高盐废水处理工艺最新研究进展李俊虎

31420188EnvironmentalScienceandTechnologyVol．31No．4Aug．2018：2018-04-13：（1988-），，，，，.，，，（，201507）：，。、、、、、、3.5%，。，。：；；；；:X5:A:1674-4829（2018）04-0074-05TheLatestProgressofTreatmentTechnologyforHighSalinityWastewaterLIJun-hu,ZHOUMin,WANGQiao,CHENChun-yue(ShanghaiChemicalIndustryParkSinoFrenchWaterDevelopment,Shanghai201507,China)Abstract:Thesource，compositionandcharacteristicsofhighsalinitywastewaterwhichcontainsTDSmorethan3.5%arebrieflyintroducedinthispaper.Thelatesttreatmentprogressofvarioushighsalinitywastewatersuchasbiologicaltreatment,adsorption,extraction,incineration,electrochemicaloxidation,Fentonoxidation,wetcatalyticoxidationisreviewed.Thefuturedevelopmentdirectionofthehighsalinitywastewatertreatmentprocesshasbeenpointedout.Keywords:Salinitywastewater;Halophilicbacteria;Advancedoxidation;Adsorption;Extraction0，，。，（NaCl）1％[1-2]；3.5%（）[3-4]。2：①、、、、，，，、、、，[5-6]；②，，，，，，，[7]。，，，[8]。，。，33.5%。1，，，，[9]，。，3.5%，1%，314，，，，，[10]。，[11]。TAN[12]，3。，3.7%5.7%，220mg/L1100mg/L。，90%。，。[13]33∶2∶1，48hCODCr81.85%，。FERRER-POLONIO[14]SBRNaCl80g/L，SBR，P.persalinus，20.9±3.1℃，22.5±7.5d，MLVSS3292±532mg/L，CODCr425.6±66.2mg/L，12.2±1.6mg/L，CODCr79.9%±2.9%。2，，，，，，，。、，，[15]。2.1，，，，，，[16]。[17]3.6%，P507/，pH8~9，1∶10，60min，95%，CODCr76%，。GUO[18]。12h，87.9%，，68.1%，。2.2，，。、，，[19]。[20]HYA-10618.9～38.9g/LTNT。pH3.0，1.0BV/h，0.5%NaOH+（V/V=4∶1），2.0BV/h，CODCr272.5mg/g，，。CHEN[21]NAD-150NaCl146.1g/LNa2CO31.5mol/L，NAD-150400mg/g。，。，，，，，，，。2.3，，7520188，，，，，[22]。JORFI[23]，4%，pH5，0.5A，（，××12×3×0.3cm）2cm，CODCr94%，TDS，CODCr。，，，，。[24]（NaCl15%），Ti/SnO2，Ti/β-PbO2，Ti/RuO2，Ti/RuO2，，。，，，。71mA/cm2，7h，98%，134mA/cm2，4h，98%，，。2.4，Fe2+H2O2。2.80V，，，[25]。，。SHI[26]NaCl20%，pH3，Fe2+25mmol/L，H2O2500mmol/L，m（Fe2+）∶m（H2O2）=1∶20，120min，TOC62.50%，Fenton，TOC89.27%，。PENG[27]，0.1mol/L，，。（NaCl292.2g/L），40%。（HA）（BQ），60%，。2.5，[28]。[29]NaCl18.5%，200℃，5g/L，2h，TOC94.7%。。[30]166g/L，280℃、60min、Fe2+100mg/LTOC97.9%。t470.2。，，，，。，。2.6，，，[31]。[32]6%31，0.7MPa、1.2V，15A，pH6，/Sb-N-TiO2/Sb-SnO2/A/Al2O399%，，，，。[33]，，，CODCr，CODCr。NaCl5%，，0.05mol/L，CODCr95%。5%76314，，0.05mol/L，CODCr90%。，，，。，，。。2.7800～1000℃，，，。，，，ρ(CODCr)≥100000mg/L，≥2500×4.1868kJ/kg10%[34]。[35]20%，，600℃，1100℃，4s，550kg/h，6900Pa，1.23%，。，，，，，。，，，。、1。1、（），，，。，，，，，。，，，，。，，，，。，，，，。，，，。，，，。，，，，。，，，，。，，。，。，，。，SS，。，，，，，，。，，，，。，，，，。3。，，，。，，，。，。，，，，，，。[][1],,.[J].,2002,22(11):1-4.[2],,,.SBBR[J].,2010,29(4):281-284.[3]WOOLARDCR,IRVINERL.Treatmentofhypersalinewast-ewaterinthesequencingbatchreactor[J].Waterresearch,1995,29(4):1159-1168.