. Thi s demonstratio n o

f maximu mhea t inpu t capacit y shal l b e mad e durin g th e initia l performanc e tes t fo r affect

e dfacilitie s tha t

mee t th e criteri ao

f § 60.44b(j)

. I t

shal l b e mad e withi n 6 0 day s afte r

achievin g th e maximu m productio n rat e a t

whic h th e affecte d facilit y wil l b e operated , bu t

no t late r tha n 180 day s afte r

initia l start-u p o

f eac h facility , fo r

affecte dfacilitie s meetin g th e criteri ao f § 60.44b(k)

. Subsequen t

demonstration s ma y b e re quire db y th e Administrato r a t an y othe r time

. If thi s demonstratio n indi

cate s tha t

th e maximu mhea t

inpu t capacity o

f th e affecte dfacility i s les s tha n tha t state db y th e manufacture r o f th e affecte dfacility , th e maximu m hea t inpu t capacit y determine ddurin g thi s demonstratio n shal l b e use dt o de

termin e th e capacit y utilizatio n rat e fo r th e affecte dfacility

. Otherwise , th e maximu mhea t

inpu t capacit y pro vide db y th e manufacture r i s used

. (h ) Th e owne r

o r operato r o f a n af

fecte dfacilit y describe di n § 60.44b(j ) tha t ha s ahea t

inpu t capacit y greate r tha n 7 3 M

W (25 0 millio n Btu/hour ) shall : (1 ) Conduc t

a n initia l performanc e tes t a s require dunde r

§ 60. 8 over

a minimu mof

2 4 consecutiv e stea mgen eratin g uni t

operatin g hour s a t

maxi

mumhea t

inpu t capacit y t o demon

strat e complianc e wit h th e nitroge n oxide s emissio n standard s unde r 5 60.44 b usin g Metho d7 , 7A

. 7E , o r othe r approve dreferenc e methods ; an d (2 ) Conduc t

subsequen t

performanc e test s onc e pe r

calenda r yea r o r every 40 0 hour s of

operatio n (whicheve r come s first ) t o demonstrat e compli

anc e wit h th e nitroge n oxide s emissio n standard s unde r

5 60.44b ove r

amini

mu mof 3 consecutiv e stea mgenerat

ing uni t operatin g hour s a t

maximu m hea t inpu t capacit y usin g Metho d7 , 7A , 7E , o r othe r approve dreferenc e methods

. [5 2 F R47842 . Dec . 16 , 1987 , a s amende d a t 5 4 F R51820 . 51825 . Dec . 18 . 1989 ; 55 F R 18876, Ma y 7,1990 ] § 60.47 b § 60.47 b Emissio n monitorin g fo r sulfu r dioxide . (a ) Excep t

a s provide di n paragraph s (b ) an d(f ) o f thi s section , th e owne r

o r operato r o f a n affecte dfacility subjec t t o th e sulfu r

dioxid e standard s unde r § 60.42b shal l install , calibrate , main

tain , an doperat e continuou s emissio n monitorin g system s (CEMS ) fo r meas urin g sulfu r

dioxid e concentration s an deithe r

oxyge n (O z ) o r

carbo n diox

id e (C0 2 ) concentration s an dshal l recor dth e outpu t

o f th e systems

. Th e sulfu r dioxid e an deithe r

oxyge n o r carbo n dioxid e concentration s shal l bot h b e monitore da t

th e inle t

an d outle t o f th e sulfu r

dioxid e contro l device

. (b ) A s a n alternativ e t o operatin g CEM S a s require dunde r paragrap h (a ) o f thi s section , a n owne r

o r opera to r ma y elec t

t o determin e th e averag e sulfu r dioxid e emission s an dpercen t reductio n by : (1 ) Collectin g coa l o r

oi l sample s i n a n as-fire dconditio n a t th e inle t

t o th e stea mgeneratin g uni t an danalyz

in g the mfo r

sulfu r an dhea t

conten t accordin g t o Metho d19

. Metho d1 9 provide s procedure s fo r convertin g thes e measurement s int o th e forma t t o b e use di n calculatin g th e averag e sulfu r dioxid e inpu t

rate , o r (2 ) Measurin g sulfu r

dioxid e accord

in g t o Metho d6 B a t

th e inle t o r outle t t o th e sulfu r

dioxid e contro l system

. A n initia l stratificatio n tes t i s require d t o verif y th e adequac y o

f th e Metho d 6 B samplin g location

. Th e stratifica

tio n tes t shal l consis t

o f thre e paire d run s o f asuitabl e sulfur

dioxid e an d carbo n dioxid e measuremen t trai n op erate da t th e candidat e locatio n an da secon dsimila r

trai n operate daccord

in g t o th e procedure s i n Sectio n 3. 2 an dth e applicabl e procedure s i n Sec

tio n 7 of Performanc e Specificatio n 2

. Metho d6B , Metho d6A , o r acombina

tio n o f Method s 6 an d3 o r

3 B o r Method s 6 C an d3A ar e suitabl e meas uremen t techniques

. I f

Metho d6 B i s use dfo r th e secon dtrain , samplin g tim e an dtime r

operatio n ma y b e ad

juste dfo r

th e stratificatio n tes t a s lon g a s a n adequat e sampl e volum e i s collected ; however , bot h samplin g train s ar e t o b e operate dsimilarly

