異丙醇生產(chǎn)工藝研究的物料衡算與熱量衡算計(jì)算案例目錄TOC\o"1-3"\h\u31096異丙醇生產(chǎn)工藝研究的物料衡算與熱量衡算計(jì)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熱量衡算 6281771.2.1第一工段熱量衡算 6153601.2.1.1丙烷脫氫反應(yīng)器（R0101） 6296031.2.2第二工段熱量衡算 81.1物料衡算1.1.1第一工段物料衡算1.1.1.1反應(yīng)器（R0101）表5-1進(jìn)出物料衡算表序號(hào)組分名稱質(zhì)量流量kg/h百分含量進(jìn)料出料進(jìn)料出料溫度°C2065020650壓力bar110110氣相分率0.763610.763611C3H8832014370.2360.33042H20403.63400.29253C3H606479.36600.37674N200005O200006H2O133313330.00040.00047C3H8O0000總量965396531.0001.0001.1.1.2脫水塔（T0101）表5-2脫水塔進(jìn)出物料衡算表序號(hào)組分名稱質(zhì)量流量kg/h百分含量進(jìn)料1出料1出料2進(jìn)料1出料1出料2溫度°C202020202020壓力bar1121211212氣相分率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總量96538341.6526837.346591.00001.00001.00001.1.1.3冷凝塔(T0102)表5-3冷凝塔進(jìn)出物料衡算表序號(hào)組分名稱質(zhì)量流量kg/h百分含量進(jìn)料出料1出料2進(jìn)料出料1出料2溫度°C-70-70-70-70-70-70壓力bar121212121212氣相分率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總量10399.241624992.692710171.73391.0001.0001.0001.1.1.4精餾塔（T0104）表5-4精餾塔進(jìn)出物料衡算表序號(hào)組分名稱質(zhì)量流量kg/h百分含量進(jìn)料出料1出料2進(jìn)料出料1出料2溫度°C-7019.075333.9517-7019.075333.9517壓力bar121012121012氣相分率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總量9620.873888148.3993411.824541.0001.0001.0001.1.2第二工段物料衡算1.1.2.1水合反應(yīng)器（R0201）表5-5水合反應(yīng)器進(jìn)出物料衡算表序號(hào)組分名稱質(zhì)量流量kg/h百分含量進(jìn)料出料1進(jìn)料出料1溫度°C2519025190壓力bar1.072.01.072.0氣相分率0.57660.67330.57660.67331C3H849.541949.54190.00060.00072H28.17088.17080.00040.00033C3H610223.21717409.86380.51630.04214N200005O200006H2O03163.863600.20747C3H8O05623.185900.6688總量17480.929817480.92981.0001.0001.1.2.2丙烯精餾塔(T0201)表5-6精餾塔進(jìn)出物料衡算表序號(hào)組分名稱質(zhì)量流量kg/h百分含量進(jìn)料出料1出料2進(jìn)料出料1出料2溫度°C603030603030壓力bar111111氣相分率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總量111398.07242612.52275481.1411.0001.0001.0001.1.2.3異丙醇精餾塔(T0205)表5-7精餾塔進(jìn)出物料衡算表序號(hào)組分名稱質(zhì)量流量kg/h百分含量進(jìn)料出料1出料2進(jìn)料出料1出料2溫度°C2021.316081.45332011.534481.0410壓力bar179179氣相分率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總量9054.49887731．13278906.21911.0001.0001.0001.2熱量衡算1.2.1第一工段熱量衡算1.2.1.1丙烷脫氫反應(yīng)器（R0101）表5-8進(jìn)出物料焓值表項(xiàng)目進(jìn)料出料溫度°C20650壓力bar110質(zhì)量流量kg/h96539653焓值Gcal/hr-12.34211.5153ΣHGcal/hr-12.34211.51531.2.1.2丙烯脫水塔（T0101）表5-9進(jìn)出物料焓值表項(xiàng)目進(jìn)料出料1出料2溫度°C202020壓力bar11212氣相分率0.860610質(zhì)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進(jìn)出物料焓值表項(xiàng)目進(jìn)料出料1出料2溫度°C-70-70-70壓力bar121212質(zhì)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丙烯精餾塔（T0104）表5-11進(jìn)出物料焓值表項(xiàng)目進(jìn)料出料1出料2溫度°C-7019.075333.9517壓力bar121012質(zhì)量流量kg/h9620.873888148.3993411.82454焓值Gcal/hr-4.69513.3631-3.3541ΣHGcal/hr-4.6951-0.3101.2.2第二工段熱量衡算1.2.2.1異丙醇反應(yīng)器（R0201）表5-12進(jìn)出物料焓值表項(xiàng)目進(jìn)料出料1溫度°C25190壓力bar1.072.0質(zhì)量流量kg/h15249.45515249.455焓值Gcal/hr-12.3110-21.1418ΣHGc