附錄一物料計(jì)算書(shū)

1.11.2物料1.11.2物料衡算目1.3物料衡算方1-1各衡算方法適用類1-1各衡算方法適用類原始原子物質(zhì)的量衡適適適總衡算組分衡算元素原子衡算1.4總項(xiàng)目衡1.4.11.4.21-1醋酸乙烯合成表1-2醋酸乙烯合成工段總物料衡進(jìn)1.4.21-1醋酸乙烯合成表1-2醋酸乙烯合成工段總物料衡進(jìn)進(jìn)出流股編出10111℃VaporFracMassFlowkg/hrVolumeFlowMass00007.03E-5.03E-4.33E-6.89E-0000Mass0000總00002.07E-3.52E-2.52E-2.17E-3.45E-1.4.2.1醋酸乙烯反應(yīng)器1-2醋酸乙烯反應(yīng)器1-3醋酸1.4.2.1醋酸乙烯反應(yīng)器1-2醋酸乙烯反應(yīng)器1-3醋酸乙烯預(yù)反應(yīng)器物料衡算表11流股編11℃VaporFracMassFlowkg/hrVolumeFlowMass0000Mass00001.4.2.2換熱器1-3換熱器表1-4換熱器（E0101）物料衡算進(jìn)出1.4.2.2換熱器1-3換熱器表1-4換熱器（E0101）物料衡算進(jìn)出流股編Temperature℃PressurebarVaporFracMoleFlowMassFlow100010Mass00006.143E-Mass6.143E-0000總00002.57E-4.408E-2.68E-2.57E-4.408E-2.68E-00001.4.2.3換熱器1-4總00002.57E-4.408E-2.68E-2.57E-4.408E-2.68E-00001.4.2.3換熱器1-4換熱器表1-5換熱器（E0102）物料衡算進(jìn)流股編出1111℃PressurebarVaporFracMoleFlowMassFlowMass3.021E-Mass1.58E-2.92E-6.38E-3.021E-Mass1.58E-2.92E-6.38E-3.021E-總1.58E-2.92E-6.38E-1.4.2.4換熱器1-5換熱器表1-進(jìn)出流股編出℃VaporFracMassFlowkg/hrVolumeFlowMassMassMassMass總1.4.2.5換熱器1-6換熱器表1-流股編出℃1010PressureVaporMoleFlowMassFlowkg/hr--MassMoleFlowMassFlowkg/hr--Mass00000000Mass0000總00001.4.2.6壓縮機(jī)1-7壓縮機(jī)表1-8壓縮機(jī)（C0101）物料衡算表Pressure出1VaporFracMassFlowkg/hrVolumeFlow11MassVaporFracMassFlowkg/hrVolumeFlow11MassMass總1.4.2.7混合器1-8混合器1-9混合器（M0101）物料衡算進(jìn)表進(jìn)出流股編出Temperature℃PressurebarVaporFracMoleFlowMassFlowkg/hr10MassTemperature℃PressurebarVaporFracMoleFlowMassFlowkg/hr10Mass0000117.034E-5.03E-4.33E-13.0E-Mass總00001.68E-2.85E-2.04E-1.75E-1.58E-2.92E-6.38E-1.4.2.8混合器1-混合器表1-10混合器（M0102）物料衡算進(jìn)出Temperature℃PressurebarVaporFracMoleFlow進(jìn)出Temperature℃PressurebarVaporFracMoleFlowMassFlowkg/hr11Mass000017.03E-5.03E-4.33E-6.89E-117.03E-5.03E-4.33E-Mass總00002.07E-3.52E-2.52E-2.17E-3.45E-1.68E-2.85E-2.04E-1.76E-1-10氣體分離工1-11氣體分離工段物料衡算表X進(jìn)出出流股編VaporFracMoleFlowMassFlow1-10氣體分離工1-11氣體分離工段物料衡算表X進(jìn)出出流股編VaporFracMoleFlowMassFlow-00