. Fo r th e locatio n t o b e adequat e fo r 

### 28 9P.1 8

§ 60.48 b Metho d 6B 24-hou r tests , th e mean o f th e absolute differenc e betwee n th e thre e paire d run s mus tb e les s tha n 1 0 percent . (3 ) A dail y sulfu r dioxid e emissio n rate , E

D , shal l b e determine d usin g th e procedur e describe d i n Metho d 6A, Sectio n 7.6. 2 (Equatio n 6A-8 ) an d state d i n ng/ J (lb/millio n Btu ) hea t input . (4 ) Th e mea n 30-da

y emissio n rate i s calculate d usin g th e dail y measure d value s i n ng/ J (lb/millio n Btu ) fo r 3 0 successiv e stea m generatin g uni toper - atin g day s usin g equatio n 19-20 o f Metho d 19 . (c ) Th e owne r or operato r o f an affecte d facility shal l obtai n emissio n dat a fo r a tleas t7

5 percen to

f th e op - eratin g hour s i n a tleas t2 2 ou to f 3 0 successiv e boile r operatin g days . I f this minirnn

m dat a requiremen ti s no t me twith a singl e monitorin g system , th e owne r o r operato r of th e affecte d facilit y shal l supplemen tth e emissio n dat a wit h data collecte d wit h othe r monitorin g system s a s approved b y th e Administrato r or th e referenc e method s an d procedure s a s described i n paragrap h (b ) o

f thi s section . (d ) Th e 1-hou

r averag e sulfu r diox - ide emissio n rate s measure d by th e CEM S require d b y paragrap h (a ) o f this sectio n an d require d unde r § 60.13(h ) i s expresse d i n ng/ J or lb / millio n Bt u hea tinpu tan d i s use d t o calculat e th e averag e emissio n rate s unde r 5 60.42b . Eac h 1-hou r average sulfu r dioxid e emissio n rat e mus tb e base d o n more tha n 3 0 minute s o f steam generatin g uni toperatio n and includ e a tleas t2 dat a point s with eac h representin g a 15-minut e period . Hourly sulfu r dioxid e emissio n rate s ar e no tcalculate d i

f th e affecte d facil - ity i s operate d les s tha n 30 minute s i n a 1-hou r perio d an d ar e no tcounte d towar d determinatio n o

f a stea m gen - eratin g uni toperatin g day . (e ) Th e procedure s unde r § 60.1 3 shal l b e followe d fo r installation , eval - uation , an d operatio n o

f th e CEMS . (1 ) Al l CEM S shal l b e operate d i n accordance wit h th e applicabl e proce - dures unde r Performanc e Specifica - tion s 1 , 2 , an d 3 (Appendi x B) . (2 ) Quarterl y accuracy determina - tion s an d dail y calibratio n drif ttest s 4 0 CF

RCh. I (7-1-9 0 Edition) shal l b e performe d i n accordance with Procedure 1 (Appendi x F) . (3 ) Fo r affecte d facilitie s combustin g coal o r oil , alon e or i n combinatio n wit h othe r fuels , th e spa n valu e o f th e sulfu r dioxid e CEM

S a tth e inle tt o th e sulfu r dioxid e contro l device i s 12 5 percen to

f th e maximum estimate d hourl y potentia l sulfu r dioxid e emis - sion s o f th e fue l combusted , and th e spa n valu e o

f th e CEM

S atth e outle t t o th e sulfu r dioxid e contro l devic e i s 50 percen to

f th e maximu

m estimate d hourl y potentia l sulfu r dioxid e emis - sion s of th e fue l combusted . (f ) Th e owne r or operato r o f a n affecte d facility tha tcombust s ver y lo w sulfu r oi l i s no tsubjec tt o th e emissio n monitorin g requirements o f thi s sec - tio n i f th e owne r or operato r obtain s fue l receipt s a s describe d i n § 60.49b(r) . ^ [5 2 F R47842 . Dec

