35万吨C4综合利用项目 尚川--附录.docVIP

35万吨C4综合利用项目—附录  PAGE \* MERGEFORMAT 52 35万吨C4综合利用项目—附录  PAGE \* MERGEFORMAT 24 附录一物料衡算一览表 1.1丁二烯抽提工段 流入物流1流入物流2流出物流1流出物流2Temperature C39.990317341.4648835.24148130.3244Pressure MPa0.450.460.390.53Vapor Frac0100Mole Flow kmol/hr4104.26362814.3707428.12574490.509Mass Flow kg/hr3000004500024100320900Volume Flow l/min5372.8315777182.63697.80056660.748Enthalpy Gcal/hr-231.736258.841078-3.5805-207.005Mass Flow kg/hrDMF30000003.77E-08300000IBUTANE01801806.04E-19N-BUTANE0261026102.49E-111-BUTENE2.87E-1516771.516771.50.000282CIS-2-BU2.82E-0818001571.021228.9789TRA-2-BU9.76E-1123222319.9112.088866ISOBU1.13E-16526.5526.59.35E-061,3C44.14E-052038576.0679620308.93C4H40.00021923151.54E-05315.0002C5H121.39E-08454.36E-0544.99996C3H6045451.89E-28Mass FracDMF101.56E-120.934871IBUTANE00.0040.0074691.88E-24N-BUTANE00.0580.1082997.77E-171-BUTENE9.57E-210.37270.6959138.79E-10CIS-2-BU9.39E-140.040.0651880.000714TRA-2-BU3.25E-160.05160.0962626.51E-06ISOBU3.78E-220.01170.0218462.91E-111,3C41.38E-100.4530.0031560.063287C4H47.31E-100.0076.40E-100.000982C5H124.64E-140.0011.81E-090.00014C3H600.0010.0018675.89E-341.1.1第一萃取精馏塔（T0101） 1.1.2第一汽提塔(T0102) 物流流入物流流出1??流流出2Temperature C600.395441111.6394Pressure MPa0.510.0250.03Vapor Frac010Mole Flow kmol/hr4490.50868387.61314102.896Mass Flow kg/hr32090021000299900Volume Flow l/min6096.67697587711.25831.451Enthalpy Gcal/hr-219.971689.970353-220.34Mass Flow kg/hrDMF30000099.99993299900IBUTANE6.04E-1900N-BUTANE2.49E-11001-BUTENE00.0002822.87E-15CIS-2-BU228.978862228.97892.82E-08TRA-2-BU2.08886632.0888669.76E-11ISOBU9.35E-069.35E-061.13E-161,3C420308.932120308.934.14E-05C4H4315.00019315.00010.000138C5H1244.999956444.999961.39E-08C3H61.89E-2800