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230 Subpart K—Indirect Discharge Point Sources

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230 Subpart K—Indirect Discharge Point Sources § 414.110 40 CFR Ch. I (7±1±00 Edition) [52 FR 42568, Nov. 5, 1987, as amended at 58 PSES and PSNS 1 FR 36893, July 9, 1993] Maximum Effluent characteristics Maximum for any for any monthly Subpart KÐIndirect Discharge one day average Point Sources Acenaphthene ................................... 47 19 Anthracene ........................................ 47 19 SOURCE: 58 FR 36893, July 9, 1993, unless Benzene ............................................ 134 57 otherwise noted. Bis(2-ethylhexyl) phthalate ................ 258 95 Carbon Tetrachloride ......................... 380 142 § 414.110 Applicability; description of Chlorobenzene .................................. 380 142 Chloroethane ..................................... 295 110 the subcategory of indirect dis- Chloroform ......................................... 325 111 charge point sources. Di-n-butyl phthalate ........................... 43 20 1,2-Dichlorobenzene .......................... 794 196 The provisions of this subpart are ap- 1,3-Dichlorobenzene .......................... 380 142 plicable to the process wastewater dis- 1,4-Dichlorobenzene .......................... 380 142 charges resulting from the manufac- 1,1-Dichloroethane ............................ 59 22 ture of the OCPSF products and prod- 1,2-Dichloroethane ............................ 574 180 1,1-Dichloroethylene .......................... 60 22 uct groups defined by § 414.11 from any 1,2-trans-Dichloroethylene ................. 66 25 indirect discharge point source. 1,2-Dichloropropane .......................... 794 196 1,3-Dichloropropylene ....................... 794 196 Diethyl phthalate ................................ 113 46 § 414.111 Toxic pollutant standards for Dimethyl phthalate ............................. 47 19 indirect discharge point sources. 4,6-Dinitro-o-cresol ............................ 277 78 (a) Any point source subject to this Ethylbenzene ..................................... 380 142 Fluoranthene ..................................... 54 22 subpart must achieve discharges not Fluorene ............................................ 47 19 exceeding the quantity (mass) deter- Hexachlorobenzene ........................... 794 196 mined by multiplying the process Hexachlorobutadiene ......................... 380 142 Hexachloroethane ............................. 794 196 wastewater flow subject to this subpart Methyl Chloride ................................. 295 110 times the concentration listed in the Methylene Chloride ........................... 170 36 following table. Naphthalene ...................................... 47 19 Nitrobenzene ..................................... 6,402 2,237 (b) In the case of lead, zinc, and total 2-Nitrophenol ..................................... 231 65 cyanide the discharge quantity (mass) 4-Nitrophenol ..................................... 576 162 shall be determined by multiplying the Phenanthrene .................................... 47 19 concentrations listed in the following Pyrene ............................................... 48 20 Tetrachloroethylene ........................... 164 52 table for these pollutants times the Toluene .............................................. 74 28 flow from metal-bearing waste streams Total Cyanide .................................... 1,200 420 for metals and times the flow from the Total Lead ......................................... 690 320 Total Zinc 2 ......................................... 2,610 1,050 cyanide-bearing waste streams for 1,2,4-Trichlorobenzene ...................... 794 196 total cyanide. The metal-bearing waste 1,1,1-Trichloroethane ........................ 59 22 streams and cyanide-bearing waste 1,1,2-Trichloroethane ........................ 127 32 Trichloroethylene ............................... 69 26 streams are defined as those waste Vinyl Chloride .................................... 172 97 streams listed in Appendix A of this 1 All units are micrograms per liter. part, plus any additional OCPSF proc- 2 Total Zinc for Rayon Fiber Manufacture that uses the vis- ess wastewater streams identified by cose process and Acrylic Fiber Manufacture that uses the zinc chloride/solvent process is 6,796 µg/l and 3,325 µg/l for max- the control authority on a case-by-case imum for any one day and maximum for monthly average, basis as metal or cyanide bearing based respectively. upon a determination that such streams contain significant amounts of APPENDIX A TO PART 414ÐNON- the pollutants identified above. Any COMPLEXED METAL-BEARING WASTE such streams designated as metal or STREAMS AND CYANIDE-BEARING cyanide bearing must be treated inde- WASTE STREAMS pendently of other metal or cyanide Chromium bearing waste