马友 (自己机器报错,别的机器不报错) 精馏塔报错的解决方法
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 30ITERATIONS.COMPOSITE FEEDFLASH FAILED TO CONVERGE; COLUMN CALCULATIONS CONTINUE.IF CALCULATIONSFAIL, 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 17695677627 发表于 2020-8-21 16:03
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 17695677627 发表于 2020-8-21 16:11
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
liu_jia_tao 发表于 2020-8-21 16:27
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 ...
感谢感谢,已找到{:543:} 我这还是没解决 -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 OF0.10000E-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
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