. 16

. 1987 , a s amende da t 5 4 F R51820 , Dec

. 18,1989 ; 5 5 F R5212

. Feb

. 14

. 1990 ; 5 5 F R18876

. Ma y 7 , 1990 ] § 60.48 b Emissio n monitorin g fo r particu - lat e matte r an d nitroge n oxides . (a ) Th e owne r or operato r o f a n affecte d facilit y subjec tt o th e opacit y standar d unde r 5 60.43b shal l install , calibrate , maintain , and operate a con- , tinuou s monitorin g syste m fo r measur - in g th e opacit

y o f emission s dis - charge d t o th e atmospher e and recor d th e outpu to

f th e system . (b ) Excep ta s provided unde r para - graph s (g) , (h) , and (i ) o f this section , th e owne r o r operato r o f a n affected , facilit y subjec tt o th e nitroge n oxides i standard s unde r 5 60.44b shal l install, ; calibrate , maintain , and operate a con- , tinuou s monitorin g syste m fo r measur- ' in g nitroge n oxide s emission s dis - charge d t o th e atmospher e an d record ^ th e outpu to

f th e system . - / (c ) Th e continuou s monitorin g sys-. f terns require d unde r paragrap h (b ) o l thi s sectio n shal l b e operate d an d data ^ recorde d durin g al l period s o f operrt^ atio n o f th e affecte d facility except ^ fo r continuou s monitorin g syste m $ breakdown s an d repairs . Dat a i s re»if . corded durin g calibratio n checks , and ^ zero an d spa n adjustments . ^'ay>k (d ) Th e 1-hou

r average nitrog e oxide s emissio n rate s measure d b y continuou s nitroge n oxide s monito r i 

### 29 0P.1 9

% Environmenta l Protectio n Agenc y quired by paragrap h (b ) o f thi s sectio n an d required unde r 5 60.13(h ) shal l b e expresse d i n ng/ J or lb/millio n Btu hea tinpu tand shal l b e use d t o calcu - lat e th e averag e emissio n rate s under 5 60.44b . Th e 1-hou

r average s shal l b e calculate d usin g th e data point s re - quired unde r 5 60.13(b) . A tleas t2 dat a points mus tb e use d t o calculat e eac h 1-hou r average . (e ) Th e procedure s unde r 5 60.1 3 shal l b e followe d fo r installation , eval - uation , an d operatio n o

f th e continu - ous monitorin g systems . (1 ) Fo r affecte d facilitie s combustin g coal , wood or municipal-typ e soli d waste , th e spa n valu e fo r a continuou s monitorin g syste m fo r measurin g opacit y shal l b e betwee n 6

0 an d 8 0 percent . (2 ) Fo r affecte d facilitie s combustin g coal , oil , or natural gas , th e spa n valu e fo r nitroge n oxide s i s determine d as follows :

Oi l Coa l Mixture s Fue l Spa n values fo r nitroge n oxide

s (PPM ) 50 0 SC O 1,00 0 500(x+y)+1.000 z where : x i s th e fractio n o f

tota l hea t

inpu t derive d fro mnatura l gas , y i s th e fractio n o f

tota l hea t

inpu t derive d fro moil , an d z i s th e fractio n o f

tota l hea t

inpu t derive d fro mcoal

. (3 ) All spa n value s compute d unde r paragraph (e)(2 ) o

f thi s sectio n fo r combustin g mixture s o f regulate d fuel s are rounde d t o th e neares t500 ppm . (f ) Whe n nitroge n oxide s emissio n dat a are no tobtaine d becaus e o f con - tinuou s monitorin g syste m break- downs , repairs , calibratio n check s an d zer o an d spa n adjustments , emissio n dat a wil l b e obtaine d b y usin g standb y monitorin g systems , Metho d 7, Metho d 7A , o r othe r approved refer - ence method s t o provid e emissio n data for a minimim

n o f 7 5 percen to

f th e op - eratin g hour s i n eac h stea m generat - in g uni toperatin g day , i n a tleas t2 2 ou to f 3 0 successiv e stea m generatin g uni toperatin g days . § 60.49 b (g ) Th e owne r o

r operato r o

f a n affecte d facility tha tha s a hea tinpu t capacit y o f 7 3 M W (25 0 millio n Btu / hour ) or less , an d whic h ha s a n annua l capacit y facto r fo r residua

l oil havin g a nitroge n conten to

f 0.30 weigh tper- cen tor less , natura l gas , distillat e oil , or any mixtur e o

f thes e fuels , greate r tha n 10 percen t(0.10 ) shall : (1 ) Compl

y wit h th e provision s o f paragraph s (b) , (c) , (d) , (e)(2) , (e)(3) , and (f ) o f thi s section , or (2 ) Monito r stea m generatin g uni t operatin g condition s and predictnitro - ge n oxide s emissio n rate s a s specifie d i n a pla n submitte d pursuantt o § 60.49b(c) . (h ) Th e owne r or operato r o f an affecte d facilit y whic h i s subjec tt o th e nitroge n oxide s standard s o f 5 60.44b(a)(4 ) i s no trequired t o instal l or operate a continuou s monitorin g syste m t o measur e nitroge n oxide s emissions . (i ) Th e owne r or operato r o f a n affecte d facUit

y describe d i n 5 60.44b(j ) or 5 60.44b(k ) i s no trequired t o instal l o r operat e a continuou s monitorin g syste m fo r measurin g nitroge n oxide s emissions . (Approve db y th e Offic e of Managemen t an dBudge t

