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『Aspen HYSYS交流』

337.55 KB (03-11) Comparing Pressure Flow Solvers for Dynamic Process Simulation.pdf (35)
519.5 KB (03-04) LPG脱乙烷不收敛-1457079230.hsc (21)
2.39 MB (02-05) TEG脱水-1453893984.xml (48)
283.63 KB (01-30) 溶剂法脱除天然气中有机硫的原理及发展趋势-1454134024.pdf (15)
850.3 KB (01-29) 多元精馏体系仿真中的问题及对策.pdf (33)
574.33 KB (01-29) Dynamic Simulation of Tank in HYSYS.pdf (299)
548.15 KB (01-27) TEG脱水-1453893984.hsc (29)
548.15 KB (01-27) TEG脱水.hsc (19)
374.99 KB (01-27) 虚拟导热油+DOW导热油环戊烷流程.hsc (3)
7.05 MB (01-25) Task 3b Final.zip (6)
8.48 MB (01-25) Task 2 Final.zip (6)
7.36 MB (01-25) Task 1 Final.zip (7)
156.95 KB (01-23) LNG-test.hsc (1)
4.87 MB (01-17) DYN COMPRESSOR MODEL SAMPLE.xml (7)
491.78 KB (01-13) DYN COMPRESSOR MODEL SAMPLE.zip (11)
22.15 KB (12-22) rundll32.zip (28)
2.37 MB (12-18) 教你成功安装Aspen HYSYS V7.2的步骤.pdf (25)
1.08 MB (12-13) 三种气液混输软件的模拟计算与分析.pdf (363)
7.21 MB (12-08) HYSYS基础.ppt (195)
2.29 MB (11-26) 3.XML (78)
551.6 KB (11-26) 3.HSC (62)
1.34 MB (11-24) 常减压.hsc (8)
313.21 KB (11-18) try_edr-1447831856.hsc (3)
1.21 MB (11-06) 通用Gibbs反应器的机理建模和求解方法_郑小青.pdf (144)
3.35 MB (11-05) 当今国际市场商品化流程模拟类软件分类及性能分析.pdf (237)
218.55 KB (10-26) 精馏塔.HSC (9)
239.58 KB (10-10) 08_AcidGasSweeteningWithDEA.pdf (3)