您好,欢迎访问三七文档
当前位置:首页 > 商业/管理/HR > 管理学资料 > 管式生物过滤器去除乙苯废气徐超
84环境工程学报Vol.8No.420144ChineseJournalofEnvironmentalEngineeringApr.201412123*121231.4100822.4100823.310018VOCs。、。TBFs。、EBCT、RE。。40mg/m340d15s40、80、120160mg/m3。。15s30s60s38.60g/m3·h。。。X701.7A1673-9108201404-1579-07EvaluationoftubularbiofilterperformancesforethylbenzeneremovalfromwastegasstreamsXuChao12YangChunping123HeHuijun12ChengYan12LyuLi31.CollegeofEnvironmentalScienceandEngineeringHunanUniversityChangsha410082China2.KeyLaboratoryofEnvironmentalBiologyandPollutionControlHunanUniversityMinistryofEducationChangsha410082China3.ZhejiangProvincialKeyLaboratoryofSolidWasteTreatmentandRecyclingCollegeofEnvironmentalScienceandEngineeringZhejiangGongshangUniversityHangzhou310018ChinaAbstractBiofiltrationisbecomingaconventionaltechnologyforthecontrolofvolatileorganiccompoundsVOCsandodoremissionsfromwastegasstreamsduetoitswellcost-effectivenessandenvironmentalfriendli-ness.Evendistributionofnutrientsolutionsbiofilmsandgasstreamswithinthemediumbediscrucialtoabetterperformanceofabiofilter.TubularbiofiltersTBFsmanufacturedinthislaboratoryshowthisadvantage.Inthisinvestigationperformancesoftubularbiofilterspackedwithpolyurethanespongemediawereevaluatedunderva-riousethylbenzeneloadingratesgasemptybedcontacttimeEBCTanddifferentgasflowrates.Theperform-ancesoftheTBFsweremonitoredatthestart-upperiod.Theacclimationofmicrobialtoethylbenzenewasa-chievedbyexposingthebiofilterbedtoaninletethylbenzeneconcentrationof40mg/m3andanEBCTof15sfor40days.ThentheTBFswereoperatedcontinuouslyatinletethylbenzeneconcentrationsof4080120and160mg/m3.ResultsshowedthattheethylbenzeneremovalefficiencyREdecreasedwithanincreasedethylbenzeneloadingrate.WhenEBCTincreasedfrom15sto30sand60sataconstantVOCloadingrateof38.60gethyl-benzene/m3·htheethylbenzeneREincreasedslightly.InadditionthemaximumaverageREwasdecreasedwhiletheeliminationcapacityincreasedwithincreasedgasflowrateataconstantinletethylbenzeneconcentration.ResultsalsoshowedthatsurfactantTritonX-100inthenutrientsolutionledtoahigherRE.Keywordsbiofiltrationethylbenzenesurfactanttubularbiofiltervolatileorganiccompound51278464200901611100102013-03-272013-06-131989~。E-mailxuchao0538@foxmail.com*E-mailyangc@hnu.edu.cn、、BTEX。BTEX。812。、、、、BTEX、、34。、5-8910。11-19。、、、、、20-23。、、、、。、、pH。。、、、VOCs。。、、、。11.1。。1.2TBFs。TBF96%30mm80mm140mm100mm1.036L。1.3TBFs、、。16cm0.5cm15cm。TBF。TBF。。VOCCO2H2O。。1Fig.1Schematicdiagramoftubularbiofilter1.4ethylbenzeneC8H1099.0%。。2。1.5、、。。。124。1.6FIDHP5890SeriesIIHewlett-PackardPaloAltoCali-fornia。HP-VOC60m×320μmID×1.8μm120℃120℃250℃。