118254Mass1.412E-7.03E-3.51E-7.99E-Mass7.00E-6.543E-7.446E-1.743E-3.96E-5.03E-4.33E-6.89E-4.38E-1.91E-3.51E-7.99E-Mass7.00E-6.543E-7.446E-1.743E-3.96E-5.03E-4.33E-6.89E-4.38E-1.91E-2.14E-2.07E-3.52E-2.52E-2.17E-3.45E-1.164E-8.456E-總1.4.3.1換熱器1-11換熱器表1-進(jìn)出流股編出11℃VaporFracMoleFlowMassFlowkg/hrMass7.03E-7.03E-5.03E-4.33E-6.89E-Mass2.07E-3.52E-2.52E-2.17E-3.45E-5.03E-4.33E-6.89E-總5.03E-4.33E-6.89E-Mass2.07E-3.52E-2.52E-2.17E-3.45E-5.03E-4.33E-6.89E-總2.07E-3.52E-2.52E-2.17E-3.45E-1.4.3.2換熱器1-12換熱器表1-13進(jìn)出流股編0101℃VaporFracMoleFlowMassFlowVolume--Mass7.03E-5.03E-4.33E-6.89E---Mass7.03E-5.03E-4.33E-6.89E-7.03E-5.03E-4.33E-6.89E-Mass2.07E-3.52E-2.52E-2.17E-3.45E-總2.14E-2.14E-2.07E-3.52E-2.52E-2.17E-3.45E-1.4.3.3泵1-13泵1-表流股編出℃-0-0PressureVaporMoleFlowMassFlowkg/hrMassMoleFlowMassFlowkg/hrMass3.51E-3.51E-Mass4.68E-1.24E-總4.68E-1.24E-1.4.3.4混合器1-14混合器表1-15混合器（M0201）物料衡算進(jìn)進(jìn)出流股編出-℃VaporFracMoleFlowMassFlowkg/hr0VaporFracMoleFlowMassFlowkg/hr0Mass3.51E-0--Mass總4.6E-1.24E-1.4.3.5第一脫氣塔1-第一脫氣塔1-16第一脫氣塔（T0201）物料衡算進(jìn)表出流股編Temperature℃1-16第一脫氣塔（T0201）物料衡算進(jìn)表出流股編Temperature℃PressurebarVaporFracMoleFlowMassFlowkg/hrMass-11.41E-3.52E-7.997E-0-Mass總7.00E-6.54E-7.45E-1.743E-3.963E-1.4.3.6第二脫氣塔1-16第二脫氣塔表1-171.4.3.6第二脫氣塔1-16第二脫氣塔表1-17第二脫氣塔物料衡進(jìn)出流股編TemperatureVaporFracMassFlowkg/hrVolumeFlow-Mass-10-4.38E-1.91E-Mass1.164E-8.456E-2.15E-總3.6775E-1.4.3.7洗滌塔1-洗滌塔表1-18洗滌塔（T0207）物料總3.6775E-1.4.3.7洗滌塔1-洗滌塔表1-18洗滌塔（T0207）物料衡算進(jìn)出流股編TemperatureVaporFracMassFlowkg/hrVolumeFlow0-110Mass00001.412E-3.51E-7.99E-Mass7.034E-5.03E-4.33E-6.89E-3.51E-0總0007.00E-6.543E-7.446E-1.743E-3.96E-2.077E-3.52E-2.52E-2.17E-3.45E-4.68E-1.247E-總0007.00E-6.543E-7.446E-1.743E-3.96E-2.077E-3.52E-2.52E-2.17E-3.45E-4.68E-1.247E-1-18乙醛精制工表1-19乙醛精制工段物料衡算進(jìn)進(jìn)出出20-流股編Temperature℃PressurebarVaporFracMassFlowkg/hrVolumeFlow0-0-0002Mass000008.935E-1.884E-1.218E-2.609E-6.734E-1.11E-1.196E-7.506E-Mass3.161E-6.665E-5.94E-4.31E-總0000012.114E-Mass3.161E-6.665E-5.94E-4.31E-總0000012.114E-5.45E-4.150E-4.435E-2.783E-6.618E-1.4.4.1泵1-泵表1-進(jìn)出流股編出0-0-℃VaporFracMassFlowkg/hrVolumeFlowMassMass總Mass總1.4.4.2換熱器1-20換熱器表1-進(jìn)出流股編出0-Mass 