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『Aspen Plus交流』

34.71 KB (02-07) Simulation 1.bkp (2)
3.41 MB (02-06) AspenEngineeringSuiteV7_2-Inst.pdf (4)
3.6 MB (02-06) AspenEngineeringSuiteV8_0-Inst.pdf (6)
4.39 MB (02-06) AspenEngineeringSuiteV8_4-Inst.pdf (5)
84.15 KB (02-06) LSERVRC_004_2139F.lic (1)
84.15 KB (02-06) LSERVRC_000_27B99.lic (1)
36.3 KB (02-04) Simu运用电解质向导做的一个混合模块出现错误控制面板上说是所有组分不挥发.bkp (2)
21.35 KB (02-03) eh2so4 为什么用平衡模块不可以-1422976587.bkp (4)
731.5 KB (02-03) 题目-1422976587.doc (9)
42.44 KB (02-03) 孙兰义教材60页有警报-1422959419.bkp (0)
23.5 KB (02-03) 设计规定不成立求助-1422959419.doc (0)
47.13 KB (02-03) Example2.1-Flowsheet.bkp (8)
33.76 KB (02-03) 习题3.1.bkp (60)
43.44 KB (02-02) 孙兰义教材60页有警报.bkp (1)
184.89 KB (02-02) 包例4-3苯塔再沸器设计计算---v8.0.bkp (4)
631.81 KB (02-02) AspenPlusElectrolytesV7_1-Start.pdf (11)
185.91 KB (02-01) 包例4-3苯塔再沸器设计计算.bkp (21)
114.87 KB (02-01) 模拟2.bkp (6)
49.78 KB (02-01) 例题2-5平衡模块修改---V8.6.bkp (8)
41.65 KB (01-31) 例题2-5设计规定做成功.bkp (10)
14.14 KB (01-31) 例题2-5平衡模块不成功.bkp (14)
55.6 KB (01-30) 甲苯萃取苯胺-1422540421-V8.6.bkp (19)
438.24 KB (01-29) 甲苯萃取苯胺-1422540421.apwz (26)
10.85 MB (01-23) AspenPlus软件在烟气脱硫系统中的应用.pdf (432)
41.99 KB (01-22) 油品分馏.bkp (21)
31.2 KB (01-21) C12H8O2S物性估算.bkp (2)
528 KB (01-21) C12H8O2S物性估算.apw (0)