jackzhong1080 发表于 2013-5-13 23:14:03

CSTR模拟结果出错。。。

用CSTR模拟气体在液相的反应，，结果有问题

Beginning Convergence Loop $OLVER01 Method: WEGSTEIN
Converging tear streams: CATARE

   Block: R-101    Model: RCSTR

   Block: R-102    Model: RCSTR

   Block: F-1      Model: FLASH2

   Block: F-2      Model: FLASH2
*   WARNING
      ZERO FEED TO THE BLOCK.BLOCK BYPASSED


> Loop $OLVER01 Method: WEGSTEIN   Iteration    1
Converging tear streams: CATARE
   2 vars not converged, Max Err/Tol-0.10000E+05

   Block: R-101    Model: RCSTR
      HENRY CONSTANT MODEL HENRY1 HAS MISSING PARAMETERS. PLEASE
      PROVIDE THE MISSING PARAMETERS FOR MAJOR SOLVENTS. THIS ERROR MAY OCCUR
      BECAUSE THE STREAM IS ALL VAPOR, BUT VLE CALCULATION IS REQUESTED.
      TRY SPECIFY VALID-PHASES=VAPOR-ONLY
      HENRY/1ST ELEMENT (DATA SET 1) MISSING FOR SUPERCRITICAL COMPONENT
      H2 WITH ALL SOLVENTS:
      PE

      CO WITH ALL SOLVENTS:
      PE

****PROPERTY PARAMETER ERROR
      ERRORS ENCOUNTERED IN CALCULATION OF LIQUID MIXTURE PROPS USING
      OPTION SET UNIQ-RK FOR PHIMX

! Calculations stopped because of missingproperty parameters

->By-passing economic evaluation because simulation case failed

<< Run Saved >>


ws1wqqqq 发表于 2013-5-13 23:14:03

抱歉，我不能帮助你了。

小柳 发表于 2013-5-13 23:14:03

你先翻译 翻译了内容再说
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