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CFB脱硫塔设计计算

上传者:菩提 |  格式:xls  |  页数:5 |  大小:694KB

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nabsorber,modatethebottomconditions.TocalculateGasdensityAvg.molecularweight=29.45Kg/KmolIfgasflowrateisgiveninkg/hIfgasflowrateisgiveninm3/hGasin=0.009432183Kmol/sGasin=(m3/s)x273kmol=mass/molwtTinkelvin=(kmol/s)xTinkelvinx1.0atmx22.4273pr.Inatm1=0Kmol/s=0.234499m3/s=0Kg/smass=molwtxkmolSelectvol.flowrateandmassflowratefromabove,Selectedmassflowrate=0.277777778Kg/sSelectedvol.Flowrate=0.234499m3/sSelectedmolarflowrate=0.009432183Kmol/sTherefore,gasdensity=1.1846Kg/m3(massflowrate/vol.Flowrate)TofindL',G'andTowerc/ponentremoved=0.0207Kg/s(p.xmol.Wt.)Liquidleaving=0.0420Kg/s(p.Removed)L'G0.5=0.00497G'LUsing0.00497asordinate,Referfig.6.34usingagaspressuredropofG'2CfµL0.1J=0.04(fromgraph)G(L--G)gcTherefore,G'=0.04G(L--G)gc0.5CfµL0.1J=1.6665Kg/m2.sTowerc/sarea=0.1667m2(c/sarea=massflowrate/G')

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