99%30mL/min99%30mL/min350mL/min。。085141Table1Compositionandconcentrationsofnutrientsolutionmg/Lmg/LNaNO3490NaHCO324.00KH2PO49.25K2HPO428.16CaCl22.69CuCl2·2H2O0.062MgSO44.40CoCl2·6H2O0.866MnCl2·4H2O0.144FeCl30.0926B20.00230.000890.00230.0023B60.0046B10.00231.7。TBF。、、EBCT。238d。1~3435~82、75~110、111~166167~238、EBCT、。2。2Table2Operatingconditionsofexperimentsg/m3·hmg/m3EBCTs35~429.65401543~5319.30801555~609.65401561~6928.951201570~749.65401575~8238.801601583~9338.803203094~10138.8016015102~11038.8064060111~1669.654015167~1849.654015185~19519.30407.5196~2029.654015203~22738.80403.85228~2389.65401522.1。15s21240mg/m39.65g/m3·h。2。2Fig.2PerformanceofTBFduringstart-upperiod。20mg/m380%。40mg/m390%。YangC.P.25。DeshussesM.A.26。TBF40mg/m3EBCT15s、。TBF。34TBF90%91.1%。27、7d12d1851819d。。。2.2。35~42TBF40mg/m39.65g/m3·h。43~53、61~6975~8280、160320mg/m319.30、28.9538.80g/m3·h。TBF40mg/m39.65g/m3·hTBF。3。3Fig.3InfluencesoforganicloadingrateonethylbenzeneRE3。35~4290.2%。43279.3%81.1%。61365.9%71.6%。75464.6%65.5%。2~3d。。。ChenH.7。。2.3EBCTEBCT38.80g/m3·h75~82TBF15s。83~93102~11030s60s。TBF160mg/m315sTBF。4。4EBCTFig.4InfluenceofEBCTonethylbenzeneRE4。75~8265.5%。8371%。102474.4%。。28514。。28。1~2d。EBCT4511。2.4TBFEBCT。。EBCT29。40mg/m3。175~184、185~198203~2279.65、19.3038.80g/m3·h15、7.53.75s。TBF9.65g/m3·h15sTBF。5。5Fig.5InfluencesofinletgasflowrateonethylbenzeneRE5175~18490.6%。1850.5m3/h7.5s19.30g/m3·h。19488.6%。2031.0m3/h。。21876.1%。3Table3Eliminationcapacityatvariousorganicloadingratesstagesg/m3·hEBCTsmg/m3g/m3·h%9.6515409.0490.419.30158015.6880.938.801516024.7165.74Table4Eliminationcapacityatvariousinletgasflowratesstagesg/m3·hEBCTsmg/m3g/m3·h%9.6515409.0290.619.307.54018.5088.638.803.754033.2976.1EBCTEBCT4。1∶2.05∶3.69。39.65、19.3038.80g/m3·h15s1∶1.73∶2.73。。2.5111~166。9.65g/m3·hEBCT15s。146。6。EBCT126~14589.6%。14693.7%。4385186Fig.6EffectofTritonX-100onperformanceofTBF。。。3134d。。2。。3。。4。EBCT。5。1.2.20022KimI.Thepromisingworldofbio-oxidation.Chem.Eng.Prog.2004100463KennesC.ReneE.R.VeigaM.C.Bioprocessesforairpollutioncontrol.J.Chem.Technol.Biotechnol.200984101419-14364KennesC.MontesM.LópezM.E.etal.Wastegastreat-mentinbioreactorsEnvironmentalengineeringaspects.Can.J.Civil.Eng.200936121887-18945./.2009418241-243SongNingningWangLipingHuaSulan.Treatmentofben-zeneandtoluenewastegasbybiotricklingfilter.JournalofHarbinInstituteofTechnology2009418241-243inChinese6YangC.P.ChenH.ZengG.M.etal.Modelingbiodeg-radationoftolueneinrotatingdrumbiofilter.WaterSci.Technol.2006541137-1447ChenH.YangC.P.ZengG.M.etal.Tubularbiofilterfortoluenere
本文标题:管式生物过滤器去除乙苯废气徐超
链接地址:https://www.777doc.com/doc-6566699 .html