aspen培训bkp文件例题

1、例题A1:酸气碱洗塔输入数据如下FGASPGASNAOH1Temperature C 504040Pressure kPa 131.398.325591.7Vapor Frac 110Mole Flow kmol/hr 11.933495.5168Mass Flow kg/hr 420.7993323400Mass Flow kg/hr H2O 9.4932706.42720 CO2 144.944.1790 H2S 202.3143.550 O2 16.86224410 N2 44.29737450 AR 2.789252.390 NAOH 00680例题A2:间歇精馏进料组成如下1Temp

2、erature C 40Pressure kg/sqcm 5Mass Flow kg/hr 5000Volume Flow cum/hr 5.424Mass Frac H2O 0.04 ISOBU-01 0.95 TERT-01 0.01理论板35塔顶压力kg/cm20.1全塔压降kg/cm20.1冷凝器滞液量m30.3其它塔板m30.006进料量kg5000操作工况一塔顶馏出产品500kg/h回流比1.2操作工况二塔顶馏出产品400kg/h回流比1.5热力学NRTL-RK操作参数如下例题A3:萃取精馏101102Temperature C 5040Pressure kg/sqcm 85Mol

3、e Flow kmol/hr 17.246147.753Mass Flow kg/hr 120010800Mass Flow kg/hr 3-MEC4= 3-METHYL-1-BUTENEC5H10-718.4080 IC5 2-METHYL-BUTANEC5H12-265.2680 C5X 1,4-PENTADIENEC5H8-43.7920 2-MEC4= 2-METHYL-1-BUTENEC5H10-551.1680 NC50 N-PENTANEC5H12-179.1160 C5=1 1-PENTENEC5H10-2205.560 IC5= 2-METHYL-1,3-BUTADIENEC

4、5H8-6443.1360 TC5=2 TRANS-2-PENTENEC5H10-445.060 CC5=2 CIS-2-PENTENEC5H10-325.8480 2-MET-2 2-METHYL-2-BUTENEC5H10-644.8440 PD-1 1-TRANS-3-PENTADIENEC5H8-3117.7920 PD-2 CIS-1,3-PENTADIENEC5H835.40 CPD CYCLOPENTADIENEC5H618.9120 CYC5= CYCLOPENTENEC5H8-124.9240 CYC50 CYCLOPENTANEC5H10-16.1080 DCPD DICY

5、CLOPENTADIENEC10H12-D03.7080 C9X INDENEC9H810.9560 DMF N,N-DIMETHYLFORMAMIDEC3H7NO010800进料参数理论板98冷凝器压力kg/cm22.5塔顶压力kg/cm22.6全塔压降kg/cm21.0进料板5/49回流比4.5塔顶馏出量kg/h170热力学UNIFAC操作参数如下例题A4:共沸脱水317Temperature C 25Pressure kg/sqcm 5Vapor Frac 0Mole Flow kmol/hr 263.894Mass Flow kg/hr 14252Mass Flow kg/hr H2O 14.252 AIR 0 1-BUT-01 2.85 TRANS-01 14.252 CIS-2-01 18.528 1,3-B-01 14194.992 2,2-D-01 0 2-MET-03 0 3-MET-01 0 N-HEX-01 0 TBC 7.126 ETHYL-01 0进料组成如