您好,欢迎访问三七文档
当前位置:首页 > 商业/管理/HR > 企业文化 > 电絮凝技术处理高盐废水的研究进展王思宁
35120182JOURNALOFNATURALSCIENCEOFHEILONGJIANGUNIVERSITYVol.35No.1February2018DOI10.13482/j.issn1001-7011.2017.10.122http//hdzrxb.cbpt.cnki.net2017-07-112012ZX07201003-0022016DX05LBH-Z160731993-E-mail278797605@qq.com1962-E-mailzhql1962@163.com.J.201835172-78.150090、。。。、。X703.1A1001-7011201801-0072-07ResearchandapplicationofelectrocoagulationforhighsalinitywastewatertreatmentWANGSiningDINGJingZHAOQingliangHUANGHuibinYUANYixingStateKeyLaboratoryofUrbanWaterResourceandEnvironmentSchoolofEnvironmentHarbinInstituteofTechnologyHarbin150090ChinaAbstractDuetoitsinhibitoryeffectonmicroorganismgrowthhighsalinitywastewaterwasdifficulttomeetthedisposalrequirementbyconventionalbiologicaltreatment.Electrocoagulationwithadvantagesofhighremovalefficiencysimpleoperationandsmallsizehasattractedgreatattentionofresearchers.Highsalinityinwastewatercouldreducetheelectricconsumptionwithapplicationofelectrocoagulation.Thiswastewatertreatmentcouldbecarriedoutwithalowcost.Thusresearchandapplicationofelectro-coagulationinhighsalinitywastewatertreatmentgraduallyincreased.Theprincipleandcharacteristicsofelectrocoagulationwereintroducedandtheapplicationswereelaboratedtocovermarineaquaculturewastewaterlandfillleachateanddyeingwastewater.Keywordshighsalinitywastewaterelectrocoagulationwastewatertreatment0。5%12%2。。。3.5%TDS。、、、3。、。。Lefebvre24。1、、Al、Fe。、。、、、5。。1Fig.1Schematicdiagramofelectrocoagulation1.1、。、、61。、、、、、、、、。6。Al-3e-→Al3+Al3++3OH-→AlOH3Al3++3H2O→AlOH3+3H+Fe-2e-→Fe2+Fe-3e-→Fe3+Fe2++2OH-→FeOH2Fe3++3OH-→FeOH34Fe2++10H2O+O2→4FeOH3+8H+2H2O+2e-→H2+2OH-1.2pH、、、。。·37·11.2.1pHpH。pH。pH7。Vasudevan80.2A·dm-2pHpH7.098.2%。pHpH。1.2.2。。Heidmann101.0~3.0A0.05~0.1A。8。1.2.311。Vasudevan8。Eyvaz12COD10min15minCOD50%80%COD。1.2.4。、13。5。。1.2.5。。Akbal14、、、100%。15-。、、16。1.3、、、、、。、17、。6。18。7。17。。2。。、·47·35。1。1Table1Examplesofthecharacteristicandelectrocoagulationtreatmentontypicalhigh-salinitywastewaterpH8.530g·L-10.3~0.6g·L-190%220.2%0.3~0.6g·L-195%21pH7.19~8.423.5%COD2.11~5.25mg·L-189.9%COD68.1%87.0%93.8%23pH8.175.57g·L-1COD10000mg·L-1、、70%、37%62%25pH6~83A·mm-2COD8000~10000mg·L-1COD65.4%26pH7.6~8.912.15~13.55ms·cm-1COD28200~34200mg·L-1COD、、70%、24%、56%60%68%、15%、28%16%27pH6.4~7.32319mg·L-1COD2566mg·L-1COD49.8%38.6%28pH8293g·L-1COD260O2mg·L-1COD56%5NTU80%40%29pH6~92.4ms·cm-1COD2500mg·L-1200mg·L-1COD85%~95%32pH7.424VCOD2937.6mg·L-199%COD70%332.119。、、、、、、、、20。1V21。Vandamme22、30min、150r·min-190%1~2。21-0.1%95%。23、COD、0.063~0.077kW·h·t-1。2.2、、·57·1。、、、。24。、。Mussa2510V、5.57g·L-1120min、、70%、37%62%230Wh·L-1。