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29.51 KB (01-20) Simu1-1421764317.bkp (11)
105.78 KB (01-17) 共沸精馏过程模拟.bkp (115)
173.91 KB (01-16) 包例4-2苯塔设备计算.bkp (7)
82.35 KB (01-16) Simu1.bkp (19)
1.51 MB (01-15) AspenPlusUserModelsV7_3-Ref.pdf (70)
23.84 MB (01-14) 吴教授课件-1421196660.zip (186)
54.81 KB (01-13) Simulation 1-1421159159.bkp (16)
73.99 KB (01-13) Example12.2-3phases.bkp (7)
138.41 KB (01-13) Example13.3-IPAConv.bkp (6)
77.41 KB (01-12) 例13.3.bkp (1)
122.35 KB (01-12) 三相反应精馏.bkp (4)
26.42 KB (01-11) Simu1.bkp (19)
262.47 KB (01-07) 干气精制工段3接循环前.bkp (38)
101.55 KB (01-07) 干气精制工段3 - 接循环后.bkp (32)
205.61 KB (01-06) 2万方沼气-水洗-pall.bkp (46)
1.08 MB (01-04) 结晶器模拟-1420343041.apw (8)
16.67 MB (01-04) Aspen-dynamics-from-aspen-8.0.mkv (191)
682.15 KB (12-31) Aspen_Plus_Model_for_Moving_Bed_Coal_Gasifier.rar (146)
82.48 KB (12-30) kemea吸收CO2速率-1419922281.bkp (37)
246.56 KB (12-29) Solution11.1b-Crude.bkp (0)
23.58 KB (12-29) Solution11.1a-AssayData.bkp (0)
56.64 KB (12-29) 氨废水蒸氨-1419843655.bkp (11)
56.64 KB (12-29) 氨废水蒸氨.bkp (26)
32.04 KB (12-29) 习题12.1.bkp (8)
427.82 KB (12-28) sP e n Pl us 用户模型开发方法探讨.pdf (74)
726.02 KB (12-28) Aspen Plus 功能扩展方法探讨.pdf (87)
2.25 MB (12-28) 反应精馏塔用户模型开发.pdf (92)