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230.96 KB (10-30) zheda-02-wuxing.bkp (3)
27.14 KB (10-28) 石油蒸馏3.bkp (18)
93.92 KB (10-28) 天然气.bkp (7)
251.43 KB (10-27) 1000.bkp (3)
2.02 MB (10-26) 初始数据3(反应精馏）-1445852665.apw (12)
1.88 MB (10-26) 初始数据3(反应精馏）.apw (9)
218.55 KB (10-26) 精馏塔.HSC (9)
416.08 KB (10-26) Simu1$backup-1445834605.bkp (18)
729.35 KB (10-26) 只加乙二醇版.zip (12)
107.79 KB (10-26) Simu1$backup.bkp (14)
220.38 KB (10-21) Simee.bkp (2)
80.47 KB (10-21) 例题2.12问题.bkp (11)
126.27 KB (10-20) example2.16-1445315958.bkp (0)
126.27 KB (10-20) example2.16.bkp (0)
41.09 KB (10-20) 2-5.bkp (13)
7.04 MB (10-19) 基于AspenPlus的氯乙烯精馏过程模拟_周文军.caj (12)
220.38 KB (10-19) Simee.bkp (17)
108.01 KB (10-17) Simu2.bkp (31)
100.4 KB (10-17) 1.bkp (22)
163.56 KB (10-16) 吸收单元kemdea.bkp (15)
15.73 MB (10-16) 《化工过程分析与综合》鄢烈祥化学工业出版社2010[1].3.pdf (240)
17.24 KB (10-15) Comsol51_3.torrent (50)
347.87 KB (10-10) 甲烷化.apwz (32)
41.86 KB (10-10) Simu1.bkp (5)
239.58 KB (10-10) 08_AcidGasSweeteningWithDEA.pdf (3)
201.29 KB (10-10) 06_GasGathering.pdf (2)
199.98 KB (10-09) 09_NaturalGasDehydrationWithTEG.pdf (7)

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