26、20mm、pH6~8、3A·mm-2COD65.4%。Bouhezila27OUEDSMAR125~500A·m-2、2.8cm、150r·minCOD、、70%、24%、56%60%68%、15%、28%16%。Al0.022kWh·L-10.54US$·m-3Fe0.019kWh·L-10.47US$·m-3。Li284.96mA·cm-2、pH、2319mg·L-1、90min、FeCOD49.8%38.6%。Ricordel292cm、、95A·m-2210minCOD56%5NTU80%40%COD135Wh·kg-1COD。、。2.3、、、、、、。、、、、、、30。。、31。Merzouk32pH6~9COD2500mg·L-1200mg·L-114min31.25mA·cm-22.4ms·cm-11cmCOD85%~95%3.82~5.73kWh·kg-1COD。3424V、35minCOD99%70%。Ashtoukhy3368%87%。33.1。35。36。、、。。14。3.2、。·67·35、37。38。39、。3.3。。Boroski40COD1753mg·L-1160mg·L-1TiO250mg·L-1。Zhu41。Yetilmezso42UASB、pH5.0、15mA·cm-2、20minUASB90%COD92%2.6kwh·g-1COD。、、、。、43。4。。、、。1CUIYPENGCPENGYetal.EffectsofsaltonmicrobialpopulationsandtreatmentperformanceinpurifyingsalinesewageusingtheMUCTprocessJ.Clean-SoilAirWater2009378649-656.2LEFEBVREOMOLETTAR.TreatmentoforganicpollutioninindustrialsalinewastewateraliteraturereviewJ.WaterResearch200640203671-3682.3.J.2014332493-497.4.D.2012.5.J.201638333-37.6.J.20153459-15.7KHANDEGARVSAROHAAK.Electrocoagulationforthetreatmentoftextileindustryeffluent-areviewJ.JournalofEnvironmentalManage-ment2013128949-963.8VASUDEVANSLAKSHMIJPACKIYAMM.ElectrocoagulationstudiesonremovalofcadmiumusingmagnesiumelectrodeJ.JournalofAppliedElectrochemistry201040112023-2032.9.J.20144415-420.10HEIDMANNICALMANOW.RemovalofCrVIfrommodelwastewatersbyelectrocoagulationwithFeelectrodesJ.SeparationandPurificationTechnology200861115-21.11NARAYANANNVGANESANM.UseofadsorptionusinggranularactivatedcarbonGACfortheenhancementofremovalofchromiumfromsyn-theticwastewaterbyelectrocoagulationJ.JournalofHazardousMaterials20091611575-580.12EYVAZM.TreatmentofbrewerywastewaterwithelectrocoagulationimprovingtheprocessperformancebyusingalternatingpulsecurrentJ.In-·77·1ternationalJournalofElectrochemicalScience20161164988-5008.13JIMENEZIZQUIERDOCCANIZARESPRODRIGOMAetal.EffectofthenatureofthesupportingelectrolyteonthetreatmentofsolubleoilsbyelectrocoagulationJ.Desalination20102551-315-20.14AKBALFCAMCIS.CopperchromiumandnickelremovalfrommetalplatingwastewaterbyelectrocoagulationJ.Desalination20112691-3214-222.15.-ⅥJ.20071051-54.16.D.2005.17MOLLAHMMORKVOSKYPGOMESJetal.FundamentalspresentandfutureperspectivesofelectrocoagulationJ.JournalofHazardousMaterials20041141-3199-210.18.J.2009138-40.19.SBRSBBRD.2014.20.J.20133106-108.21.-J.2010740-42.22VANDAMMEDPONTESSCVGOIRISKetal.Evaluationofelectro-coagulation-flocculationforharvestingmarineandfreshwatermicroalgaeJ.BiotechnologyandBioengineering2011108102320-2329.23.D.2010.24.-Fenton-BAFROD.2015.25MUSSAZHOTHMAN
本文标题:电絮凝技术处理高盐废水的研究进展王思宁
链接地址:https://www.777doc.com/doc-6556772 .html