附录一物料计算书

1.11.2物料1.11.2物料衡算目1.3物料衡算方1-1各衡算方法适用类1-1各衡算方法适用类原始原子物质的量衡适适适总衡算组分衡算元素原子衡算1.4总项目衡1.4.11.4.21-1醋酸乙烯合成表1-2醋酸乙烯合成工段总物料衡进1.4.21-1醋酸乙烯合成表1-2醋酸乙烯合成工段总物料衡进进出流股编出10111℃VaporFracMassFlowkg/hrVolumeFlowMass00007.03E-5.03E-4.33E-6.89E-0000Mass0000总00002.07E-3.52E-2.52E-2.17E-3.45E-1.4.2.1醋酸乙烯反应器1-2醋酸乙烯反应器1-3醋酸1.4.2.1醋酸乙烯反应器1-2醋酸乙烯反应器1-3醋酸乙烯预反应器物料衡算表11流股编11℃VaporFracMassFlowkg/hrVolumeFlowMass0000Mass00001.4.2.2换热器1-3换热器表1-4换热器（E0101）物料衡算进出1.4.2.2换热器1-3换热器表1-4换热器（E0101）物料衡算进出流股编Temperature℃PressurebarVaporFracMoleFlowMassFlow100010Mass00006.143E-Mass6.143E-0000总00002.57E-4.408E-2.68E-2.57E-4.408E-2.68E-00001.4.2.3换热器1-4总00002.57E-4.408E-2.68E-2.57E-4.408E-2.68E-00001.4.2.3换热器1-4换热器表1-5换热器（E0102）物料衡算进流股编出1111℃PressurebarVaporFracMoleFlowMassFlowMass3.021E-Mass1.58E-2.92E-6.38E-3.021E-Mass1.58E-2.92E-6.38E-3.021E-总1.58E-2.92E-6.38E-1.4.2.4换热器1-5换热器表1-进出流股编出℃VaporFracMassFlowkg/hrVolumeFlowMassMassMassMass总1.4.2.5换热器1-6换热器表1-流股编出℃1010PressureVaporMoleFlowMassFlowkg/hr--MassMoleFlowMassFlowkg/hr--Mass00000000Mass0000总00001.4.2.6压缩机1-7压缩机表1-8压缩机（C0101）物料衡算表Pressure出1VaporFracMassFlowkg/hrVolumeFlow11MassVaporFracMassFlowkg/hrVolumeFlow11MassMass总1.4.2.7混合器1-8混合器1-9混合器（M0101）物料衡算进表进出流股编出Temperature℃PressurebarVaporFracMoleFlowMassFlowkg/hr10MassTemperature℃PressurebarVaporFracMoleFlowMassFlowkg/hr10Mass0000117.034E-5.03E-4.33E-13.0E-Mass总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）物料衡算进出Temperature℃PressurebarVaporFracMoleFlow进出Temperature℃PressurebarVaporFracMoleFlowMassFlowkg/hr11Mass000017.03E-5.03E-4.33E-6.89E-117.03E-5.03E-4.33E-Mass总00002.07E-3.52E-2.52E-2.17E-3.45E-1.68E-2.85E-2.04E-1.76E-1-10气体分离工1-11气体分离工段物料衡算表X进出出流股编VaporFracMoleFlowMassFlow1-10气体分离工1-11气体分离工段物料衡算表X进出出流股编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-总1.4.3.1换热器1-11换热器表1-进出流股编出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-总5.03E-4.33E-6.89E-Mass2.07E-3.52E-2.52E-2.17E-3.45E-5.03E-4.33E-6.89E-总2.07E-3.52E-2.52E-2.17E-3.45E-1.4.3.2换热器1-12换热器表1-13进出流股编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-总2.14E-2.14E-2.07E-3.52E-2.52E-2.17E-3.45E-1.4.3.3泵1-13泵1-表流股编出℃-0-0PressureVaporMoleFlowMassFlowkg/hrMassMoleFlowMassFlowkg/hrMass3.51E-3.51E-Mass4.68E-1.24E-总4.68E-1.24E-1.4.3.4混合器1-14混合器表1-15混合器（M0201）物料衡算进进出流股编出-℃VaporFracMoleFlowMassFlowkg/hr0VaporFracMoleFlowMassFlowkg/hr0Mass3.51E-0--Mass总4.6E-1.24E-1.4.3.5第一脱气塔1-第一脱气塔1-16第一脱气塔（T0201）物料衡算进表出流股编Temperature℃1-16第一脱气塔（T0201）物料衡算进表出流股编Temperature℃PressurebarVaporFracMoleFlowMassFlowkg/hrMass-11.41E-3.52E-7.997E-0-Mass总7.00E-6.54E-7.45E-1.743E-3.963E-1.4.3.6第二脱气塔1-16第二脱气塔表1-171.4.3.6第二脱气塔1-16第二脱气塔表1-17第二脱气塔物料衡进出流股编TemperatureVaporFracMassFlowkg/hrVolumeFlow-Mass-10-4.38E-1.91E-Mass1.164E-8.456E-2.15E-总3.6775E-1.4.3.7洗涤塔1-洗涤塔表1-18洗涤塔（T0207）物料总3.6775E-1.4.3.7洗涤塔1-洗涤塔表1-18洗涤塔（T0207）物料衡算进出流股编TemperatureVaporFracMassFlowkg/hrVolumeFlow0-110Mass00001.412E-3.51E-7.99E-Mass7.034E-5.03E-4.33E-6.89E-3.51E-0总0007.00E-6.543E-7.446E-1.743E-3.96E-2.077E-3.52E-2.52E-2.17E-3.45E-4.68E-1.247E-总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进进出出20-流股编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-总0000012.114E-Mass3.161E-6.665E-5.94E-4.31E-总0000012.114E-5.45E-4.150E-4.435E-2.783E-6.618E-1.4.4.1泵1-泵表1-进出流股编出0-0-℃VaporFracMassFlowkg/hrVolumeFlowMassMass总Mass总1.4.4.2换热器1-20换热器表1-进出流股编出0-Mass 20-℃VaporFracMoleFlowMassFlowkg/hrMassMass总1.4.4.3萃取塔1-21萃取塔表1-22萃取塔（T0301）物料衡算进出Temperature℃PressurebarVaporFracMoleFlowMassFlow0000VolumeFlow----Mass00000VolumeFlow----Mass000008.935E-1.884E-1.218E-Mass总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）物料衡算流股编进出℃VaporFracMoleFlowMassFlowkg/hr00002VaporFracMoleFlowMassFlowkg/hr00002Mass1.11E-1.196E-7.506E-2.609E-6.734E-Mass2.114E-5.45E-总4.150E-4.435E-2.783E-6.618E-1.4.5图1-23甲基丙烯酸甲酯合成工表1-24醋酸乙烯精制工段总物料衡进出流股编TemperaturePressureMoleFlowMassFlow00000--8.935E-MoleFlowMassFlow00000--8.935E-7.456E---Mass8.92E-1.88E-1.21E-6.14E-04.6448E-06.3577E-001.044E-Mass总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）物料衡算进进出流股编出Temperature℃PressurebarVaporFracMoleFlowMassFlowkg/hr0-Temperature℃PressurebarVaporFracMoleFlowMassFlowkg/hr0-0-Mass8.92E-Mass3.33E-6.32E-8.92E-总3.33E-6.32E-1.4.5.2混合器1-25混合器表1-26混合器（M0401）物料衡算进进出出Temperature℃PressurebarVaporFracMoleFlowMassFlowkg/hrTemperature℃PressurebarVaporFracMoleFlowMassFlowkg/hr0-Mass6.14E-0-8.92E-1.88E-1.21E-0-8.92E-Mass总2.57E-4.40E-2.68E-3.15E-6.669E-5.94E-4.31E-3.33E-6.32E-1.4.5.3脱乙醛塔图1-脱乙醛塔1-27脱乙醛塔（T0401）物料衡算进表出流股编1-27脱乙醛塔（T0401）物料衡算进表出流股编0-Mass0-0-℃VaporFracMoleFlowMassFlowkg/hr6.1E-Mass总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-总7.66E-1.4.5.5醋酸精制塔1-28醋酸精制塔总7.66E-1.4.5.5醋酸精制塔1-28醋酸精制塔表