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[ASPEN] 运算错误

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<< All Blocks Reinitialized >>


<< Run reinitialized 15:53:32 Sun Aug 5, 2018>>



->Processing input specifications ...

  *   WARNING IN THE "STREAM" PARAGRAPH WHICH BEGINS ON LINE 63
      STREAM NAME: AIRIN
      COMPONENT MASS FRACTIONS ARE NORMALIZED TO UNITY.

  Flowsheet Analysis :

Block $OLVER01 (Method: WEGSTEIN) has been defined to converge
         streams: Q3        9

COMPUTATION ORDER FOR THE FLOWSHEET:
$OLVER01 AIRHEAT CH4HEAT H2OHEAT MIXER PREFORM STACK COMB
|  HEATER2
(RETURN $OLVER01)

->Calculations begin ...


> Beginning Convergence Loop $OLVER01 Method: WEGSTEIN
  Converging tear streams: Q3        9

   Block: AIRHEAT  Model: HEATX
  *   WARNING
      AT LEAST ONE FEED HAS ZERO FLOW
      BLOCK BYPASSED


   Block: CH4HEAT  Model: HEATX
  *   WARNING
      AT LEAST ONE FEED HAS ZERO FLOW
      BLOCK BYPASSED


   Block: H2OHEAT  Model: HEATX
  *   WARNING
      AT LEAST ONE FEED HAS ZERO FLOW
      BLOCK BYPASSED


   Block: MIXER    Model: MIXER

   Block: PREFORM  Model: RGIBBS

   Block: STACK    Model: RGIBBS

   Block: COMB     Model: RSTOIC
  *   WARNING
      COMPONENT "OXYGE-01" HAS ZERO FLOWRATE IN THE OUTLET STREAM.
      FRACTIONAL CONVERSION HAS BEEN MODIFIED BY
      A FACTOR OF "0.3636957E-19"


   Block: HEATER2  Model: HEATER
  *** SEVERE ERROR
      FLASH RESULTS ARE WITHIN TOLERANCE, BUT MAY BE UNSATISFACTORY BECAUSE
      EXTRAPOLATED EOS VAPOR VOLUME ROOT WAS USED FOR PROPERTY CALCULATIONS.
      FAILURE TO SOLVE 2-PHASE ADIABATIC PROBLEM AS TP SUBPROBLEMS. T= 10.0000
      P= 1.0133D+05 HCALC= -6.8411D+07 HFSPEC= -9.3143D+07 PROBLEM OCCURRED
      WHILE FLASHING OUTLET STREAM.


> Loop $OLVER01 Method: WEGSTEIN     Iteration    1
  Converging tear streams: Q3        9
  *** SEVERE ERROR
      FLASH RESULTS ARE WITHIN TOLERANCE, BUT MAY BE UNSATISFACTORY BECAUSE
      EXTRAPOLATED EOS VAPOR VOLUME ROOT WAS USED FOR PROPERTY CALCULATIONS.
      FAILURE TO SOLVE 2-PHASE ADIABATIC PROBLEM AS TP SUBPROBLEMS. T= 10.0000
      P= 1.0133D+05 HCALC= -6.8411D+07 HFSPEC= -9.3143D+07 ERRORS OCCURRED IN
      FLASH CALCULATIONS FOR TEAR STREAM  9 .

   7 vars not converged, Max Err/Tol   0.10000E+07

   Block: AIRHEAT  Model: HEATX
  **  ERROR
      FLASH RESULTS ARE WITHIN TOLERANCE, BUT MAY BE UNSATISFACTORY BECAUSE
      EXTRAPOLATED EOS VAPOR VOLUME ROOT WAS USED FOR PROPERTY CALCULATIONS.
      FAILURE TO SOLVE 2-PHASE ADIABATIC PROBLEM AS TP SUBPROBLEMS. T= 10.0000
      P= 1.0133D+05 HCALC= -6.8411D+07 HFSPEC= -9.3143D+07 HOT FEED FLASH
      FAILED.

