05-附录05-附录2010版

镇海精炼25万吨/年环氧丙烷，8万吨/年异丙醇胺生产项目附录(同化技术-陕西鼓杯)第10届全国大学生化学设计竞赛镇海精炼25万吨/年环氧丙烷，8万吨/年异丙醇胺生产项目附录设计单位常州大学石油化工学院设计团队K.m成员名称张少波号润霞刘文豪康景阳优雅指导教师马建全高小新王俊子年杨德明2016年8月15日附录I物料平衡列表1.1物料平衡计算的第一部分1.1.1丙烷万亿分塔(T0101)表1.1丙烷粗塔进出口流量清单序号组件名称质量流kg/hr进料流动股票塔顶出料塔槽排放温度/c2026.167.7压力/条形101010气象分数1001丙烷6127061266.4903.5112丙烯531.058531.05803氢0004甲烷0.0040.00405乙烯0.1050.10506异丁烯6.95706.9577异丁烷1171.710.0031171.7078乙烷130.667130.66609水00010过氧化氢00011甲醇00012环氧丙烷00013氧气00014丙二醇甲醚00015氨00016异丙醇胺00017二异丙醇胺00018三异丙醇胺00019普罗维登斯000总计63110.50061928.3201182.175序号组件名称质量分数进料流动股票塔顶出料塔槽排放1丙烷0.9710.0030.9892丙烯0.00800.0083氢0004甲烷0005乙烯0006异丁烯00.00607异丁烷0.0190.99108乙烷0.00200.0029水00010过氧化氢00011甲醇00012环氧丙烷00013氧气00014丙二醇甲醚00015氨00016异丙醇胺00017二异丙醇胺00018三异丙醇胺00019普罗维登斯000总计1111.1.2 PDH反应器(R0101)表1.2 PDH反应器入口和出口流量列表序号组件名称质量流kg/hr进料流动股票径流周温度/c639464.2压力/条形43.1气象分数111丙烷710575.29053427.9402丙烯584.765171174.5603氢3247.0824066.8014甲烷0.0040.0255乙烯0.1050.1406异丁烯007异丁烷0.0760.0768乙烷130.670130.6719水0010过氧化氢0011甲醇0012环氧丙烷0013氧气0014丙二醇甲醚0015氨0016异丙醇胺0017二异丙醇胺0018三异丙醇胺0019普罗维登斯0.040257.816总计75038.04075038.040序号组件名称质量分数进料流动股票径流周1丙烷0.9470.7122丙烯0.0080.2283氢0.0430.0544甲烷005乙烯006异丁烯007异丁烷008乙烷0.00209水0010过氧化氢0011甲醇0012环氧丙烷0013氧气0014丙二醇甲醚0015氨0016异丙醇胺0017二异丙醇胺0018三异丙醇胺0019普罗维登斯00.006总计111.1.3 PDH反应器(R0102)表1.3 PDH反应器入口和出口流量列表序号组件名称质量流kg/hr进料流动股票径流周温度/c650467.1压力/条形3.12.5气象分数111丙烷53427.94035068.9902丙烯171174.5603422.2703氢4066.8014928.6854甲烷0.02490.0625乙烯0.1410.2056异丁烯007异丁烷0.0760.07608乙烷130.671130.6719水0010过氧化氢0011甲醇0012环氧丙烷0013氧气0014丙二醇甲醚0015氨0016异丙醇胺0017二异丙醇胺0018三异丙醇胺0019普罗维登斯257.816707.083总计75038.04075038.040序号组件名称质量分数进料流动股票流出附注11丙烷0.7120.4672丙烯0.2290.4563氢0.0540.0664甲烷005乙烯006异丁烯007异丁烷008乙烷0.0020.0029水0010过氧化氢0011甲醇0012环氧丙烷0013氧气0014丙二醇甲醚0015氨0016异丙醇胺0017二异丙醇胺0018三异丙醇胺0019普罗维登斯0.0030.009总计111.1.4 PDH反应器(R0103)表1.4 PDH反应器入口和出口流量列表序号组件名称质量流kg/hr进料流动股票径流周温度/c648543.7压力/条形2.51.9气象分数111丙烷35068.99024134.8602丙烯3422.27044525.5403氢4928.6855433.8534甲烷0.060.0775乙烯0.2050.2316异丁烯007异丁烷0.0760.0768乙烷130.671130.6729水0010过氧化氢0011甲醇0012环氧丙烷0013氧气0014丙二醇甲醚0015氨0016异丙醇胺0017二异丙醇胺0018三异丙醇胺0019普罗维登斯707.083812.719总计75038.04075038.040序号组件名称质量分数进料流动股票径流周1丙烷0.4670.3222丙烯0.4560.5933氢0.0660.07244甲烷005乙烯006异丁烯007异丁烷008乙烷0.0020.0029水0010过氧化氢0011甲醇0012环氧丙烷0013氧气0014丙二醇甲醚0015氨0016异丙醇胺0017二异丙醇胺0018三异丙醇胺0019普罗维登斯0.0090.011总计111.1.5 PDH反应器(R0104)表1.5 PDH反应器入口和出口流量列表序号组件名称质量流kg/hr进料流动股票径流周温度/c648502.9压力/条形1.91.4气象分数111丙烷24134.8609812.7402丙烯44525.54057478.2403氢5433.8536122.8104甲烷0.0770.1515乙烯0.2310.3586异丁烯007异丁烷0.0760.0768乙烷130.672130.6749水0010过氧化氢0011甲醇0012环氧丙烷0013氧气0014丙二醇甲醚0015氨0016异丙醇胺0017二异丙醇胺0018三异丙醇胺0019普罗维登斯812.7191492.99总计75038.0475038.04序号组件名称质量分数进料流动股票径流周1丙烷0.3220.1312丙烯0.5930.7663氢0.0720.0824甲烷005乙烯006异丁烯007异丁烷008乙烷0.0020.0029水0010过氧化氢0011甲醇0012环氧丙烷0013氧气0014丙二醇甲醚0015氨0016异丙醇胺0017二异丙醇胺0018三异丙醇胺0019普罗维登斯0.0110.020总计111.2第二部分物料平衡计算1.2.1变压吸附塔(T0201)表1.6变压吸附塔入口和出口流量列表序号组件名称质量流kg/hr进料流动股票塔顶出料塔槽排放温度/c404040压力/条形1.43233气象分数1111丙烷9812.7400.3109812.4292丙烯57478.24012.24557465.9903氢6122.8106122.7490.0614甲烷0.15100.1515乙烯0.35800.3586异丁烯0007异丁烷0.07600.0768乙烷130.6730.008130.6669水00010过氧化氢00011甲醇00012环氧丙烷00013氧气00014丙二醇甲醚00015氨00016异丙醇胺00017二异丙醇胺00018三异丙醇胺00019普罗维登斯1492.990.0091492.981总计75038.046135.32268902.72序号组件名称质量分数进料流动股票塔顶出料塔槽排放1丙烷0.13100.1422丙烯0.7660.0020.8343氢0.0820.99804甲烷0005乙烯0006异丁烯0007异丁烷0008乙烷0.00200.0029水00010过氧化氢00011甲醇00012环氧丙烷00013氧气00014丙二醇甲醚00015氨00016异丙醇胺