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当前位置:首页 > 机械/制造/汽车 > 汽车理论 > BSSF滚筒法液态钢渣水淬尾气净化工艺的分析刘钰天
BSSF112221.2016202.、243000BSSF、、、。。5.0m/s、4.00.7L/m3。THEANALYSISOFPURIFICATIONPROCESSOFTHETAILGASFROMSTEELSLAGWATERQUENCHINGBYBSSFROLLERMETHODLiuYutian1ShenHenggen1YanWeihua2MaJianping2HuJia21.CollegeofEnvironmentalScienceandEngineeringDonghuaUniversityShanghai201620China2.AnticorrosiveandEnvironmentalProtectionBranchMaanshanSteelGroupIndustrialDevelopmentCompanyMaanshan243000ChinaAbstractAimingatthecharacteristicsashighhumidityintermittencebigvolatilitysmallsizeofdustparticleetcofthetailgasfromsteelslagwaterquenchingbyBSSFrollermethoditwasproposedcombinedprocessofswirlingspraydustingandself-stimulatedwetdusting.Anditwasdemonstratedthededustingeffectoftheprocessbythespecificengineeringexamplesandcombinedwiththetheoryanalysisandnumericalsimulation.Theresultsshowthatthesizeofparticulatescanbeincreased.adoptingaerosoltwo-phaseguntosprayinthepipeatthefrontofthedustremovalequipmentandthroughthecollisionbetweensubtlemotesanddroplets.Whenthepipelinesectionaveragewindspeedsare5m/sandcylinderentranceandpipelinesectionarearatioisaround4theliquid-gasratioisnotlessthan0.7thepurificationprocesscanachievededustingrequirements.Keywordsliquidsteelslagwaterquenchingfluegaspurificationswirlingspraydedustingself-stimulatingdeduster1BSSFBaosteel'sshort-flow。、、、、、。11-2。1。3276mg/m38720118294DOI:10.13205/j.hjgc.2011.04.009EGB/T16157—19962.5m3.5m3012H。pH11~13≤100mg/L5min20min3~10t1300℃1.3MPa200~210℃250m。1。1/L/%/m3·h-1/m3·h-1/kPa/Pa/m·s-1/mg·m-3/℃/mm27.6029.304.76×1049.28×104100.621.005.303376.2076.02500×82、、。。。。2.1BSSF5min20min。6~9m3/h76℃5m/s3276mg/m3。1。2.2BSSF22。PM1050%2μm14%2~10μm26%~32%。2/μm/%123/%≤13.343.333.823.501~210.077.858.938.952~1037.8126.5630.1831.52>1048.8162.2657.0556.04100.03100.0099.98100.00。。、。2.32。21。。2。。3。4。。59720118294。6。。34η=1-exp-32·avrd·Hvg()Ea———vr———m/sd———mH———mvg———m/sE———。zr=RH。a=L2πRHvrL———m3/s。η=1-exp-34·δdr0Er*U*()zδ、r0、d、r*U*z。Herne4EStk。E=0.00376-0.464Stk+9.68Stk2-16.25Stk30.0416≤Stk≤0.3E=Stk2Stk+0.252Stk≥0.3StkStk=vrρpd2p18μdvr=322d1.5ρlv2t15υ0.5ρg槡RStkStk=ρpd2p18μd·322d1.5ρlv2t15υ0.5ρg槡R=Cd2pv2t()R232/3。、、。44.13。3。4。45。551/m1μm、3000kg/m3。082011829454∶13.821600mm×400mm。4.2。。。6。δ/d。δ/d。1μmδ/d>790%。67FM2571/mFM253。7。FM25100μm0.7L/m350t/hFM257t/h7214。3。3FM25/7/mm5.0/MPa0.30/m3·h-17/m3·h-1150/MPa0.304.3S、。58。896%。3276mg/m3。。。。9。8918201182944、5。8.78t/a。4/m3·h-1/mg·m-3/kg·h-12008-05-09125614865.216.70225363058.414.81325357559.615.112008-05-10125463563.516.17225486161.715.72325471664.316.385/m3·h-1/mg·m-3/kg·h-12008-05-0912785834.81.3422706744.61.2532736294.51.232008-5-1012675314.31.1522713164.11.1132700084.41.191。2。1.M.1996.2.M.2005.1000883301082227673E-maillopoco@yeah.net2010-12-15櫅櫅櫅櫅櫅櫅櫅櫅櫅櫅櫅櫅櫅櫅櫅櫅櫅櫅櫅櫅櫅櫅櫅櫅櫅櫅櫅櫅櫅櫅櫅櫅櫅櫅櫅櫅櫅櫅櫅櫅櫅櫅櫅櫅櫅櫅櫅櫅櫅櫅81998.5%>99%50mg/m3。。51、、、。2BSSF5m/s、0.7L/m3、4。1.BSSFJ.2009z190-94.2.BSSFJ.2009321-23.3.FM10J.2004440-41.4.M.1987.5.M.2005.20162029993145E-mailliuyutian1234@163.com2010-11-299820118294
本文标题:BSSF滚筒法液态钢渣水淬尾气净化工艺的分析刘钰天
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