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43820148AppliedChemicalIndustryVol.43No.8Aug.20142014-04-292012KTCG01-111980-。13891127505E-mail21978484@qq.com1964-、。029-88382706E-mailxianquct@xsyu.edu.cn123451.7173002.7186003.7273004.8340005.710065、、、、。20min1.5cm200A、、SRBTGB88.3mg/L、106mg/L、104105/mL1.6mg/L、2.1mg/L、101/mL102/mL。TE991B1671-3206201408-1547-02Studyofelectro-floatationofoilfieldwastewaterCAOWei-li1WANGYan-long2GUOMing3WANGYi-jun4QUCheng-tun51.ZichangOilProductionPlantofYanchangOilfieldYan’an717300China2.DingbianOilProductionPlantofYanchangOilfieldYulin718600China3.ShaanxiHuanglingCoal-ChenmicalLimitedLiabilityCompanyYan’an727300China4.SandaLimitedLiabilityCompanyofKaramayKaramay834000China5.Xi’anShiyouUniversityCollegeofChemistryandChemicalEngineeringXi’an710065ChinaAbstractElectro-floatationEFwasusedtodisposeofoilfieldwastewater.Theeffectofelectrodemate-rialselectrodeseparationdistancecurrentintensityelectricalconductivityondisposalwasdiscussed.Theexperimentalresultsshowedwhenelectro-floatationtimewas20minelectrodeseparationdistancewas1.5cmcurrentintensitywas200AelectrodematerialwasgraphitethecontentofsuspendsolidoilSRBandTGBwasreducedfrom88.3mg/L106mg/L104/mLand105/mLto1.6mg/L2.1mg/L101/mLand102/mL.Keywordsoily-producedwaterelectricairfloatationbactericidalactionremovalofiron、、、、、。-、、-、、、。O2Cl2H2、1。、、、、。11.1、、500mL43。1。1Table1Theanalysisresultsofproduced-water/℃pH/mg·L-1SS/mg·L-1/mg·L-1Fe2+/mg·L-1366.0106.688.317.215.81.220cm21.5cm200A20min。SY/T5329—2012、、。22.12、。2、Table2Influenceofcurrentdensitytoremovalrateofsuspendedsolidsandoilcontent/A/%/%5063.570.810075.981.315085.488.720090.292.425092.193.52、200A、。“”、2200A。2.2、3。3Table3Effectoftreatmentofelectricfloattoremovalrate/min/%/%1073.578.71585.686.22090.893.13092.294.24093.395.53、20min、。10~40μm80~100μm、3-5。2.3、4。4Table4Effectoftheelectrodespacingtoremovalrate/cm/%/%0.593.595.41.092.694.51.590.993.62.086.688.13.083.885.24、1.5cm、。2、。2.420cm220min200A1.5cm、5。5Table5Effectoftheelectrodematerialstoremovalrate/%/%90.993.682.384.779.673.996.498.25、、。、3。15528451432Table2Influenceofrepeatabilitytocatalystontheacetalreactionofbenzaldehydeandethyleneglycol/%/%191.799.4290.999.2389.499.1487.199.4585.499.025。3DawsonYH6P2Mo15V3O62YH6P2Mo15V3O62/PaAPTES0.2g93.3%。1.J.2000149-55.2.J.1998127-9.3.J.200012483-489.4.J.20001520-24.5.J.19992208-212.6.J.199421-10.7.M.1998.8.DawsonJ.198846757-763.15482.56。6Table6Theresultsofproduced-waterqualitybeforeandafterthetreatmentofelectricfloat/mg·L-1106.62.1<10SS/mg·L-148.01.6<5/mg·L-117.20.09<0.5/mg·L-112.41.1<2.0SRB/·mL-1104101101TGB/·mL-11051021026Cl23。3120min1.5cm200A。2、、SRBTGB88.3mg/L、106mg/L、104105/mL1.6mg/L、2.1mg/L、101102/mL。1.J.200929105-8.2.J.200231211-14.3.J.200611158-61.4.M.2001.5.M.2008.2551
本文标题:采油污水的电气浮处理技术研究
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