  **  ERROR
      "COLD" STREAM IS HOTTER THAN "HOT" STREAM
      BLOCK BYPASSED


   Block: CH4HEAT  Model: HEATX
  **  ERROR
      FLASH RESULTS ARE WITHIN TOLERANCE, BUT MAY BE UNSATISFACTORY BECAUSE
      EXTRAPOLATED EOS VAPOR VOLUME ROOT WAS USED FOR PROPERTY CALCULATIONS.
      FAILURE TO SOLVE 2-PHASE ADIABATIC PROBLEM AS TP SUBPROBLEMS. T= 10.0000
      P= 1.0133D+05 HCALC= -6.8411D+07 HFSPEC= -9.3143D+07 HOT FEED FLASH
      FAILED.

  **  ERROR
      "COLD" STREAM IS HOTTER THAN "HOT" STREAM
      BLOCK BYPASSED


   Block: H2OHEAT  Model: HEATX
  **  ERROR
      FLASH RESULTS ARE WITHIN TOLERANCE, BUT MAY BE UNSATISFACTORY BECAUSE
      EXTRAPOLATED EOS VAPOR VOLUME ROOT WAS USED FOR PROPERTY CALCULATIONS.
      FAILURE TO SOLVE 2-PHASE ADIABATIC PROBLEM AS TP SUBPROBLEMS. T= 10.0000
      P= 1.0133D+05 HCALC= -6.8411D+07 HFSPEC= -9.3143D+07 HOT FEED FLASH
      FAILED.

  **  ERROR
      "COLD" STREAM IS HOTTER THAN "HOT" STREAM
      BLOCK BYPASSED


   Block: MIXER    Model: MIXER

   Block: PREFORM  Model: RGIBBS

   Block: STACK    Model: RGIBBS

   Block: COMB     Model: RSTOIC
  *   WARNING
      COMPONENT "OXYGE-01" HAS ZERO FLOWRATE IN THE OUTLET STREAM.
      FRACTIONAL CONVERSION HAS BEEN MODIFIED BY
      A FACTOR OF "0.3636973E-19"


   Block: HEATER2  Model: HEATER
  *** SEVERE ERROR
      FLASH RESULTS ARE WITHIN TOLERANCE, BUT MAY BE UNSATISFACTORY BECAUSE
      EXTRAPOLATED EOS VAPOR VOLUME ROOT WAS USED FOR PROPERTY CALCULATIONS.
      FAILURE TO SOLVE 2-PHASE ADIABATIC PROBLEM AS TP SUBPROBLEMS. T= 10.0000
      P= 1.0133D+05 HCALC= -6.8411D+07 HFSPEC= -9.3143D+07 PROBLEM OCCURRED
      WHILE FLASHING OUTLET STREAM.


> Loop $OLVER01 Method: WEGSTEIN     Iteration    2
  Converging tear streams: Q3        9
# Converged              Max Err/Tol   0.26737E-08

->Generating block results ...

    Block: H2OHEAT  Model: HEATX
  **  ERROR WHILE GENERATING RESULTS FOR UNIT OPERATIONS BLOCK: "H2OHEAT"
      (MODEL: "HEATX")
      FLASH RESULTS ARE WITHIN TOLERANCE, BUT MAY BE UNSATISFACTORY BECAUSE
      EXTRAPOLATED EOS VAPOR VOLUME ROOT WAS USED FOR PROPERTY CALCULATIONS.
      FAILURE TO SOLVE 2-PHASE ADIABATIC PROBLEM AS TP SUBPROBLEMS. T= 10.0000
      P= 1.0133D+05 HCALC= -6.8411D+07 HFSPEC= -9.3143D+07 HOT FEED FLASH
      FAILED.

