Document LKakY7pkbpez8Xx3zNKdp1VqX

tea leaves as fuel to exceed 0.70 pounds of sulfur dioxide per mmbtu of actual beat Input. . (Source: Added at 7 111. te. *219. effective March 28. 1981) SUBPART 0: PETROLEUM RCFiRIRS. PETROCHEMICAL AMO CHEMICAL MAJOffACTURIM6 ' b) No person shall cause.'or.'allow the emission s of more than. 1.000 ppm.of 'sulfpr dioxide into the atmosphere from any process emission source In the st.ALouis (Illinois) major metropolitan area designed to remove sulfur compounds from the flue gases of petroleum ' and petrochemical processes. . | c) The following tlmttatlens apply to any petroleum reflhery ; In the village of Roxanar Section 214.380 Scope a) This Subpart contains rules,tditeh-modlfy the general sulfur emission rules of Subparts A ' through N as applied to'a given Industry or at a given s.lte. General rules Include: ' 1) `' Mo. person shall )cause, or allow the contest Ion of refinery flasher pitch cpntaln.tng'morr than SvOXJthreepercent) sulfur by.weight./This shall be demonstrated by dally sampling of refinery'flasher, pitch. 1).* Subparts B through -X: Fuel contest Ion emission sources and Incinerators: 2) Subparts K through M: Process emission sources. b) These rules have been grouped for the convenience of the public; the scope of each is determined by (ts language and history, tales placed In this Subpart Include those which appear, to be primarily directed at the - following major Industry groups: .1) Chemicals-and allied, products: | .x 1 . , 2) Mo person'shall burn'petroleum refinery fuel gas In any fuel gas contestIon device If that refinery fuel gas contains, more' than.-39' groans h/drogcn solMdo-po*100 dry standard cubic leet (893 ng/scm): this shall be.demonstrated by . sampling the refinery fuel gas once every . ..-eight hours', pursuant to the 'TutwIler Procedure (Section ll*.104(c)). . : ' *- 3) Mo person shall, cause..or-allow the total emission of sulfur dioxide Into the atmosphere from. the..faI4<Mlng. source ...... groupings tip exceed the fallowing amounts: 2) Petroleum refining and related Industries; 3) Rubber and miscellaneous plastics protacts. ./.('Source: Added and codified at 7.111..Reg. . 13597) , ... A) All' process- heate*at^d.lst1111ng unit Mo. I - 459 lbs/hr (200 bg/hr). B) ATT process.heaterr at.d.1st111tng unit Mo. 2 - 1260 Ibs/br ($71 kg/hr). . i. C) All gas plant process beaters 1S9 1ksAAtn.1.kgAcU . Section 214.301 Sulfuric Acid Manufacturing a).No person.shall cause or allow the emission of sulfur dioxide Into the atmosphere from any new sulfuric acid'manufacturing plant to exceed 4.0 pounds of sulfur dioxide per ton of acid produced (2.0 kg/Mg). 0) ' All .vacuum flasher unit heaters - 378 lbs/hr (171 kg/hr). E) All process heaters at the alkylaUoru.benzen*..extraction unit and catalytic feed hydrotreating units - 346 lbs/hr (157. kg/hr). . b) No person shall.cause or allow the emission of sulfuric.acid mist Into thelatmosphere from any process emission source to exceed 0.)S pounds of acid mist per ton of acid . .. manufactured i 75 g/Mg)v ' c)No person shall cause or allow the emission of sulfur dioxide Into the atmosphere from any sulfuric acid manufacturing process In the City of Chicago to exceed 500 ppm. (Source: Amended at 7. III..Reg. 4219. effective March 28. 1983) f) All boilers generatln'g'steaw'forgeneral pl.int .use -. 2.400'lbs/br (l.w6kg/hr).. . 6) All heaters 'serving the hydrocracker dntt catalytic reformer No. 1, and - the saturates gas; plant - 1.660 lbs/hr (7S3. kg/hr). ' H) ATI process-heaters aitiu&: ar.omatics east proceSs',.-T 768 lbs/hr (148 kg/hr). 1) All catalytic cracking units - 1.430 lbs/hr (1.S60 kg/hr). Section 214.382 .. Petroleum and Petrochemical Processes ' a) Section 214.301 shall not apply to existing processes designed to remove sulfur compounds from the -flue gases of petroleum and petrochemical processes. J) All asphalt converters, distilling unit No. 1. the aromatics east process, all boilers generating steam for general., plant, use., and all gas plant process heaters - 2.710 lbs/hr (1.230 kg/hr). . ao