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『Aspen Plus交流』

497.48 KB (05-23) cooled turbine model-1.bkp (6)
853.93 KB (05-15) 5.12.bkp (1)
857.71 KB (05-14) 5.12.bkp (2)
599.73 KB (05-08) 050601-1557298854.bkp (8)
234.01 KB (05-08) 050601.bkp (9)
2.58 MB (05-07) 醋酸与水萃取塔xiugai.rar (17)
4.68 MB (05-07) Simulation 0423熊.apwz (2)
225.69 KB (05-06) 5-6EDA精馏-1557152281.bkp (1)
46.88 KB (05-06) 精馏模拟.bkp (2)
1.53 MB (05-05) 醋酸与水萃取塔-1557042531.zip (13)
23.57 KB (05-04) 精馏模拟1严格计算.his (2)
245 KB (05-01) 经济分析报告.xls (4)
329.95 KB (05-01) 经济分析.bkp (6)
184.32 KB (04-30) DMF-新工艺-ENRTL-RK.bkp (2)
40.71 KB (04-29) DMF-新工艺-ENRTL-RK.bkp (5)
85.83 KB (04-27) Simulation 2-1556364842.bkp (3)
2.16 MB (04-26) 丙烷脱氢2.apwz (5)
19.25 KB (04-25) 萃取精馏.bkp (7)
154.09 KB (04-25) 动力费托-1556163687.bkp (38)
11.73 KB (04-24) Cl2+NaCN.bkp (1)
30 MB (04-23) Distillation Design and Control Using Aspen Simulation 2nd.rar (28)
3.28 MB (04-22) 最终版产率反应反应器.apw (7)
284.3 KB (04-22) t1.apwz (1)
496.34 KB (04-21) 甲醇合成反应过程的模拟与优化_张秋利.caj (39)
4.2 MB (04-20) 最终版产率反应反应器.apw (7)
106.65 KB (04-17) 反应精馏塔.bkp (10)
419.99 KB (04-17) 吸收模拟.apwz (10)