  **  ERROR WHILE GENERATING RESULTS FOR UNIT OPERATIONS BLOCK: "H2OHEAT"
      (MODEL: "HEATX")
      "COLD" STREAM IS HOTTER THAN "HOT" STREAM
      BLOCK BYPASSED


    Block: CH4HEAT  Model: HEATX
  **  ERROR WHILE GENERATING RESULTS FOR UNIT OPERATIONS BLOCK: "CH4HEAT"
      (MODEL: "HEATX")
      FLASH RESULTS ARE WITHIN TOLERANCE, BUT MAY BE UNSATISFACTORY BECAUSE
      EXTRAPOLATED EOS VAPOR VOLUME ROOT WAS USED FOR PROPERTY CALCULATIONS.
      FAILURE TO SOLVE 2-PHASE ADIABATIC PROBLEM AS TP SUBPROBLEMS. T= 10.0000
      P= 1.0133D+05 HCALC= -6.8411D+07 HFSPEC= -9.3143D+07 HOT FEED FLASH
      FAILED.

  **  ERROR WHILE GENERATING RESULTS FOR UNIT OPERATIONS BLOCK: "CH4HEAT"
      (MODEL: "HEATX")
      "COLD" STREAM IS HOTTER THAN "HOT" STREAM
      BLOCK BYPASSED


    Block: HEATER2  Model: HEATER

    Block: AIRHEAT  Model: HEATX
  **  ERROR WHILE GENERATING RESULTS FOR UNIT OPERATIONS BLOCK: "AIRHEAT"
      (MODEL: "HEATX")
      "COLD" STREAM IS HOTTER THAN "HOT" STREAM
      BLOCK BYPASSED


->Simulation calculations completed ...



  ***  Warning(s) were issued during Input Translation ***
  ***  Check the Run Status Results for more Information ***


               ***  Summary of Simulation Errors  ***

                   Physical
                   Property         System        Simulation
  Terminal Errors      0               0               0
    Severe Errors      0               0               3
           Errors      0               0              11
         Warnings      0               0               5

->Generating block results ...

    Block: H2OHEAT  Model: HEATX
  **  ERROR WHILE GENERATING RESULTS FOR UNIT OPERATIONS BLOCK: "H2OHEAT"
      (MODEL: "HEATX")
      FLASH RESULTS ARE WITHIN TOLERANCE, BUT MAY BE UNSATISFACTORY BECAUSE
      EXTRAPOLATED EOS VAPOR VOLUME ROOT WAS USED FOR PROPERTY CALCULATIONS.
      FAILURE TO SOLVE 2-PHASE ADIABATIC PROBLEM AS TP SUBPROBLEMS. T= 10.0000
      P= 1.0133D+05 HCALC= -6.8411D+07 HFSPEC= -9.3143D+07 HOT FEED FLASH
      FAILED.

  **  ERROR WHILE GENERATING RESULTS FOR UNIT OPERATIONS BLOCK: "H2OHEAT"
      (MODEL: "HEATX")
      "COLD" STREAM IS HOTTER THAN "HOT" STREAM
      BLOCK BYPASSED


    Block: CH4HEAT  Model: HEATX
  **  ERROR WHILE GENERATING RESULTS FOR UNIT OPERATIONS BLOCK: "CH4HEAT"
      (MODEL: "HEATX")
      "COLD" STREAM IS HOTTER THAN "HOT" STREAM
      BLOCK BYPASSED


    Block: AIRHEAT  Model: HEATX
  **  ERROR WHILE GENERATING RESULTS FOR UNIT OPERATIONS BLOCK: "AIRHEAT"
      (MODEL: "HEATX")
      "COLD" STREAM IS HOTTER THAN "HOT" STREAM
      BLOCK BYPASSED

  **  ERROR
      "COLD" STREAM IS HOTTER THAN "HOT" STREAM
      BLOCK BYPASSED

 

发表于 2018-8-5 15:58:13

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各位老铁看看为啥会这样。

 

发表于 2018-8-5 15:58:35

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