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蒸发器用丝网除沫器的计算
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ITEMV-6721PROJ. N°CLIENTSERVICEGENERAL INPUTVaporFlowDensityViscosityFlowDensityViscosityPressureCALC'Svmax0.421992m/secVapor flow167.4907m3/h0.046525m3/secAmin0.110251m2D*min0.374668mDmin0.474668mID0.5mA0.19635m2Liquid flow40.02535m3/hHl5.435932mHl tot5.435932mHa6.535932mHb5.960932mH6.54mNOZZLESFeed (p x vi^2 <= 1500 kg/m sec)Density169.7083kg/m3IDfeed min157.1177mmVaporx50000IDvap. min64.65625mmLiquid (vl < 1m/sec)IDliq. minPRESSURE DROPDP gasDP dem.DP tot.2696.616.10.0232520.6812.50.13kg/hkg/m3cPkg/hkg/m3cPDATEREV.BY2014-9-110Demister (Kv= .06 critical / .09 non critical)Kv0.06-Hold upHHL-HLHL-LLLL-LLLHtLLL-emp.0min1.6minmin1.6min0mLiquid36bar(a)RESULTVesselIDHAVSIDfeed minIDvap. minIDliq. min0.56.540.1961.28410.6661576.2652.51194.7mmm2m3m2mminmminmmin150550400HHL65400HL5440118.9793mm0LLLLL0.026363kg/cm20.0025kg/cm20.0289kg/cm20REMARKS: 232290973.xls
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