您好,欢迎访问三七文档
当前位置:首页 > 行业资料 > 冶金工业 > 超强永磁场处理对工业循环水电导率影响的研究
1,2113(1.,100083;2.,014030;3.,518066),:、、;(Ca2+2.5mmol/L),0.62.3m/s,;CaCl2Ca(HCO3)2(Ca2+2.5mmol/L),1.22.3m/s,。:、,,。;;;;InfluenceofPermanentMagneticFieldTreatmentonConductivityofIndustrialCirculatingWaterLiDongkui1,2JiangLili1ZuoHaibin1TanZanlin3(1.SchoolofMetallurgicalandEcologicalEngineering,UniversityofScienceandTechnology,Beijing100083,China;2.SchoolofInformationScienceandTechnology,BaotouTeacher'sCollege,BaotouInnerMongolia014030,China;3.ShenzhenYitianMagneticMaterialCo.Ltd.,ShenzhenGuangdong518066,China)ABSTRACTInthisresearch,thedevelopedwatertreatmentequipmentadoptingpermanentmagneticfieldwasusedtosimulatethephysicalhandlingprocessoftheindustrialcirculatingwatersysteminthelaboratory.Theexperimentshowthatthemagneticfieldintensity,processingtimeandflowratehavenotableimpactontheconductivityofcirculatingwa-ter;whenthecirculatingsolutionistapwater(Ca2+concentrationislessthan2.5mmol/L),velocityis0.6m/sor2.3m/s,theconductivityofthetreatedsolutionfirstlyincreaseswiththeincreasingofthemagneticfieldtreatmenttimeandthenpresentsthemulti-extremumproperty;whenthecirculatingsolutioniscalciumchlorideandcalciumbicarbonatemixedsolution(Ca2+concentrationisgreaterthan2.5mmol/L),velocityis1.2m/sor2.3m/s,theconductivityofthetreatedsolu-tionfirstlydecreaseswiththeincreasingofthemagnetictreatmenttimeandthenpresentsthemulti-extremumproperty.Theresultsshowthatchoosingtheappropriatemagneticfieldintensity,flowrateandprocessingtimeofcirculatingwater,theconductivityofthetreatedcirculatingwatercanbecontrolled,thehazardsofthescalinginthecirculatingwatersys-temmaybereduced.KEYWORDScirculatingwater;magneticfieldtreatment;two-wayANOVA;conductivity;scaleinhibition:(1963-),,,,:,。201112Dec.2011286Vol.28No.6CEMENTEDCARBIDE!!!!!!!!!!doi:10.3969/j.issn.1003-7292.2011.06.00728282828,,,、[1-3]。[4-5]。[6-8]。,[9-11]。,、、pH、,、[12-21]。。CaCO3,,,,。,Ca2+2.5mmol/L,CaCO3;2.5mmol/L,CaCO3[17-18]。,Ca2+、HCO3-1,[19]。,CaCO3,[20]。,pHCa2+,[18-21]。,、、,。。11.11,,,。1)(YT-CQY-0702);300~34000Gs。(1Gs=10-4T)。2)。3)Mettler-ToledoDelta326。4)。5)Na2CO3、CaCl2()。1.21.2.11):300,7000,17000,2650034000Gs;0.6、1.22.3m/s。,。、。、、12h;2):30L;0.6m/s;;300Gs。,1h,200mL,,(,,,,1Fig.1SimulatorofcirculatingwatertreatmentequippedwithPermanentMagneticFieldDevice(PMD)Submersible374··28282828,)、;12h,、。,;;30L,7000Gs,;;,。1.2.21.2.1,:2.22gNa2CO320L,,6.24gCaCl210L,,。1200mL、,,,1.5h1、,6。12h,,、。,,。1.3,,。Ca2+CO32-,,,Ca2+CO32-。Ca2+CO32-,,,CaCO3。,CaCO3,,,CaCO3。[25]。22.11、2、。2.2(Dixon)[22],。1、2,*、**,,OriginPro8SR1,。3。33.11),0.6m/s,2(a),4;2.3m/s,2(b),5。0.62.3m/s(2.3m/s、300Gs1h),,2:。3,2.3m/s,;0.6m/s,。,12h(),12h,。0.6m/s,()[16];2)1.2m/s,3(a);6;2.3m/s,3(b);7。1.22.3m/s(2.3m/s,7000Gs3h),3:;3h。3,2.3m/s,;1.2m/s,,,12h,;3h,CaCO3Ca(HCO3)2,1.5hHCO3-,CaCO3,1.5hCO2,HCO3-,,“”[16]。,,,:375··28282828Circulatingwaterflowrate/(m/s)2.3Conductivityofsampleafterstandingfor12h0.6Conductivityofsampleafterstandingfor12h1.2Conductivityofsampleafterstandingfor12h1Table1Observedconductivityvaluesundervariousmagneticintensityandtreatmenttimewhencirculatingwateristapwater(Conductivity:μS/cm)Time/h012345xj012345012345xj012345012345xj012345300Gs579575590616607647*602.3573583568581582579557560576582586604577.5561570567571572707**682587591603625630619.7587584584568**5885857000Gs576585589608601612595.2582584571570569570560563573571579618577.3582561573561562559572580583605616599592.558.357256557457757417000Gs540552564569566592563.8560550541552562560569572581574600583579.8570582581583564577549565573575572590570.755455755555555355526500Gs570575592586609615591.2581582663**581582584562565568571576582570.7575585560564556569551557566582576584569.356855956455955755934000Gs573574575581609616588575583568575579570567566572573603606581.17575572573565*572577540553556573584567562.2544545552548551557xi567.6572.2582592598.4616.4563565.2574574.2588.8598.6577.33569.67576.33587597.83598.33Note:1.xiistheaverageconductivityunderthesamesampletimeanddifferentmagneticintensity;xiistheaverageconductivityunderthesamemagneticintensityanddifferentsampletime.2.Thedeviationvaluesaremarkedby*,theoutliersaremarkedby**.376··28282828Circulatingwaterflowrate/(m/s)2.3Conductivityofsampleafterstandingfor12h0.6Conductivityofsampleafterstandingfor12h1.2Conductivityofsampleafterstandingfor12h2Table2Observedconductivityvaluesundervariousmagneticintensityandtreatmenttimewhencirculatingwaterismixedsolution(Conductivity:μS/cm)Time/h01.534.567.5xj01.534.567.501.534.567.5xj01.534.567.501.534.567.5xj01.534.567.5300Gs960930961980984999976.892010791050959932925100997699699710011011998.33476472469466428**646-------------7000Gs10151447**1046100298910841027.29829129519739159399779349599839881044980.33917901909905900902994104510941074107210651057.3939944100199399699817000Gs997963994953109910631021.2943930945*934935930103810101020104110441093*10419729759699699559541067103610421053112210881068993100099899399298826500Gs9509531184126995210161074.2981938115212179098701004984100210049791015998942940943941931921105810241026109910639921044100198498297496996534000Gs986965969988103810631008.893492491792893095
本文标题:超强永磁场处理对工业循环水电导率影响的研究
链接地址:https://www.777doc.com/doc-6547328 .html