【《异丙醇生产工艺研究的物料衡算与热量衡算计算案例》1400字】

异丙醇生产工艺研究的物料衡算与热量衡算计算案例目录TOC\o"1-3"\h\u31096异丙醇生产工艺研究的物料衡算与热量衡算计算案例 1251161.1物料衡算 186831.1.1第一工段物料衡算 131931.1.2第二工段物料衡算 4187631.2热量衡算 6281771.2.1第一工段热量衡算 6153601.2.1.1丙烷脱氢反应器（R0101） 6296031.2.2第二工段热量衡算 81.1物料衡算1.1.1第一工段物料衡算1.1.1.1反应器（R0101）表5-1进出物料衡算表序号组分名称质量流量kg/h百分含量进料出料进料出料温度°C2065020650压力bar110110气相分率0.763610.763611C3H8832014370.2360.33042H20403.63400.29253C3H606479.36600.37674N200005O200006H2O133313330.00040.00047C3H8O0000总量965396531.0001.0001.1.1.2脱水塔（T0101）表5-2脱水塔进出物料衡算表序号组分名称质量流量kg/h百分含量进料1出料1出料2进料1出料1出料2温度°C202020202020压力bar1121211212气相分率0.8606100.8606101C3H814371137.16450.00450.03410.04941.4224e-072H21513.6293341.18490.000090.02570.02968.6342e-083C3H65369.37076801.4550.01310.72530.91953.6783e-064N20000005O20000006H2O133353.8482837.32890.21490.001418010.99997C3H8O000000总量96538341.6526837.346591.00001.00001.00001.1.1.3冷凝塔(T0102)表5-3冷凝塔进出物料衡算表序号组分名称质量流量kg/h百分含量进料出料1出料2进料出料1出料2温度°C-70-70-70-70-70-70压力bar121212121212气相分率0.6439100.5319101C3H81437.3331247.76641697.13080.24910.04960.12602H2403.63437583.65712.77090.03930.50440.00023C3H68493.643134361.29258450.03810.70950.44580.85414N20000005O20000006H2O64.63100.016321.79410.00141.4643e-050.001524627C3H8O000000总量10399.241624992.692710171.73391.0001.0001.0001.1.1.4精馏塔（T0104）表5-4精馏塔进出物料衡算表序号组分名称质量流量kg/h百分含量进料出料1出料2进料出料1出料2温度°C-7019.075333.9517-7019.075333.9517压力bar121012121012气相分率0100101C3H81401.0988852.69122716.42810.13600.00170.88622H24.39014.39012.027e-120.00010.00023.443e-163C3H68196.815708091.31770324.66130.75210.99790.10444N20000005O20000006H2O14.5692014.56920.001500.00927C3H8O000000总量9620.873888148.3993411.824541.0001.0001.0001.1.2第二工段物料衡算1.1.2.1水合反应器（R0201）表5-5水合反应器进出物料衡算表序号组分名称质量流量kg/h百分含量进料出料1进料出料1温度°C2519025190压力bar1.072.01.072.0气相分率0.57660.67330.57660.67331C3H849.541949.54190.00060.00072H28.17088.17080.00040.00033C3H610223.21717409.86380.51630.04214N200005O200006H2O03163.863600.20747C3H8O05623.185900.6688总量17480.929817480.92981.0001.0001.1.2.2丙烯精馏塔(T0201)表5-6精馏塔进出物料衡算表序号组分名称质量流量kg/h百分含量进料出料1出料2进料出料1出料2温度°C603030603030压力bar111111气相分率0.4322100.4322101C3H847.311247.31123.1488e-060.00080.01020.00022H28.45018.45011.2198e-060.00020.00271.9949e-073C3H6813.8639813.86390.00040.04810.60130.02404N20000005O20000006H2O439.482691.07113610.44340.20710.03940.38817C3H8O8617.31551649.04850.31130.56180.51160.5616总量111398.07242612.52275481.1411.0001.0001.0001.1.2.3异丙醇精馏塔(T0205)表5-7精馏塔进出物料衡算表序号组分名称质量流量kg/h百分含量进料出料1出料2进料出料1出料2温度°C2021.316081.45332011.534481.0410压力bar179179气相分率1101101C3H829.496229.19970.09280.01910.03174.3442e-052H27.37198.47193.2763e-130.00380.00513.002e-163C3H6781.8631781.45111.90910.40010.87110.00104N20000005O20000006H2O81.0652081.06520.024400.06127C3H8O8151.06156912.0017901.82940.48910.00090.9445总量9054.49887731．13278906.21911.0001.0001.0001.2热量衡算1.2.1第一工段热量衡算1.2.1.1丙烷脱氢反应器（R0101）表5-8进出物料焓值表项目进料出料温度°C20650压力bar110质量流量kg/h96539653焓值Gcal/hr-12.34211.5153ΣHGcal/hr-12.34211.51531.2.1.2丙烯脱水塔（T0101）表5-9进出物料焓值表项目进料出料1出料2温度°C202020压力bar11212气相分率0.860610质量流量kg/hr96538341.6526837.34659焓值Gcal/hr-6.21710.1431-6.8901ΣHGcal/hr-6.2171-6.89011.2.1.3丙烯冷凝塔(T0102)表5-10进出物料焓值表项目进料出料1出料2温度°C-70-70-70压力bar121212质量流量kg/h10399.241624992.692710171.7339焓值Gcal/hr-1.3812-0.4854-4.8716ΣHGcal/hr-1.3812-1.38121.2.1.4丙烯精馏塔（T0104）表5-11进出物料焓值表项目进料出料1出料2温度°C-7019.075333.9517压力bar121012质量流量kg/h9620.873888148.3993411.82454焓值Gcal/hr-4.69513.3631-3.3541ΣHGcal/hr-4.6951-0.3101.2.2第二工段热量衡算1.2.2.1异丙醇反应器（R0201）表5-12进出物料焓值表项目进料出料1温度°C25190压力bar1.072.0质量流量kg/h15249.45515249.455焓值Gcal/hr-12.3110-21.1418ΣHGc