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ca <br /> �+ TABLE 302.4--LIST OF HAZARDOUS SUBSTANCES AND REPORTABLE QUANTITIES--CoHdirlued a <br /> I,f p4ow Ali CownwftNoM3 Are Located at the End of This Table! <br /> Stan" <br /> RO <br /> Hazardous substance CASRN Re2ulerory syranyms RO Coast waste Pclmds(Kg) <br /> Number <br /> i Process residues from annine ex"ction from the <br /> production of aniline. <br /> ........ .............. 1' 4 K104 A 10{Ab1} <br /> . ................... <br /> Combined wastewater streams generated from <br /> 1 L- Mlnpben2andaniline production, 10 4.541 <br /> .f ................................................................ 1' 4 K105 A <br /> * K105.......................................................................... ................... <br /> Separated aqueous stream iron the reactor product . <br /> washing stop in the production at ehWohenzenas. - <br /> i1' 4 K106 X l(0.454) <br /> wastewater treatment sludge from the mercury cen <br /> process In chlorine production. <br /> ....... .................. ....... <br /> ................ .............................. f0 4 K197 % 101454) <br /> ........... ............ <br /> Column bottoms Nom product separation from the <br /> production of 1,1-dlnwMylhydrazine (UDMH) <br /> trom carbosytic acid hydrazines. 10 4 K108 X 10(4.54) <br /> K108.........................................................,........,.,..... .................. ................................................................................... <br /> r Condensed column overheads lrom product sepa- <br /> ration and condensed reactor vent gases from <br /> the production of 1.14methyihydrazine(UDMH) _ <br /> frau cwboxjnic add hydrazides. <br /> 10 4 K109 % 10(4.54) . <br /> Spent filter cartridges from product purilkason <br /> .from the production of 1,1- dmethylhydraxlne -n <br /> TY <br /> (UDMH)from carbo*Ic"hyd 10 4 K110 X 16(4.64) w <br /> K119.......................................................................... .................. ................................................................................ <br /> Condensed column overheads horn intermediate <br /> separation Nom the production of 1.1- _ <br /> " ylhydrazlne(UDMH)from carboxylic add .-. <br /> K511 1• 4 Kttt A 10(4541 <br /> ._........................................................................ .................. ......................................... ........... <br /> �! Product washwaters from the production of dinnro- <br /> r' L toluene via nitration of toluene. t' 4 K112 A 10(4.54) <br /> W <br /> K712...... ............ .. <br /> ............................................... .................. .................................................................. ............... <br /> .. T <br /> s Reaction by-product water from the drying column In CL <br /> the production of loiuenediamine vie hydro- 9 <br /> genallon of dinhrotoluene. 1 4 K113 A 10(4.64) <br /> ' K113........................................................................... .............:.... ....»....................................,........................................ <br /> e �x <br /> r m <br /> ! Condensed liquid npht ends from 1116 puriflealion 01 <br /> i soluanedlamine in ft production of <br /> tduenediamine via hydrogenation of dtnitf u- <br /> fine. .................................................... 1' 4 K114 A 19(4.64) <br /> ...............................................I............ ............................... <br /> tAdnW3 from the purl6caUan of tahuenedamins in 3 <br /> k IM producWn of talwnadiamine via hydro- <br /> genation <br /> ydragenation of dnttrosotuene. 4 K115 A 10(4.54) <br /> ................_..................................... 1' <br /> Heavy finds Nom r*puntiCason Of tahrened'iamine <br /> in 1116 production of tolueriediaMne via hydro- <br /> ._............... <br /> priatfon of dnitio uerie' 4 K118 A 10(4.54) <br /> Organic wxiensate Tram the aohrerd recovery 001- <br /> . - u mn In the production d toluene dilswyanate ria m <br /> plgsgenetiort O1 tduenedlamirt6. ........................................ <br /> 1 0.454) <br /> Kt17....................._................................................... .................. ......................................... .. 1' 4 K117 X <br /> ! Waslawater ham the reaction vent go scnrQbw In '< <br /> the production of ethylene bromide vis br nrt- <br /> nation of ethene. 1(0.4641 <br /> vs K118 ........................................................................... .................. ................................................................................. ,• 4 K 118 <br /> F t Spent absorbent solids tram puri6C811011 of ethylene <br /> +� dbmmids in the production Of ethylene db mk%. <br /> .................. ............................................................................... <br /> .... 1' 4 K123 A 10(4.541 <br /> Process wastewater(including supemales.filtrates, . <br /> and wasrrwalenl from the production of <br /> ' Nhylenabiedlhiccarbamic 4 Kt24 A <br /> acM and ft salts. 10(4.54) <br /> ' ........................................................................... 1• <br /> Reactor vent Scrubber water from the production Of . <br /> ethylenebisdithiocarbamic add and its eels. .., 1• 4 K125 A 10(4.54) <br /> K126 .......................................................................... .................. ................................................................................ <br /> 1:Wreticn,eveporation,and centrifugation solids from- <br /> # the production of ethylenedsdithiocerbamK add <br /> and its sells. 4 Kt28 A 10(4.64) <br /> i t' <br /> BBVXK a dust and floor sweepings In milling and <br /> } padroping operations Nom the production or ta- <br /> #� mulation of athylanabisdllik"bamic add and As <br /> v sofa. 100 4 K131 % too(46.4) <br /> K131 ..................................«............................_................. <br /> wastewater from the reactor and spent sulfuric ] <br /> SM from pie acid dryer in the production 01 N <br /> me"br'omWe. 1000 4 K132 x 1000(454) A <br />