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本帖最后由 banknation 于 2020-5-1 20:16 编辑

马友精馏塔报错的解决方法

- INFORMATION
  FLASH CALCULATIONS FAILED TO CONVERGE IN 30  ITERATIONS.  COMPOSITE FEED  FLASH FAILED TO CONVERGE; COLUMN CALCULATIONS CONTINUE.  IF CALCULATIONS  FAIL, SUPPLY T-EST AND OPTIONALLY BOTH X-EST AND Y-EST.
** ERROR
  RADFRAC NOT CONVERGED IN 200 OUTSIDE LOOP ITERATIONS.

提示：提供估算温度

解决方法：在收敛项中，设置第1块塔板（塔顶冷凝器）估算温度为52摄氏度
重置、运行


流程收敛，OK！
马友原文件已修改好：

大哥能给小弟分享一下你的汉化版的模拟软件吗？万分感谢

有偿也行啊，大哥

Aspen V11版本，去年春天发布的，会根据所安装的系统的语言区域自动转换为英语-汉语，安装包网上搜就可以找到

感谢感谢，已找到

-  INFORMATION
   COMPOSITE FEED FLASH FAILED TO CONVERGE; COLUMN CALCULATIONS CONTINUE.
   IF CALCULATIONS FAIL, SUPPLY T-EST AND OPTIONALLY BOTH X-EST AND Y-EST.

** ERROR
   RADFRAC NOT CONVERGED IN 200 OUTSIDE LOOP ITERATIONS.

***SEVERE ERROR
   MATERIAL AND ENERGY BALANCES FAILED TO CONVERGE: CHECK COL-SPECS
   OR SUPPLY BETTER TEMPERATURE AND COMPOSITION ESTIMATES.

***SEVERE ERROR
   THE FOLLOWING STAGES DRIED UP:
     1    2    3    4    7    8    9   10   21
   A LIMIT OF  0.10000E-04 * SUM OF FEEDS WAS IMPOSED ON THE FLOW RATES.

** ERROR
   BLOCK RADFRAC IS NOT IN MASS BALANCE:
   MASS INLET FLOW = 0.70833333E+01, MASS OUTLET FLOW = 0.12420751E+02
   RELATIVE DIFFERENCE = 0.75351773E+00