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『Aspen Plus交流』

92.33 KB (01-17) E01-20220116.bkp (9)
1.11 MB (01-17) E01-20220116.apw (8)
7.97 MB (01-15) Vapor-liquid Equilibria Using Unifac. A Group-Contribution Method by Aage Fredenslund Auth. z-lib.org.pdf (59)
9.54 MB (01-13) -1-马后炮化工.apwz (30)
997.65 KB (01-11) -1.apwz (10)
103.39 KB (01-10) 精馏模拟.bkp (14)
80.32 MB (01-06) 换热器工艺设计_孙兰义等主编_中国石化出版社2015.pdf (88)
806.41 KB (01-01) 流程模拟.apwz (12)
998.03 KB (12-29) 建模引用的原始论文.rar (97)
100 MB (12-29) Aspen HYSYS Video Training.rar (26)
1.58 MB (12-22) 用Aspen-plus模拟活性炭吸附床对苯酚的吸附.rar (33)
1.25 MB (12-14) 水的相图.rar (149)
619.5 KB (12-14) PITZ_3.bkp (49)
30.95 KB (12-13) Simulation 1.apwz (35)
75.69 KB (12-05) 碳（固体）与氧反应的设置（平衡反应器）.bkp (32)
312.1 KB (12-31) 基于COM技术的MATLAB与AspenPlus接口及高级应用.rar (85)
980.05 KB (11-24) 译AspenPlusUserModelsV11-Ref-马后炮化工.docx (139)
208.05 KB (11-19) Simulation 1.apwz (2)
49.68 KB (11-09) Example24.1-DATAFIT.bkp (35)
388.36 KB (11-07) EA2 （循环2）.bkp (6)
31.38 KB (11-04) mh2so4.bkp (17)
41.66 MB (11-04) Azeotropic_Data-III.pdf (21)
1.35 MB (11-04) aaa.apwz (4)
9.41 MB (11-02) 自动化指南GAMP5中文版.pdf (13)
824.52 KB (10-31) EA2.apwz (2)
62.57 KB (10-25) NACL-NA2SO4-H2O-ELECNRTL-1_90.bkp (7)
62.82 KB (10-24) NACL-NA2SO4-H2O-ELECNRTL-1_110.bkp (8)