unde r contro l numbe r

2060

- 0072 ) [5 2 F R47842 , Dec

. 16 , 1987 , a s amende da t 5 4 F R51825

. Dec

. 18

. 1989 ] § 60.49 b Reportin g an d recordkeepin g re - quirements

. (a ) Th e owne r or operato r o f eac h affecte d facilit y shal l submi tnotifica - tio n o f th e date o

f initia l startup , a s provided b y § 60.7 . Thi s notificatio n shal l include : (1 ) Th e desig n hea tinpu tcapacit y o f th e affecte d facility and identificatio n o f th e fuel s t o b e combuste d i n th e affecte d facility , (2 ) I f applicable , a cop y o

f an y Fed - erall y enforceabl e requiremen ttha t limit s th e annua l capacit y facto r fo r an y fue l o r mixtur e o f fuel s unde r §§60.42b(d)(l) . 60.43b(a)(2) , (a)(3)(iil) , (c)(2)(il) , (d)(2)(ili) , 60.44b(c) . (d) , (e) , (i) , (J) , (k) . 60.45b(d) . (g) . 60.46b(h) , o r 60.48b(i) , (3 ) Th e annua l capacit y facto r a t whic h th e owne r or operato r antici - pate s operatin g th e facility base d o n 

### 29 1P.2 0

§ 60.49 b al l fuel s fire d an d base d o n eac h indi vidua l fue l fired , and , (4 ) Notificatio n tha ta n emergin g technolog y wil l b e use d fo r controllin g emission s o

f sulfu r dioxide . Th e Administrato r wil l examin e th e descrip tio n o f th e emergin g technolog y an d will determin e whethe r th e technolo g y qualifie s a s a n emergin g technolo gy . I n makin g thi s determination , th e Administrato r ma

y require th e owner o r operato r o

f th e affecte d facility to submi tadditiona l informatio n con cernin g th e contro l device . Th e affect ed facility i s subjec tt o th e provision s o f 5 60.42b(a) unles s an d unti l this determinatio n i s mad e by th e Adminis trator . (b ) Th e owne r o r operato r o f eac h affecte d facility subjec tt o th e sulfu r dioxide , particulat e matter , and/o r ni troge n oxide s emissio n limit s unde r 5 5 60.42b . 60.43b , an d 60.44 b shal l submi tt o th e Administrato r th e per formance tes tdat a fro m th e initia l performance tes tan d th e performance evaluatio n o

f th e CEM S usin g th e ap plicabl e performanc e specification s i n appendix B . Th e owne r o r operato r o f eac h affecte d facility described i n 5 60.44b(J) o r 5 60.44b(k ) shal l submi t t o th e Administrato r th e maximum hea tinpu tcapacity data fro m th e demonstratio n of

th e maximum hea t inpu tcapacit

y o f th e affecte d facility . (c ) Th e owne r o r operato r o f eac h affecte d facility subjec tt o th e nitroge n oxide s standar d of

§ 60.44b wh o seek s t o demonstrate complianc e with thos e standard s throug h th e monitorin g o f stea m generatin g uni toperatin g condi tion s unde r th e provision s o f 5 60.48b(g)(2 ) sha h submi tt o th e Administrato r fo r approva l a pla n tha t identifie s th e operatin g condition s t o b e monitore d unde r 5 60.48b(g)(2 ) and th e record s t o b e maintaine d unde r 5 60.49b(j) . Thi s pla n shal l b e submit te d t o th e Administrato r fo r approva l withi n 360 day s o

f th e initia l startu p o f th e affecte d facility . Th e pla n shall : (1 ) Identif

y th e specifi c operatin g condition s t o b e monitore d and th e re lationshi p betwee n thes e operatin g condition s an d nitroge n oxide s emis sio n rate s (i.e. , ng/ J o r lbs/millio n Btu hea tinput) . Stea m generatin g uni top eratin g condition s include , bu tar e no t limite d to , th e degre e o f stage d com 4 0 CF R Ch . I (7-1-9 0 Edition ) bustio n (i.e. , th e rati o o f primar y ai r t o secondary and/o r tertiary air ) an d th e leve l o

f exces s ai r (i.e. , flu e ga s oxyge n level) ; (2 ) Includ e th e dat

a an d informatio n tha tth e owne r or operato r use d t o identif y th e relationshi p betwee n ni troge n oxide s emissio n rate s and thes e operatin g conditions ; (3 ) Identif

y how thes e operatin g conditions , includin g steam generatin g uni tload , wil l b e monitore d unde r § 60.48b(g ) o n an hourl y basi s by th e owne r or operato r during th e perio d o f operatio n o

f th e affecte d facility ; th e qualit y assuranc e procedure s or prac tice s tha twil l b e employe d t o ensur e tha tth e data generate d b y monitorin g thes e operatin g condition s wil l b e rep resentativ e and accurate ; an d th e typ e and formato

