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『Aspen Plus交流』

879.5 KB (05-10) 热泵-1462786003[1]001.apw (9)
1.85 MB (05-09) AspenPlusSolidsV8_2-Start.pdf (8)
139.6 KB (05-09) RE B 精馏.bkp (9)
25.01 KB (05-09) 热泵-1462786003.bkp (22)
104.58 KB (05-09) Simu13.3异丙醇共沸精馏.bkp (6)
49.65 KB (05-08) 分解煤.bkp (6)
180.41 KB (05-08) 作品2.bkp (10)
52.24 KB (05-07) SHT 0553-1993工业丙烷、丁烷.rar (44)
538.39 KB (05-07) HG 20559.2-1993 管道仪表流程图设备图形符号.pdf (42)
191.8 KB (05-06) 4乙腈精制工段 - 副本 (3).bkp (12)
32.04 KB (05-06) 新建文件夹.rar (11)
201.46 KB (05-06) UNNAMED$backup.bkp (8)
744.37 KB (05-05) 先脱丙烷流程灵敏度分析2.bkp (16)
30.43 MB (05-05) 能量的有效利用：夹点分析与过程集成原著第二版.rar (1)
308.99 KB (05-05) Simu1-1462451004.bkp (4)
31.47 MB (05-04) 能量的有效利用：夹点分析与过程集成原着....pdf (710)
476.78 KB (05-03) CO2.bkp (13)
37.62 KB (05-03) 异丙醇和水共沸精馏粗算.bkp (42)
448 KB (05-02) 5.apw (51)
661.97 KB (05-02) 先脱丙烷流程灵敏度分析2.bkp (21)
105.68 KB (05-02) propane-dehy-reactor-1462177208.bkp (35)
1.85 MB (05-02) Kinetic-model-and-Simulation-Analysis-for-Propane-Dehydrogenation-in-an-Industrial-Moving-Bed-Reactor.pdf (20)
504.63 KB (05-02) 萃取精馏塔 - 副本 (6)JIA1 - 副本 - 副本$backup-1462156836.bkp (12)
453.26 KB (05-01) 1.pdf (10)
87.69 KB (05-01) 氨气不能被吸收.bkp (42)
1.14 MB (04-30) 脱硫反应精馏.apw (2)
180.89 KB (04-29) D8.4.29mahoushang - 副本.bkp (106)