搜索附件  

M-102 result2x-1460639712.bkp

 

aspen设计萃取精馏塔系统补充萃取剂量无法计算:
萃取精馏塔T-102错误如下***SEVERE ERROR
   THE FOLLOWING STAGES DRIED UP (VAPOR OR LIQUID FLOW APPROACHES 0):
    85
   A LIMIT OF  0.10000E-04 * SUM OF FEEDS WAS IMPOSED ON THE FLOW RATES
   OR A LIMIT OF  0.10000E-04 WAS IMPOSED ON THE STAGE V/L OR L/V RATIO.

溶剂解吸塔T-103错误如下


***SEVERE ERROR
   COMPONENT BALANCE EQUATION FAILED TO CONVERGE.

***SEVERE ERROR
   THE FOLLOWING STAGES DRIED UP (VAPOR OR LIQUID FLOW APPROACHES 0):
     7    8    9
   A LIMIT OF  0.10000E-04 * SUM OF FEEDS WAS IMPOSED ON THE FLOW RATES
   OR A LIMIT OF  0.10000E-04 WAS IMPOSED ON THE STAGE V/L OR L/V RATIO.

** ERROR
   BLOCK T-103 IS NOT IN MASS BALANCE:
   MASS INLET FLOW = 0.15998998E+02, MASS OUTLET FLOW = 0.15241218E+02
   RELATIVE DIFFERENCE = 0.49719096E-01


dried up,我也是同样的问题,干板
大神,aspen软件怎么下载能不能分享下。
梦马论坛-以梦为马,不负韶华

化工人的交流乐园

联系我们

  • 投诉建议 相关侵权、举报、投诉及建议等,请发 E-mail:admin@meng.horse
返回顶部