f th e records o

f thes e op eratin g conditions , includin g stea m generatin g uni tload , tha twil l b e maintaine d by th e owner or operato r unde r 5 60.49b(j) . I f th e pla n i s approved , th e owne r or operato r shal l maintai n record s o f pre dicte d nitroge n oxid e emissio n rate s and th e monitore d operatin g condi tions , includin g stea m generatin g uni t load , identifie d i n th e plan . (d ) Th e owne r o r operato r o f a n affecte d facilit y shal l recor d and main tai n record s o

f th e amounts o

f eac h fue l combuste d durin g eac h da y and calculat e th e annual capacit y facto r individuall y fo r coal , distillat e oil , re sidual oil , natural gas . wood , and mu nicipal-typ e soli d waste fo r eac h calen da r quarter . Th e annua l capacit

y facto r i s determine d o n a 12-mont h rollin g averag e basi s with a new annua l capacit

y facto r calculate d a t th e en d o f eac h calenda r month . (e ) Fo r a n affecte d facility tha tcom busts residual oi l and meet s th e crite ri a unde r 5

5 60.46b(e)(4) , 60.44b(J) , or (k) . th e owne r o r operato r shal l main tai n record s o

f th e nitroge n conten to

f th e residual oi l combuste d i n th e affecte d facility and calculat e th e averag e fue l nitroge n conten to n a pe r cal enda r quarte r basis . Th e nitroge n con ten tshal l b e determine d usin g AST M Metho d D3431-80 , Tes tMetho d fo r Trace Nitroge n i n Liquid Petroleu m ? Hydrocarbon s (IBR-se e 5 60.17) , or. ? fue l suppliers . I

f residual oi l blend s f 

### 29 2 

# IP.2 1 

# t

•mmEnvironmenta l Protectio n Agenc y

ar e bein g combusted , fue l nitroge n specification s may b e prorate d based o n th e rati o o

f residual oil s o

f differ - en tnitroge n conten ti n th e fue l blend . (f ) Fo r facilitie s subjec tt o th e opaci - ty standard unde r 5 60.43b , th e owner or operato r shal l maintai n records o f opacity . (g ) Excep ta s provided unde r para- grap h (p ) o

f this section , th e owner or operato r o

f an affecte d facility subjec t t o th e nitroge n oxide s standard s unde r 5 60.44 b shal l maintai n record s o f th e followin g informatio n fo r eac h steam generatin g uni toperatin g day : (1 ) Calendar date . (2 ) Th e averag e hourl y nitroge n oxide s emissio n rate s (expresse d as NOj ) (ng/ J o r lb/millio n Bt u hea t input) measure d or predicted . (3 ) Th e 30-da

y averag e nitroge n oxide s emissio n rate s (ng/ J o r lb/mil - lio n Btu hea tinput ) calculate d a tth e en d o f eac h stea m generatin g uni top - eratin g da

y from th e measure d o

r pre - dicte d hourl y nitroge n oxid e emissio n rate s fo r th e precedin g 30 stea m gen - eratin g uni toperatin g days . (4 ) Identificatio n of

th e stea m gener - atin g uni toperatin g day s whe n th e calculate d 30-da

y averag e nitroge n oxide s emissio n rate s are i n exces s o f th e nitroge n oxide s emission s stand - ards unde r 5 60.44b , wit h th e reason s fo r suc h exces s emission s a s wel l a s a descriptio n of

correctiv e action s taken . (5 ) Identificatio n o

f th e stea m gener - atin g uni toperatin g day s fo r which pollutan tdat a hav e no tbee n obtained , includin g reason s fo r no tobtainin g sufficien tdat a an d a descriptio n o f correctiv e action s taken . (6 ) Identificatio n of

th e time s whe n emissio n dat a hav e bee n exclude d fro m th e calculatio n o

f averag e emis - sio n rate s an d th e reason s fo r exclud - in g data . (7 ) Identificatio n of

"F " facto r use d for calculations , metho d o f determina - tion , and typ e o

f fue l combusted . (8 ) Identificatio n of

th e time s whe n th e pollutan tconcentratio n exceede d ful l spa n o

f th e continuou s monitorin g system . (9 ) Descriptio n o

f an y modification s t o th e continuou s monitorin g syste m tha tcoul d affec tth e ability o f th e continuou s monitorin g syste m t o § 60.49 b comply wit h Performance Specifica - tio n 2 o r 3 . (10 ) Result s o

