Document a4LYvLB9EpKg23e5arVkXNJoY

tea leaves as fuel to exceed 0.70 pounds of sulfur dioxide per nubtu of actual heat Input. . (Source: Added at 7 til. 809. 4219. effective March 20. 1983) SU8PART 0: PETROIEUM REFINING. PETROCHEMICAL AND CHEMICAL MANUFACTURING Section 214.380 Scope a) This Subpar.t contains rules idiich.modify the general sulfur emission rules of Subparts A through N as applied too given industry or at. a given s.lte. General rules include: . 1).' Subparts B through I:- Fuel, combustion emission sources and Incinerators; 2) Subparts K through H: process emission sources. . b) These rules have been grouped for the convenience of the public; the scope of each ts determined by its language and history. Rules placed In this Subpart Include those which appear to be primarily directed at the following major Industry groups: 1) Chemicals and allied, products: 2) Petroleum refining and related industries; 3) Rubber and miscellaneous plastics products. ^(Source: Added and codified at 7 111..Reg. 13597) Section 214.381 Sulfuric Acid Manufacturing a).No person, sha 1.1 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/Hg). . b) No person shall , cause or allow the emission of sulfuric-acid mist into the"atmosphere from any process emission source to exceed 0.15 pounds of acid mist per ton of acid . manufactured (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 7 111..Reg. 4219. effective March 28. 1983) 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. b) No person shall cause, or .'allow the emission I' of more' thah 1.000 ppm.of sulfur dioxide into the atmosphere from any process emission source in the St.,.Louis (Illinois) major ' metropolitan area designed to remove sulfur compounds from the Hue gases pf petroleum and petrochemical processes. . * .* | c) The following Flmitatldns apply to any petroleum refinery;In the Village of Roxanar - 1) No. person shall cause or allow the combustion of refinery flasher pitch contalning more than 3vOX,,(threepercent) sulfur bywclght. ; This shall be demonstrated by dally: sampling of ref inery flasher, pitch. 2) No person' shall burn petroleum refinery \ fuel gas In any fuel gas combustion device If that .refinery fuel gas contains . ` more than. 39. grains h/drogen slf *de- 3e 100 dry standard cubic feet (893 mg/scm). This shall be-demonstrated by sampling the refinery fuel gas once every .1 . . . eight hours; pursuant to the Tutwller 1 Procedure (Section 214.104(c)). j 3) No person shall, cause..or allow the total emission of sulfur dioxide Into the atmosphere from the.,fallowing source groupings to. exceed the following amounts: A) All process heaters at dtstllllng .. unit No. 1 - 459 lbs/hr (208 kg/hr). I B) All process heaters'at. disttiling unit No. 2-12*0 Ibs/hr (571 kg/hr). C) All gas plant process heaters 159 lbs/br (72.1-kg/toc) -- 0) All .vacuum flasher unit heaters - 378 Ibs/hr (171 kg/hr). I * E) All process heaters at the alkylatioa. benzene, extraction unit and catalytic feed hydrotreating , units - 346 Ibs/hr .(157. kg/hr). f) All boiler? generattngstea* for* r general pil,ant .use-. 2.400 Ibs/hr ' (1,090 kg/hr). G) All heaters serving the hydrocracker .unit catalytic reformer No.1 1. and the saturates gas. plant - 1.660 Ibs/hr (753 kg/hr). '. I * . * H) All process.heaters at.the: aromatics east process`..r 768 Ibs/hr (348 kg/hr). 1) All catalytic cracking wilts - 3.430 lbs/hr (1.560 kg/hr). I J) All asphalt converters, distilling unit No. 1. the aromatics east j process, all boilers generating steam for general plant use. and all gas plant process heaters - 2.710 Ibs/hr (1.230 kg/hr); - 80