以梦为马,不负韶华

搜索
查看: 1804|回复: 0
收起左侧

求问各位大神,这个报错是啥意思

[复制链接]
回帖奖励 1 回复本帖可获得 1 奖励! 每人限 1 次
发表于 1970-1-1 08:00:00 显示全部楼层 |阅读模式
aspen求助
aspen版本: 7.3
求问各位大神,这个报错是啥意思



->Calculations begin ...


   Block: B7       Model: HEATX
  **  ERROR
      INVALID HOT STREAM TEMPERATURE SPECIFICATION
      T-SPEC =  3.4315000D+02 IS MORE THAN THIN =  3.3536437D+02


   Block: B14      Model: HEATER

   Block: B4       Model: MIXER

   Block: B5       Model: HEATER

   Block: B8       Model: VALVE

   Block: B9       Model: RADFRAC

       RateSep convergence iterations: B9
           Iter     Err/Tol
              0     0.36451E+19
  **  ERROR
      RATESEP CALCULATIONS FAILED TO CONVERGE
         ITERATIONS DIVERGE


  **  ERROR
      BLOCK B9 IS NOT IN MASS BALANCE:
      MASS INLET FLOW = 0.94080287E+02, MASS OUTLET FLOW = 0.53150598E+02
      RELATIVE DIFFERENCE = 0.77007013E+00


   Block: B10      Model: HEATER

   Block: B11      Model: FLASH2

   Block: B12      Model: HEATER

   Block: B13      Model: PUMP

> Beginning Convergence Loop $OLVER01 Method: WEGSTEIN

   Block: B3       Model: RADFRAC

       Convergence iterations:
         OL   ML   IL     Err/Tol
          1    1    1     0.47816E-03

   Block: B6       Model: HEATER

   Block: B7       Model: HEATX
  **  ERROR
      INVALID HOT STREAM TEMPERATURE SPECIFICATION
      T-SPEC =  3.4315000D+02 IS MORE THAN THIN =  3.3536437D+02


   Block: B14      Model: HEATER

   Block: B4       Model: MIXER

   Block: B5       Model: HEATER

   Block: B8       Model: VALVE

   Block: B9       Model: RADFRAC

       RateSep convergence iterations: B9
           Iter     Err/Tol
              0     0.36451E+19
  **  ERROR
      RATESEP CALCULATIONS FAILED TO CONVERGE
         ITERATIONS DIVERGE


  **  ERROR
      BLOCK B9 IS NOT IN MASS BALANCE:
      MASS INLET FLOW = 0.94080295E+02, MASS OUTLET FLOW = 0.53150598E+02
      RELATIVE DIFFERENCE = 0.77007030E+00


   Block: B10      Model: HEATER

   Block: B11      Model: FLASH2

   Block: B12      Model: HEATER

   Block: B13      Model: PUMP

> Loop $OLVER01 Method: WEGSTEIN     Iteration    1
# Converged              Max Err/Tol  -0.58409E-08

->Generating block results ...

    Block: B7       Model: HEATX
  *   WARNING WHILE GENERATING RESULTS FOR UNIT OPERATIONS BLOCK: "B7" (MODEL:
      "HEATX")
      CALCULATED FEED TEMPERATURE FOR THE HOT SIDE (3.3544573D+02)
      IS INCONSISTENT WITH ITS INLET STREAM VALUE (3.3501118D+02)
      PROBABLE CAUSE: LOOSE FLASH TOLERANCE, OR UPSTREAM BLOCK WITH DIFFERENT
      NPHASE OR PROP SET. THE CALCULATED VALUE WILL BE USED IN CALCULATIONS

  **  ERROR WHILE GENERATING RESULTS FOR UNIT OPERATIONS BLOCK: "B7" (MODEL:
      "HEATX")
      INVALID HOT STREAM TEMPERATURE SPECIFICATION
      T-SPEC =  3.4315000D+02 IS MORE THAN THIN =  3.3544573D+02


    Block: B13      Model: PUMP
      INFORMATION WHILE GENERATING RESULTS FOR UNIT OPERATIONS BLOCK: "B13"
      (MODEL: "PUMP")
      NET POSITIVE SUCTION HEAD IS LESS THAN ZERO


->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               0
           Errors      0               0              13
         Warnings      0               0               2


不想打字就选择快捷回复吧
您需要登录后才可以回帖 登录 | 注册

本版积分规则

手机版|以梦为马,不负韶华

GMT+8, 2025-3-7 01:23

Powered by 以梦为马,不负韶华

© 2024-2099 Meng.Horse

快速回复 返回顶部 返回列表