f dail y CEM

S drif t test s an d quarterl y accurac y assess - ment s a s require d unde r Appendix F , Procedure 1 . (h ) Th e owne r or operato r o f an y affecte d facility i n an y categor y liste d i n paragraph s (h ) (1 ) o r (2 ) o f thi s sec - tio n i s require d t o submi texces s emis - sio n reports fo r any calenda r quarte r durin g whic h ther e are exces s emis - sion s fro m th e affecte d facility . I f ther e are n o exces s emission s durin g th e calenda r quarter , th e owner or op - erato r shal l submi ta reportsemiannu - all y statin g tha tn o exces s emission s occurred durin g th e semiannual re - portin g period . (1 ) An y affecte d facility subjec tt o th e opacity standard s unde r 5 60.43b(e ) or t o th e operatin g parame - te r monitorin g requirements unde r 5 60.13(0(1) . (2 ) Any affecte d facility tha ti s sub - jec tt o th e nitroge n oxide s standar d of 5 60.44b , an d tha t (i ) Combusts natura l gas , distillat e oil , o r residual oi l with a nitroge n con - ten to f 0. 3 weigh tpercen tor less , o r (ii ) Ha s a hea tinpu tcapacit y of 7 3 M W (25 0 millio n Btu/hour ) o r les s an d i s require d t o monito r nitroge n oxide s emission s o n a continuou s basi s unde r 5 60.48b(g)(l ) o r steam generat - in g uni toperatin g condition s unde r 5 60.48b(g)(2) . (3 ) Fo r th e purpos e o f 5 60.43b , exces s emission s are define d a s al l 6 - minut e period s durin g whic h th e aver - ag e opacity exceed s th e opacit y stand - ard s unde r 5 60.43b(f) . (4 ) Fo r purpose s of

5 60.48b(g)(l) , exces s emission s are define d a s an y calculate d 30-da

y rollin g average nitro - ge n oxide s emissio n rate , as deter - mine d unde r § 60.46b(e) , whic h ex - ceed s th e applicabl e emissio n limit s i n 5 60.44b . (i ) Th e owne r o r operato r o f an y affecte d facilit y subjec tt o th e continu ou s monitorin g requirements fo r nitro ge n oxide s unde r 5 60.48(b ) shal l submi ta quarterl y reportcontainin g th e informatio n recorded unde r para- grap h (g ) o

f thi s section . All quarterl y reports shal l b e postmarke d b y th e 30th da y followin g th e en d o

f eac h cal - enda r quarter . 

### 29 3P.2 2

§ 60.49 b (j ) Th e owne r o r operato r o f an y affecte d facility subjec tt o th e sulfu r di oxid e standard s unde r 5 60.42b shal l submi twritte n report s t o th e Adminis - trato r fo r ever

y calenda r quarter . All quarterl y reports shal l b e postmarke d by th e 30t

h da y followin g th e en d o

f eac h calenda r quarter . (k ) Fo r eac h affecte d facility subjec t t o th e complianc e an d performance testin g requirements o

f § 60.45 b an

d th e reportin g requiremen ti n para- grap h (j ) o

f thi s section , th e followin g informatio n shal l b e reporte d t o th e Administrator : (1 ) Calendar date s covere d i n th e re - portin g period . (2 ) Each 30-da

y averag e sulfu r diox - id e emissio n rate (ng/ J or lb/millio n Bt u hea tinput ) measure d durin g th e reportin g period , endin g wit h th e las t 30-da y perio d i n th e quarter ; reason s fo r noncomplianc e with th e emissio n standards ; and a descriptio n o f correc - tiv e action s taken . (3 ) Each 30-da

y averag e percen tre - ductio n i n sulfu r dioxid e emission s cal - culate d durin g th e reportin g period , endin g wit h th e las t30-da y perio d i n th e quarter ; reason s fo r noncompli - anc e with th e emissio n standards ; an d a descriptio n o

f correctiv e action s taken . (4 ) Identificatio n o

f th e stea m gener - atin g uni toperatin g day s tha tcoa l or oi l wa s combuste d an d fo r whic h sulfu r dioxid e o r diluen t(oxyge n o r carbon dioxide ) data hav e no tbee n ob - taine d by a n approve d metho d fo r a t leas t7 5 percen to

f th e operatin g hour s i n th e stea m generatin g uni toperatin g day ; justificatio n fo r no tobtainin g sufficien tdata ; an d descriptio n o f cor- rectiv e actio n taken . (5 ) Identificatio n o

f th e time s whe n emission s data hav e bee n exclude d from th e calculatio n of

averag e emis - sio n rates ; justificatio n fo r excludin g data ; an d descriptio n of correctiv e actio n take n i

f data hav e bee n ex - clude d fo r period s othe r tha n thos e durin g whic h coal o r oi l were no tcom - buste d i n th e stea m generatin g unit . (6 ) Identificatio n o f