[4]LPEZDE,TREMBLYJP.Desalinationofhypersalinebrineswithjoule-heatingandchemicalpre-treatment:Conceptualdesignandeconomics[J].Desalination,2017,415:49-57.[5]SOLTANIRDC,JORFIS,RAMEZANIH,etal.UltrasonicallyinducedZnO-biosilicananocompositefordegradationofatextiledyeinaqueousphase[J].Ultrasonicssonochemistry,2016,28:69-78.[6]OGDENDD,TREMBLYJP.Dsesalinationofhypersalinebri-nesviaJouleheating:Experimentalinvestigationsandcompar-isonofresultstoexistingmodels[J].Esalination,2017,(424):149-158.[7]ZHOUW,LIY,GAOY,etal.NutrientsremovalandrecoveryfromsalinewastewaterbySpirulinaplatensis[J].Bioresourcetechnology,2017,245(PtA):10-17.7720188[8]GAGLIANOMC,LSMAILSB,AJMS,etal.Biofilmformationandgranulepropertiesinanaerobicdigestionathighsalinity[J].Waterresearch,2017,121:61-67.[9]MIRBOLOOKIH,AMIRNEZHADR,PENDASHTEHAR.Treatmentofhighsalinetextilewastewaterbyactivatedsludgemicroorganisms[J].Journalofappliedresearch&technology,2017,15(2):167-172.[10]PRADHANS,FANL,RODDICKFA,etal.ImpactofsalinityonorganicmatterandnitrogenremovalfromamunicipalwastewaterROconcentrateusingbiologicallyactivatedcarboncoupledwithUV/H2O2[J].Waterresearch,2016,94:103-110.[11],.[J].,2002,24(5):293-296.[12]TANS,CUIC,HOUY,etal.Cultivationofactivatedsludgeusingseamudasseedtotreatindustrialphenolicwastewaterwithhighsalinity[J].Marinepollutionbulletin,2016,114(2):867-870.[13],,,.[J].,2015,44(11):33-39.[14]FERRER-POLONIOE,PEREZ-UZB,MENDOZA-ROCAJA,etal.Biologicaltreatmentofhypersalinewastewaterfromtableoliveprocessing:processperformanceandprotistpopulationunderdifferentoperatingconditions[J].Journalofindustrial&engineeringchemistry,2017,56:364-374.[15]LABIADHL,FERNANDESA,CIRIACOL,etal.Electroch-emicaltreatmentofconcentratefromreverseosmosisofsanitarylandfillleachate[J].Journalofenvironmentalmanagement,2016,181:515-521.[16].[D].：,2016.[17],,.[J].,2016,24(2):14-17.[18]GUOP,HUAL,HONG-RUIMA,etal.Effectsofmonocarb-oxylicacidsstructureparametersonperstractionbytwokindsofsiliconerubbermembrane[J].Finechemicals,2016,33(8):915-920.[19]JORFIS,DARVISHICSR,AHMADIM,etal.Sono-assistedadsorptionofatextiledyeonmilkvetch-derivedcharcoalsupportedbysilicananopowder[J].Journalofenvi-ronmentalmanagement,2017,187:111-121.[20].———TNT[D].：,2016.[21]CHENJD,XIONGWL,TANGJQ,etal.Adsorptionbehaviorofbenzylalcoholonhyper-crosslinkedNAD-150Resin[J].Journalofwuhaninstituteoftechnology,2017,39(1):19-24.[22]JAAFARZADEHN,GHANBARIF,AHMADIM,etal.Efficientintegratedprocessesforpulpandpaperwastewatertreatmentandphytotoxicityreduction:Permanganate,Electro-FentonandCo3O4/UV/peroxymonosulfate[J].Chemicalengineeringj