20-℃VaporFracMoleFlowMassFlowkg/hrMassMass總1.4.4.3萃取塔1-21萃取塔表1-22萃取塔（T0301）物料衡算進(jìn)出Temperature℃PressurebarVaporFracMoleFlowMassFlow0000VolumeFlow----Mass00000VolumeFlow----Mass000008.935E-1.884E-1.218E-Mass總0000013.161E-6.665E-5.94E-4.31E-1.4.4.4乙醛精制塔1-22乙醛精制塔表1-23乙醛精制塔（T0302）物料衡算流股編進(jìn)出℃VaporFracMoleFlowMassFlowkg/hr00002VaporFracMoleFlowMassFlowkg/hr00002Mass1.11E-1.196E-7.506E-2.609E-6.734E-Mass2.114E-5.45E-總4.150E-4.435E-2.783E-6.618E-1.4.5圖1-23甲基丙烯酸甲酯合成工表1-24醋酸乙烯精制工段總物料衡進(jìn)出流股編TemperaturePressureMoleFlowMassFlow00000--8.935E-MoleFlowMassFlow00000--8.935E-7.456E---Mass8.92E-1.88E-1.21E-6.14E-04.6448E-06.3577E-001.044E-Mass總2.57E-4.40E-2.68E-3.15E-6.669E-5.94E-4.31E-6.853E-5.719E-1.296E-5.756E-002.649E-03.493E-01.31E-4.781E-1.4.5.1泵1-24泵1-25泵（P0401）物料衡算進(jìn)進(jìn)出流股編出Temperature℃PressurebarVaporFracMoleFlowMassFlowkg/hr0-Temperature℃PressurebarVaporFracMoleFlowMassFlowkg/hr0-0-Mass8.92E-Mass3.33E-6.32E-8.92E-總3.33E-6.32E-1.4.5.2混合器1-25混合器表1-26混合器（M0401）物料衡算進(jìn)進(jìn)出出Temperature℃PressurebarVaporFracMoleFlowMassFlowkg/hrTemperature℃PressurebarVaporFracMoleFlowMassFlowkg/hr0-Mass6.14E-0-8.92E-1.88E-1.21E-0-8.92E-Mass總2.57E-4.40E-2.68E-3.15E-6.669E-5.94E-4.31E-3.33E-6.32E-1.4.5.3脫乙醛塔圖1-脫乙醛塔1-27脫乙醛塔（T0401）物料衡算進(jìn)表出流股編1-27脫乙醛塔（T0401）物料衡算進(jìn)表出流股編0-Mass0-0-℃VaporFracMoleFlowMassFlowkg/hr6.1E-Mass總2.15E-2.569E-4.403E-2.669E-1.4.5.4醋酸乙烯精制塔1-27醋酸乙烯精制塔表1-281.4.5.4醋酸乙烯精制塔1-27醋酸乙烯精制塔表1-28醋酸乙烯精制塔（T0402）物料衡算出Temperature℃PressurebarVaporFracMoleFlowMassFlowkg/hr0-Mass8.93E-0-8.935E-7.456E-0-8.799E-1.281E-1.05E-Mass3.343E-6.32E-6.853E-5.719E-1.296E-5.756E-6.427E-9.363E-總7.66E-1.4.5.5醋酸精制塔1-28醋酸精制塔總7.66E-1.4.5.5醋酸精制塔1-28醋酸精制塔表