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当前位置:首页 > 商业/管理/HR > 质量控制/管理 > UASBMBRNFRO工艺处理电厂垃圾渗滤液的效果分析邵良成
UASB+MBR+NF+RO1,2,2,1(1.,310000;2.,311201):“+UASB+MBR+NF+RO”,250m3/d,,(UASB、MBR)。:UASBCOD、BOD5、NH3-N、TP83.29%、73.76%、-0.29%、21.04%64.84%;MBRCOD、BOD5、NH3-N、TP87.48%、99.58%、97.22%、90.94%34.65%;COD、BOD5、NH3-N、TP96.56%、63.15%、90.65%、94.81%98.18%;“+UASB+MBR+NF+RO”COD、BOD5、NH3-N、TP99.93%、99.96%、99.74%、99.65%99.80%,《》A。:UASB+MBR+NF+RO;UASB;MBR;;;:X703:A:1006-8759(2018)04-0019-08EFFECTANALYSISOFTREATMENTOFLANDFILLLEACHATEFROMAMSWINCINERATIONPLANTUSINGCOMBINEDUSAB+MBR+NF+ROPROCESSSHAOLiang-cheng1,YEJian-na2,JINHai-feng2,WANGWen-lun1(1.ZhejiangQianyaoEnvironmentalEngineeringCompanyLimited,Hangzhou31000,China;2.HangzhouEnvironmentalProtectionResearchInstituteofChinaCoalTechnology&EngineeringGroup,Hangzhou311201,China)Abstract:Acombinedprocessofpretreatment+UASB+MBR+NF+ROwasappliedtotreatthelandfillleachatefromaMSWIncinerationPlantinZhejiangProvince.Thedesignedscalewas250m3/d.Theremovalefficienciesofmainpollutantsbythiscombinedprocessandeachtreatmentunitwereanalyzedbasedonone-yearmonitoringdataofthisplant.TheresultsshowedthattheUASBprocessremoved83.29%ofCOD,73.76%ofBOD5,-0.29%ofNH3-N,21.04%ofTPand64.84%ofchromaticity,respectively.TheMBRprocessremoved87.48%ofCOD,99.58%ofBOD5,97.22%ofNH3-N,90.94%ofTPand34.65%ofchromaticity,respectively.TheMembranesystemprocessremoved96.56%ofCOD,63.15%ofBOD5,90.65%ofNH3-N,94.81%ofTPand98.18%ofchromaticity,respectively.Thecombinedprocessofpretreatment+UASB+MBR+NF+ROremoved99.93%ofCOD,99.96%ofBOD5,99.74%ofNH3-N,99.65%ofTPand99.80%ofchromaticity,respectively.TheeffluentqualitysatisfiedtheStandardI-AofDischargeStandardofPollutantsforMunicipalWastewaterTreatmentPlant.Keywords:UASB+MBR+NF+RO;UASB;MBR;Membranesystem;Removalrate;Chromaticity.:2018-01-02:(1983-),,,,。EnergyEnvironmentalProtection32420188Vol.32.No.4Aug.,2018、,:、、、、[1,2]。,。,、。UASB、MBR、,,UASB、MBR、。,[3](up-flowanaerobicsludgebed,UASB),[4]、[5]、[6][7]COD(BOD5)。UASB,UASB,,[8]。[9],UASB40kg·COD/(m3·d),CODCrBOD5。MBR,MBR,[10]MBR3~5g/L15~30g/L,、CODCrBOD5,100%,。[11],MBR、、,、MBR。,[12],、、、,[13],。[14],,。,。、、COD、,GB16889-2008,。,[15]MBR+DTRO。[16]+(MBR)+(NF)+(RO)。,“+UASB+MBR+NF+RO”,。11.1,,250m3/d。“+UASB+MBR+NF+RO”,1,、、UASB、MBRNFRO《》,(GB18918-2002)《》(GB16889-2008)。1.2pH6~9,UASB32~35℃,A/O-MBR25~28℃,。,。,1。1USAB-MBR-NF-ROUASBA/OV/m3268821222250HRT/h240192216NFRO/L/h·m263.811814/m2163.2685.2877.1/%8580/Mpa1.0~2.00.5~2.53~51UASB+MBR+NF+RO·20·1.3。,2.1.4BOD5、CODCr、、。BOD5、CODCr、,。,:、UASB、A/OUFMBR、NFRO。,,,COD、BOD5、NH3-NTP(0.00%),。。22.1CODCOD2,COD3。,UASB、MBRCOD80%,,。COD,COD。,COD。