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469Vol.46No.920189CoalScienceandTechnologySep.20181212121211.1022112.1000112。-30%37.81000/t30%。X703A0253-2336201809-0037-07Processintroductionandtechno-economicanalysisonpuresaltrecoverycrystallizationforhighsalinitywastewaterXIONGRihua12HECan12MARui12LIUJie12LIUZhaofeng11.NationalInstituteofClean-and-Low-CarbonEnergyBeijing102211China2.StateKeyLaboratoryofWaterResourceProtectionandUtilizationinCoalMiningBeijing100011ChinaAbstractItisofgreatimportancetoprovideoptimalpuresaltrecoverycrystallizationprocessdesignsandmaximizerecoveryofpuresaltsatthelowestcostwhileachievingzeroliquiddischargeforthehighsalinitywastewateratcoalchemicalandotherindustries.Inthispapervarioustypicalpuresaltrecoverycrystallizationprocessesforhighsalinitywastewaterweredescribedanddiscussed.Exemplarypuresaltre-coveryprocessdesignswerethenprovidedanddiscussedwithahighsalinitycoalchemicalwastewaterasthefeedstream.Quantitativetech-no-economicanalysiswasfurtherperformedforthethermalandthemembrane-basedpuresaltrecoverycrystallizationprocesses.There-sultsindicatethatthemembrane-basedprocessshows30%highercapitalcostbutsaves30%operationcostasaresultof37.8higherper-centagerecoveryrateofpuresalts.Itisconcludedthatthemembrane-basedprocessisabettersolutioninthiscaseespeciallywhenthedisposalcostofthemixedsaltwasteishigh.Keywordshighsalinitywastewaterzeroliquiddischargepuresaltrecoverycrystallizationnanofiltrationlowtemperaturecrystallization2018-06-08DOI10.13199/j.cnki.cst.2018.09.006GJNY-18-711978—。E-mailxiongrihua@nicenergy.com.J.201846937-43.XIONGRihuaHECanMARuietal.Processintroductionandtechno-economicanalysisonpuresaltrecoverycrystallizationforhighsalinitywastewaterJ.CoalScienceandTechnology201846937-43.0。、。3000~50000mg/L。1-2。。。、、、7320189463-56-7。2015《》、、。、、18-9。10-12。。。。2017《“”》。。13-1516-18。2。1。。2。1.1、。1.1.1。1。1Fig.1FlowchartofdirectevaporationcrystallizationprocessⅠ。Ⅱ。。、。19。1.1.2。2。2Fig.2FlowchartofNaCl-Na2SO4co-productioncrystallizationprocess8320189。50~120℃20。I。ⅠⅡ。Ⅰ。。。。。。50~120℃60℃100℃45.3g42.5g-6.2%37.3g39.8g6.7%。。1.1.30~30℃。。30℃40.8g20℃19.5g10℃9.1g0℃4.9g。。30℃0℃36.3g35.7g。。。3。3Fig.3Flowchartofcombinedhighandlowtemperaturecrystallizationprocess。。。1.2。。1.2.1。。。95%。。4。7%0℃93201894621。。。4-Fig.4Flowchartofcombinednanofiltrationandlowtemperaturecrystallizationprocess-。。。1.2.2。5。。。。5Fig.5Schematicworkingprincipleonelectrodialysisbasedsaltseparationprocess。。。。。230m3/h14000mg/L42000mg/L。4000mg/L、。。2.114000mg/L42000mg/L6。6Fig.6Flowchartdesignandmassbalancewiththermalsaltrecoverycrystallizationprocess50%。15m3/hⅠ104~107℃800kg/h。I88%1.4m3/h23%。ⅠⅡ82~86℃1000kg/h。042018944.4%。2.2-7。7Fig.7Flowchartdesignandmassbalancewithmembranebasedsaltrecoverycrystallizationprocess。8.5%0℃2560kg/h。2.6m3/hⅡ。98%。75%。6.5m3/hⅠ350kg/hⅡ320kg/h。82.2%。3、。、、、。。2.12.22。3.1。2。3.1.11。。。293%~96%。99%。98%~99%。3。。。3.1.22.163.5%44.4%。。。2.214201894689.6%83.3%82.2%。。3.21。26721。12Table1Estimationofcapitalcostwithtwodifferentsaltrecoverycrystallizationprocesses/200200030015006000100030050020002600130%。。。。2。、。。6722。29.719.4。1000/t43.030.1。30%。22Table2Estimationofoperationcostwithtwodifferentsaltrecoverycrystallizationprocesses/·t-12.02.602.66.89.103.20.91.933.310.743.030.16008000h3101.9。3000/t14000.4。4。。。30m3/h-282.2%44.4%。30%1000/t242018930%。3000/t0.4。References1SEMBLANTEGalileeUyLEEJounathanZhiqiangLEELaiYokeetal.Brinepre-treatmenttechnologiesforzeroliquiddis-chargesystemsJ.Desalination201844196-111.2XIONGRihuaWEIChang.CurrentstatusandtechnologytrendsofzeroliquiddischargeatcoalchemicalindustryinChinaJ.JournalofWaterProcessEngineering201719346-351.3XIEKechangLIWenyingZHAOWei.CoalchemicalindustryanditssustainabledevelopmentinChinaJ.Energy2010354349-4355.4.J.2011362179-184.ZHANGYuzhuo.ConstructionandoperationofShenhua’smoderncoal-to-liquidandchemicalsdemonstrationprojectsJ.JournalofChinaCoalSociety2011362179-184.5.J.2016444189-195.LIUYanliLIUGe.Analysisanddiscussiononhighwatercon-sumptionproblemofcoalchemicalindustryJ.CoalScienceandTechnology2016444189-195.6.J.201442745-47.TONGLiZHOUXueshuangDUANFeizhouetal.Analysisandcoun-termeasuresonenvironmentalrisksofChina’smoderncoalchemicalindustryJ.EnvironmentProtection201442745-47.7.J.20173925-8.LIANGRuiLIJiwenLYUWeietal.EnvironmentalpermitanddevelopmentsuggestionsofmoderncoalchemicalindustryinChinaJ.EnvironmentalImpactAssessment20173925-8.8TONGTiezhengELIMELECHMenachem.TheglobalriseofzeroliquiddischargeforwastewatermanagementdriverstechnologiesandfuturedirectionsJ.EnvironmentalScience&Technology2016506846-6855.9.J.20174511205-210.MAOWeidongZHOURuluGUOZhongquan.ZeroliquiddischargetreatmenttechnologyandapplicationforcoalminedrainagewaterJ.CoalScienceandTechnology20174511205-210.10.J.201142570-75.WEIJiangbo.ZeroliquiddischargepracticeandexplorationoncoaltoliquidwastewaterJ.IndustrialWaterandWastewater201142570-75.11.“”J.201331218-24.QUFengchen.ThekeytechnologiesandproblemsofwastewaterzerodischargeincoalchemicalindustryJ.ChemicalIndustry201331218-24.12.J.2015431120-124.HEXuwenWANGChunrong.Zerodischargetechnologyandsolu-tionideaofwastewaterfromnewcoalchemi
本文标题:高盐废水分盐结晶工艺及其技术经济分析熊日华
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