"F " facto r use d fo r calculations , metho d o f determina - tion , an d typ e of

fue l combusted . (7 ) Identificatio n o

f time s whe n hourl y average s hav e bee n obtaine d based o n manual samplin g methods . 4 0 CF R Ch . I (7-1-9 0 Edition ) (8 ) Identificatio n o

f th e time s whe n th e pollutan tconcentratio n exceede d ful l spa n o

f th e CEMS . (9 ) Descriptio n o

f any modification s t o th e CEM

S tha tcoul d affec tth e ability of th e CEMS t o comply with Performanc e Specificatio n 2 or 3 . (10 ) Result s o

f dail y CEM

S drif t test s and quarterl y accurac y assess - ment s a s require d unde r Appendix F , Procedure 1 . (11 ) Th e annual capacit y facto r o

f eac h fire d a s provide d unde r para- grap h (d ) o

f thi s section . (1 ) Fo r eac h affecte d facility subjec t t o th e complianc e an d performance testin g requirements o f 5 60.45b(d) an d th e reportin g requirements o f paragrap h (j ) o

f thi s section , th e fol - lowin g informatio n shal l b e reporte d t o th e Administrator : (1 ) Calenda r date s whe n th e facility was i n operatio n durin g th e reportin g period ; (2 ) Th e 24-hou r averag e sulfu r diox - id e emissio n rat e measure d fo r eac h stea m generatin g uni toperatin g da y durin g th e reportin g perio d tha tcoal o r oi l wa s combusted , endin g i n th e las t24-hou r perio d i n th e quarter , rea - son s fo r noncomplianc e wit h th e emis - sio n standards ; an d a descriptio n o f correctiv e action s taken ; (3 ) Identificatio n o

f th e stea m gener - atin g uni toperatin g day s tha tcoa l or oi l wa s combuste d fo r whic h sulfu r di - oxid e or diluen t(oxyge n o r carbo n di - oxide ) dat a hav e no tbee n obtaine d by an approve d metho d fo r a tleas t7 5 percen tof

th e operatin g hours ; justifi - catio n fo r no tobtainin g sufficien t data ; and descriptio n o f corrective actio n taken . (4 ) Identificatio n o

f th e time s whe n emission s dat a hav e bee n exclude d from th e calculatio n o

f average emis - sio n rates ; justificatio n fo r excludin g data ; an d descriptio n o f corrective actio n take n i

f dat a hav e bee n ex - clude d fo r period s othe r tha n thos e durin g whic h coa l o r oi l were no tcom- buste d i n th e stea m generatin g unit . (5 ) Identificatio n of

"F " facto r use

d fo r calculations , metho d o f determina - tion , an d typ e of

fue l combusted . (6 ) Identificatio n o

f time s whe

n hourl y average s hav e bee n obtained f base d o n manual samplin g methods. . - ' f 

### 29 4 

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e .} P.2 3

Environmenta l Protectio n Agenc y (7 ) Identificatio n of

th e time s whe n th e pollutan tconcentratio n exceede d ful l spa n o

f th e CEMS . (8 ) Descriptio n o

f any modification s to th e CEM

S whic h coul d affec tth e abilit y o f th e CEMS t o comply with Performance Specificatio n 2 or 3 . (9 ) Result s o

f dail y CEM

S drif ttest s an d quarterl y accuracy assessment s a s required unde r Appendix F , Procedur e 1 . (m ) Fo r eac h affecte d facility sub jectt o th e sulfu r dioxid e standard s under 5 60.42

b fo r whic h th e minimu

m amounto

f data require d under § 60.47b(f ) were no tobtaine d during a calendar quarter , th e followin g infor matio n i s reporte d t o th e Administra to r i n additio n t o tha trequired under paragrap h (k ) o

f thi s section : (1 ) Th e numbe r o

f hourl y average s availabl e fo r outle temissio n rate s and inle temissio n rates . (2 ) Th e standar d deviatio n o f hourl y averages fo r outle temissio n rate s an d inle temissio n rates , a s determine d i n Metho d 19 . Sectio n 7 . (3 ) Th e lowe r confidenc e limi tfo r th e mea n outle temissio n rat e an d th e upper confidenc e limi tfo r th e mean inle temissio n rate , a s calculate d i n Metho d 19 , Sectio n 7 . (4 ) Th e rati o o

f th e lowe r confidenc e limi tfo r th e mea n outle temissio n rate an d th e allowabl e emissio n rate , a s de termine d i n Metho d 19 , Sectio n 7 . (n ) I f a percen tremoval efficienc y b y fue l pretreatmen t(i.e. , % R, ) i s used t o determin e th e overal l percen t reductio n (i.e. , % R. ) unde r 5 60.45b , th e owne r o r operato r o f th e affecte d facilit y shal l submi ta signe d state men twit h th e quarterl y report : (1 ) Indicatin g wha tremova l efficien c y by fue l pretreatmen t(i.e. , % R, ) wa s credited fo r th e calenda r quarter ; (2 ) Listin g th e quantity , hea tcon tent , an d date eac h pretreate d fue l shipmen twa s receive d durin g th e pre vious calenda r quarter ; th e nam e and locatio n o f th e fue l pretreatmen tfacil ity ; an d th e tota l quantity an d tota l heatconten to

f al l fuel s receive d a t th e affecte d facility durin g th e previ ou s calenda r quarter ; (3 ) Documentin g th e transporto f th e fue l fro m th e fue l pretreatmen t facilit y t o th e stea m generatin g unit . § 60.49 b (4 ) Includin g a signe d statemen t fro m th e owne r or operato r o f th e fue l pretreatmen tfacilit