COD21740mg/L-48820mg/L,pH6~9,UASB、MBRCOD83.29%、87.48%96.56%,,COD99.93%,COD23.61mg/L。CODGB18918-2002A(≤50mg/L)。2.2BOD5BOD53,BOD54。,UASBBOD580%,,UASB,BOD5;,MBR99%,,BOD5。,BOD5。BOD510122mg/L-17970mg/L,pH6~9,UASB、MBRBOD573.76%、99.58%63.15%,,BOD599.96%,BOD55.12mg/L。BOD5GB18918-2002A(≤10mg/L)。2CODcr(mg/L)BOD5\mg/LNH3-N\mg/LTP\mg/LSS\mg/L\20000-6000010000-300001000-300050-1508000-1200005000-70002COD3CODUASBMBR(mg/L)21740~488203657~8068600.5~787.4(mg/L)34127.465584.34688.5877.77%~91.79%79.73%~91.98%95.36%~98.41%83.29%87.48%96.56%(mg/L)3657~8068600.5~787.412.1~29.8(mg/L)5584.34688.5823.613BOD5·21·3242.3NH3-NNH3-N4,NH3-N5。,UASBNH3-N(-13.41%)(9.53%),NH3-N,NH3-NUASB(-0.29%)。MBRNH3-N87%,NH3-NMBR,。,NH3-N。NH3-N1045.4mg/L-1978.5mg/L,pH6~9,UASB、MBRNH3-N-0.29%、97.22%90.65%,,NH3-N99.74%,NH3-N4.03mg/L。NH3-NGB18918-2002B(≤8mg/L)。2.4TPTP5,TP6。,UASBTP,MBRTP80%,UASBMBR,TP。,,TP。,TP。TP70.0mg/L~99.8mg/L,pH6~9,UASB、MBRTP21.04%、90.94%94.81%,,TP99.64%,TP0.30mg/L。TPGB18918-2002B(≤1mg/L)。4BOD5UASBMBR(mg/L)10122~179703016~399310.9~18.9(mg/L)13808.83580.6714.8862.79%~79.79%99.48%~99.70%47.8%~77.61%73.76%99.58%63.15%(mg/L)3016~399310.9~18.93.8~6.4(mg/L)3580.6714.885.124NH3-NUASBMBR(mg/L)1045.4-1978.51037.4-1996.023.9-68.8(mg/L)1587.871591.1243.4-13.41%-9.53%95.69%-98.45%87.49%-95.31%-0.29%97.22%90.65%(mg/L)1037.4-1996.023.9-68.82.1-5.9(mg/L)1591.1243.44.035NH3-N5TPUASB+MBR+NF+RO·22·2.56,TP7。,;UASB,,70%;,MBR,30%98%,MBR,。,,。,。6500~7500,pH6~9,、UASB、MBR52.53%、64.84%、34.65%98.18%,,99.80%,14.15。GB18918-2002A(30/50)。2.6COD、BOD5、NH3-N、TP24h,COD、BOD5、NH3-N、TP7,8。,MBR、、、UASB。MBR2803761kW·h,UASB22.5;7.24;3.89。MBR;UASB;、;。,。,78,3775994kW·h,,。,,。6TPUASBMBR(mg/L)70.0-99.860.1-71.83.7-8.5(mg/L)84.0966.005.954.02%-35.63%86.96%-94.56%82.50%-98.40%21.04%90.94%94.81%(mg/L)60.1-71.83.7-8.50.1-1.0(mg/L)66.005.950.3067UASBMBR3192-3513.81043.1-1276.7666.5-861.83365.511182.64772.5461.77%-69.08%31.80%-38.10%97.60%-98.60%64.84%34.65%98.18%1043.1-1276.7666.5-861.89.99-19.341182.64772.5414.15(mg/L)(mg/L)(mg/L)(mg/L)6500-75007100.0050.12%-55.17%52.53%3192-3513.83365.517COD、BOD5、NH3-N、TP(kW·h)·23·3242.7“+UASB+MBR+NF+RO”2-6,“+UASB+MBR+NF+RO”COD、BOD5、NH3-N、TP98%,。7,“+UASB+MBR+NF+RO”COD、BOD5、NH3-N、TP99%,100%。pH6~9,COD、BOD5、NH3-N、TP9,COD、BOD5、TPGB18918-2002A,NH3-NGB18918-2002B,GB18918-2002A。。COD(%)BOD(%)NH3-N(%)TP(%)(%)(kw/h)0.000.000.000.0052.53387472.3UASB83.2973.76-0.2921.0464.84124882.6MBR87.4899.5897.2290.9434.65280376196.5663.1590.6594.8198.18720786.899.9399.9699.7499.6499.8037759948COD、BOD5、NH3-NTP9《》3“+UASB+MBR+NF+RO”,,,“+UASB+MBR+NF+RO”,,。,COD、BOD
本文标题:UASBMBRNFRO工艺处理电厂垃圾渗滤液的效果分析邵良成
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