streams unless the con- trol authority determines that the Methylhydroabietate/Esterification of combination of such streams, prior to hydroabietic acid (rosin) with methanol treatment, with the Appendix A waste Acrylic acid/Oxidation of propylene via acro- streams will result in substantial re- lein N-butyl alcohol/Hydrogenation of n- duction of these pollutants. This deter- Butyraldehyde, Oxo process mination must be based upon a review Cyclohexanone/From phenol via of relevant engineering, production, cyclohexanol by hydrogenation-dehydro- and sampling and analysis information. genation 230 VerDate 11<MAY>2000 03:52 Aug 01, 2000 Jkt 190156 PO 00000 Frm 00230 Fmt 8010 Sfmt 8002 Y:\SGML\190156T.XXX 190156T PsN: 190156T Environmental Protection Agency Pt. 414, App. A Fatty amines/Hydrogenation of fatty nitriles Fatty amines/Hydrogenation of fatty nitriles (batch) (batch) Helioptropin/Oxidation of isosafrole, chro- Geraniol/B-Myrcene + Hydrogen chloride, mium catalyst esterification of geranyl chloride, hydrol- Isobutanol/Hydrogenation of ysis of geranyl acetate isobutyraldehyde, Oxo process Furfuryl alcohol/Hydrogenation of furfural Cyclohexyl Mercaptan/Cyclohexanol + Hy- Geranial (Citral)/Oxidation of geraniol (cop- drogen sulfide per catalyst) Ethyl Mercaptan/Ethanol + Hydrogen sulfide Glyoxal/Oxidation of ethylene glycol Methanol/H.P. Synthesis from natural gas Isobutanol/Hydrogenation of via synthetic gas isobutyraldehyde, Oxo process Oxo Alcohols, C7±C11/Carbonation & hydro- Isopropanol/Catalytic hydrogenation of ace- genation of C6±C10 Olefins tone Polyoxypropylene diamine/Polypropylene 2-Mercaptobenzothiazoles, copper salt/2- glycol + Ammonia Mercaptobenzothiazole + copper salt n-Propyl alcohol/Hydrogenation of Methanol/High pressure synthesis from nat- propionaldehyde, Oxo process ural gas via synthetic gas SAN resin/Suspension polymerization Methanol/Low pressure synthesis from nat- Styrene/Dehydrogenation of ethylbenzene ural gas via synthetic gas Styrene/Dehydration of methyl benzyl alco- Methyl ethyl ketone/Dehydrogenation of sec- hol (coproduct of propylene oxide) Butanol 1-Tetralol, 1-Tetralone mix/Oxidation of Oxo alcohols, C7±C11/Carbonation & hydro- tetralin (1,2,3,4-Tetrahydronaphthalene) genation of C6±C10 olefins 3,3,3-Trifluoropropene/Catalyzed hydrogen Phenol/Liquid phase oxidation of benzoic fluoride exchange with chlorinated pro- acid pane Polyoxyalkylene amines/Polyoxyalkylene Vinyl toluene/Dehydrogenation (thermal) of glycol + ammonia ethyltoluene Polyphenylene oxide/Solution polymeriza- tion of 2,6-xylenol by oxidative coupling Copper (cuprous salt catalyst) Methylhydroabietate/Esterification of Polyoxypropylene diamine/Polypropylene hydroabietic acid (rosin) with methanol glycol + Ammonia Acetaldehyde/Oxidation of ethylene with cu- Quinaldine (dye intermediate)/Skraup reac- pric chloride catalyst tion of aniline + crotonaldehyde Acetic acid/Catalytic oxidation of butane Silicones, silicone fluids/Hydrolysis and con- Acetone/Dehydrogenation of isopropanol densation of chlorosilanes Acrylamide/Catalytic hydration of acrylo- Silicones, silicone rubbers/Hydrolysis and nitrile condensation of chlorosilanes Acrylic acid/Oxidation of propylene via acro- Silicones, silicone specialties (grease, disper- lein sion agents, defoamers & other products) Acrylonitrile/Propylene ammoxidation Silicones: Silicone resins/Hydrolysis & con- Adipic acid/Oxidation of cyclohexanol- densation of methyl, phenyl & vinyl cyclohexanone mixture chlorosilanes Adipic acid/Oxidation of cyclohexane via Silicones: Silicone fluids/Hydrolysis of cyclohexanol-cyclohexanone mixture chlorosilanes to acyclic & cyclic Allynitrile/Allychloride + sodium cyanide organosiloxanes Aniline/Hydrogenation of nitrobenzene Styrene/Dehydration of a-Methylbenzyl alco- Benzofurans, 2,3-Dihydro-2,2-dimethyl-7- hol (coproduct of propylene oxide) benzofuranol/ from o-Nitrophenol + Meth- Tetrachloroethylene (perchloroethylene)/ allyl chloride Oxyhydrochlorination of tetrachloroethane n-Butyl alcohol/Hydrogenation of n- Tris(anilino)s-triazine/Cyanuric chloride + Butyraldehyde, Oxo process aniline + cogeners 1,4-Butanediol/Hydrogenation of 1,4- Trichloroethylene/Oxyhydrochlorination of butynediol tetrachloroethane Butryolactone/Dehydrogenation of 1,4- Unsaturated polyester resin/Reaction of ma- butanediol leic anhydride + phthalic anhydride + pro- Caprolactam/From cyclohexane via pylene glycol polyester with styrene or cyclohexanone and its oxime methyl methacrylate Lilian (hydroxydihydrocitronellal)/Hydra- Lead tion and oxidation of citronellol 1,2-Dichloroethane/Oxyhydrochlorination of Alkyd resin/Condensation polymerization ethylene Alkyd resins/Condensation polymerization of Dialkyldithiocarbamates, metal salts/ phthalic anhydride + glycerin + vegetable Dialkylamines + carbon disulfide oil esters 2-Ethylhexanol/from
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