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943.19 KB (11-30) Hualu.bkp (147)
775.54 KB (11-29) 正丁烷两步法脱氢制丁二烯.bkp (17)
120.99 KB (11-29) 炼厂气MDEA脱硫系统模拟与优化.bkp (22)
28.51 KB (11-27) Simulation 5.bkp (7)
185.37 KB (11-25) 乙二醇.apwz (0)
31.84 KB (11-23) 丁醇和水分离.prz (10)
31.84 KB (11-23) 丁醇和水分离-1526717129.prz (3)
36.34 KB (11-19) Simulation 2.bkp (5)
36.34 KB (11-19) Simulation 2.bkp (0)
1.83 MB (11-18) Simulation 1.apwz (0)
5.17 MB (11-11) 234889424-Pressure-Relief-Dynamics-Aspen-Plus.pdf (20)
332.47 KB (11-09) 发生器.edr (0)
746.21 KB (11-07) keamp111.apwz (3)
32.28 KB (11-07) Exercise3-1.bkp (2)
594.01 KB (11-03) 改变SP值曲线没变化.docx (3)
684 KB (11-03) [muchong.com]制冷机新.apw (1)
746.21 KB (11-01) keamp111.apwz (5)
8.68 KB (11-01) USRPRES.f (100)
20.91 KB (11-01) USRKIN.f (142)
8.62 KB (10-31) 1-9.bkp (1)
224.02 KB (10-29) 设计.bkp (2)
588.32 KB (10-28) 环己烷流程模拟.apwz (6)
314.08 KB (10-28) 新建文件夹.rar (15)
13.34 KB (10-28) USRKIN.f (135)
1.49 MB (10-26) PROII培训讲义之软件入门.pdf (73)
432.27 KB (10-23) 图片.rar (1)
736.39 KB (10-22) keamp11.apwz (7)

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