y certifyin g tha t th e percen tremova l efficiency achieve d b y fue l pretreatmen twa s de termine d i n accordance wit h th e provi sion s o f Metho d 19 (Appendix A) and listin g th e hea tconten tan d sulfu r conten to f eac h fue l befor

e an d afte r fue l pretreatment . (0 ) All record s required under this sectio n shal l b e maintaine d by th e owne r or operato r o

f th e affecte d fa cility fo r a perio d o

f 2 years followin g th e dat e of

suc h record . (p ) Th e owne r or operato r o f an affecte d facUit

y describe d i n 5

5 60.44b(j ) or (k ) shal l maintai n record s o f th e followin g informatio n for eac h stea m generatin g uni toperatin g day : (1 ) Calenda r date , (2 ) Th e numbe r o

f hour s o f oper ation , and (3 ) A record o

f th e hourl y stea m load . (q ) Th e owne r or operato r o f an affecte d facility describe d i n 5 60.44b(J) or S 60.44b(k) shal l submi tt o th e Ad ministrato r o n a quarterl y basis : (1 ) Th e annual capacit

y facto r ove r th e previou s 1

2 months , (2 ) Th e averag e fue l nitroge n con ten tdurin g th e quarter , l f residua l oi l was fired ; an d (3 ) I f th e affecte d facilit

y meet s th e criteri a describe d i n 5 60.44b(j) , th e re sult s o f an y nitroge n oxide s emissio n test s require d durin g th e quarter , th e hour s o f operatio n during th e quarter , and th e hour s o

f operatio n sinc e th e las tnitroge n oxide s emissio n test . (r ) Th e owne r o r operato r o f a n affecte d facility wh o elect s t o demon strat e tha tth e affecte d facility com bust s onl y ver

y low sulfu r oi l unde r 5 60.42b(j)(2 ) shal l obtai n an d main tai n a tth e affecte d facilit y fue l re ceipt s fro m th e fue l supplie r whic h certif y tha tth e oi l meets th e defini tio n of distillat e oi l a s define d i n 5 60.41b . Fo r th e purpose s o f this sec tion , th e oi l nee d no tmee tth e fue l ni troge n conten tspecificatio n i n th e definitio n o f distillat e oil . Quarterly re ports shal l b e submitte d t o th e Admin istrato r certifyin g tha tonl y ver y lo w sulfu r oi l meetin g this definitio n wa s combuste d i n th e affecte d facility during th e precedin g quarter . 

### 29 5P.2 4

§60.5 0 (Approve d b y th e Offic e o f Managemen t an d Budge tunde r contro l numbe r 2060 - 0135 ) [5 2 F R47842 , Dec . 16 , 1987 . a s amende d a t 5 4 F R51820 , 51825 . Dec . 18 , 1989 ] 4 0 CF RCh. I (7-1-9 0 Edition ) §60.53 . (a l 'Monitorin g > 'h e tons . ie r ope i sh a an e th e y in proyjSion s o f g ope i method s and/pVocedu i

/ conducting/th e performance equire a i n £60.8 , the

* owne r o

r to r snai l us e a s referenc e met rocedure s thVtes tmetttod s ndix j A o f this par tor•/Othe r procedure s a s sffecified ion , excep ta s ppdvide

d i n 8(b L L e owng r or opeprfto

r sh s complianc e wtf

h th e Latte r standaroyui 5 60.5

5 deticu fol tter . (gr / (b ) te i late / lows : (1 ) Til e emissio n rate (dz/b f particu lat e ^matter

, correcte d t o 1

2 percen t CO/shal l h e compute d fo r eac h run g th e followin g equation : :„ = c , (12/%CO>

) where. * d i concentratio n o

f particulat

e correcte d t o 1 2 percenrCOi

. i dscf) . . / c,=concentratio

n o f .particular ' matter

, g / dsc m (gr/dscf) . %COt=CO i concentration ^ percen tdr y basis. / (2 ) Metho d 5 shal l b e usecKt o deter min e th e particulat e matte r concen tratio n (c,) . Th e samplin g tim e an d sampl e volum e fo r eacbVru n sha H b e a t leas t6 0 minute s and 0.8

5 dsc m (3 0 dscf) . (3 ) Th e emissio n rate correction factor , integrate d o r gra b sampling an d analysis-procedur e o f Metho d 3

B shal l b e use d t o determine . CO * concentrati0 n (%CO»)

. (i ) Th e CO

» sampl e shal l b e obtained (taneousY y with , and a tth e sam

e travers e point s as , th e particulate run, j f th e particulat e ru n ha s mor e than 1 2 travers e points , th e CC* * traverse point s ma

y b e reduce d t o 1

2 i f Method 1 is/use d to*locate th e 1 2 CO»'travers e points . If individual CO

a sample s take n ar teac h concentration 1 rectio n eq i ti c mean/o f sampl e concentrations : point . 

### 29 6 

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