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(,332005)(,113001),(H2S)IVP,(VOC)()BPL,1111[1],,[224],,,,(GB14554293),GB14554293(),,,,()[5],Weber2FechnerI=KlogC+a(1)I,;K,,K;C;a,,a(1),90%,,,,112[6][7,8],:()(),;,CODCr,APO,APO,,,H2S,,,,113[9],,,,,73200642422,1[10]1,,,,,,51010-5,,,[11],,,,4,,,,,[12],,,3311(JICA),1996,[14,15],[14],IVPCentaurXtr.sorbHP,IVP[12]IVP(VOC)XtrusorbBPL,312,,112SUS(AB)2FRP(AB)BPL,,A(),BIVP,AB,AB,4IVP,BPL313BPL,;IVP,BPLIVP,H2SH2S,IVP;,BPLSUS12m3Ph,FRP12m3Ph,-35601500h-1H2S(IVP);,8320064242314,H2S(GB14554293)315,(H2S),()83:GC316,,(1)IVP,,,116177gPL,108193gPL95118%;9819%23,,,23(2)BPL,IVP,,,BPLIVP,,44(3)IVPCentaurP2,,,(4)H2S,;,P(5)IVP,IVP,(6),4,:(1),(),(),(2)(3),,[1]GB14554293.[2]....[3]....[4]....[5]..,1999,21(2):272281[6]..,1995,4:3123719320064242[7],..,2000,30(4):562601[8],..,2001,24(3):252271[9]..,1995,3:222271[10].().1995,31(2):81[11]..:,1989,51[12]..,1999,81[13],..,1999,9(2).[14]..,2002,32(4):52255.3320050792288728352005-08-173(,400044),,,,,,3(0521GX2QT194)0,[1],3:[2]:,,;,,,,,,,,,;,,,,,,,,,,11,,,,2,,20LPh,5mm,():20LPh014MPa,0420064242AbstractThesilk2makingwastewaterwastreatedbyair2floatationandSBRprocess.Theeffluentqualityconformedtothefirst2ordercriterionofGB897821996.Combiningtheengineeringpractice,itwasgivensomeexperienceindesignandoperationoftheengineering.Theprocessfeaturedlowcost,simpleoperationandeasymaintenance,whichmayprovideexperienceinsewagetreatmentofsimilarsilk2makingplants.Keywordsair2floatation2SBRtreatmentandsilk2makingwastewaterTHETREATMENTOFFOOD2MAKINGWASTEWATERUSINGUASBPROCESSZhangQunchouTongPanruiGaoYusong(25)AbstractThewastewaterfromfood2makingstarchproductionisahighly2concentratedorganicwastewater.ItistreatedbyabiochemicaltreatmenttechnologyusingUASBreactorundernormaltemperatureasthemaintreatmentunit,andtricklebedasthesecondaryunit.Thesetechnicsshowthattheuseofthesaidtechnologynotonlysavesinvestment,lowersoperationalcostandsimplifiesoperationbutalsoproducesusablemethanewhilethewastewateraftertreatmentcanmeetthestandardbeforedischargedsothatgoodeconomicandenvironmentalresultscanbeobtained.Keywordsfood2makingwastewater,wastewaterofstarchproductionandUASBTREATMENTOFEXPANSIBLEPOLYSTYRENEWASTEWATERBYPROCESSOFFLOCCULATIVESEDIMENTATION2ACTIVECARBONBIOLOGICALTANKLiuXiaodongNiNingLiJianshengetal(27)AbstractExpansiblepolystyrene(EPS)wastewaterinvolveslargequantitiesoforganismcontainingbenzeneloopsuchassurfactantLASandsoonwithhightotalPindexandbadbiodegradability.Itishardtotreatit.Theprocessofflocculativesedimentation2activecarbonbiologicaltankisadaptedtotreatEPSwastewater.WhenaverageCODCroforiginalwastewateris1800mgPL,thatoftheeffluentcanreachabout80mgPLwiththeremovalrateof9515%.Theeffluentqualityremainsstableandseveralqualityindexesoftheeffluentcanmeetthefirstclasscriteriaspecifiedinthenationaldischargestandard.KeywordsEPSwastewater,activecarbonbiologicaltank,delayedaerationmethodandsurfactantTREATMENTOFCHEMICALWASTEWATERBYHYDROLYTICACIDIFICATION2APOPROCESSLiuBozhiLiuFaqiangDingXuehong(29)AbstractHydrolyticacidification2APOprocessisselectedtotreatchemicalwastewaterofhighconcentrationduetothefactthatthetraditionalactivatedsludgeprocesshasalowremovalrateofNH32NandtheeffluentCODCrcannotbeuptostandardsteadily.ThetestresultsshowthatthenewprocesshasexcellentdenitrifyingeffectwithCODCrandNH32Nmeetingthefirst2orderofthenationalemissionstandard.Keywordschemicalsewage,hydrolyticacidification,APOprocessandbiodenitrogenationTHEDESIGNFORFLUEGASATOMIZINGHUMIDIFICATIONOFSEMI2DRYFLUEGASDESULFURIZATIONShiYingjieWangFanWangHongmeietal(31)AbstractHumidificationplaysakeyroleinSO2removalforsemi2dryfluegasdesulfurization(FGD).Inthearticle.theanalysisisderivedthatperformanceofairatomizingismoreeffectivethanthatofmechanicalatomizing.ThecalculationresultsshowthatdropsizedistributionofFM10airatomizingnozzlecanmeetfluegasconditioninevaporation.Itisdeducedthatatomizingcontrailangleisconstrainedinthefluegasandlayingoutofthenozzleintheductuniformlytoavoiddropfromwettingwall.Fabricfilterissupposedtobeniceinheatpreservationandeasyinashcleaning.Asmooth2surfacedfiltermaterialisselected.Keywordssemi2dryprocess,FGD,airatomizingnozzleandhumidificationTREATINGVOCs2BEARINGEXHAUSTGASBYACTIVATEDCARBONFROMSOLIDWASTESXieLipingLinWeigangYangXuemin(34)AbstractThemaininfluencefactorsontheadsorptiontoVOCsinexhaustgaswithactivatedcarbonfromsolidwastes(SW2AC)areinvestigated.TheresultsindicatedthattheSW2ACcancertainlybeusedforthepurificationprocessofVOCs2bearingexhaustgas.KeywordsVOCs,adsorption,activatedcarbonandtreatmentofexhaustgasTREATMENTOFODORPOLLUTIONFROMAERATIONTANKFORREFINERYBYFIXEDBEDACTIVATEDCARBONADSORPTIONLuQingfangGuoBingbing(37)AbstractOdortreatmentinaerationtankbymeansoffixedbedactivatedcarbonadsorptionhasbeenstudied.ThesubjectunderstudyisaimedatthesewagetreatmentplantinJiujiangPetrochemicalComplexRefineryofSINOPEC.TheactivatedcarbonIVPfordesulphurization(hydrogensulfideandmethanthiol)andtheactivatedcarbonBPLforadsorptingVOC(benzene,methylbenzeneanddimethylbenzene)hasbeenchosenintheresearchatthepilotplant.Thetechnologyrouteremovingtheoffensiveodorfrompo