循环过程求助

，，， · 发表于 1970-1-1 08:00:00

加循环时会迭代时会有些错误但不影响流程收敛，请问有影响吗？

<< Run reinitialized 20:35:20 Sat May 28, 2016>>

->Processing input specifications ...

  Flowsheet Analysis :

Block $OLVER01 (Method: BROYDEN ) has been defined to converge
      streams: 1108    1208    302    408    415
            R1       R2

COMPUTATION ORDER FOR THE FLOWSHEET:
H101 V101 F101
$OLVER01 M2101 E1201 H1201 V1201 R1201 E1202 C1201 M1101
|  E1101 M101 E102 E103 E104 C201 F301 F302 M301 E401 T401
|  T402 V401 E402 FS401 P401 C401 F401 P403 FS402 E403 V402
|  FS403 H1101 V1101 R1101 E1102 C1101
(RETURN $OLVER01)
P402 S301 M302

->Calculations begin ...

Block: H101    Model: HEATER

Block: V101    Model: VALVE

Block: F101    Model: FSPLIT

> Beginning Convergence Loop $OLVER01 Method: BROYDEN
  Converging tear streams: 1108    1208    302    408
                        415    R1       R2

Block: M2101 Model: MIXER

Block: E1201 Model: HEATX
  * WARNING
   AT LEAST ONE FEED HAS ZERO FLOW
   BLOCK BYPASSED

Block: H1201 Model: HEATER

Block: V1201 Model: VALVE

Block: R1201 Model: RPLUG

Block: E1202 Model: HEATER

Block: C1201 Model: COMPR

Block: M1101 Model: MIXER

Block: E1101 Model: HEATX
  * WARNING
   AT LEAST ONE FEED HAS ZERO FLOW
   BLOCK BYPASSED

Block: M101    Model: MIXER
  * WARNING
   ZERO FEED TO BLOCK.

Block: E102    Model: HEATER
  * WARNING
   ZERO FEED TO THE BLOCK.  BLOCK BYPASSED

Block: E103    Model: HEATER
  * WARNING
   ZERO FEED TO THE BLOCK.  BLOCK BYPASSED

Block: E104    Model: HEATX
  * WARNING
   AT LEAST ONE FEED HAS ZERO FLOW
   BLOCK BYPASSED

Block: C201    Model: MCOMPR
  * WARNING
   ZERO FEED TO THE BLOCK. BLOCK IS BYPASSED

Block: F301    Model: FLASH2
  * WARNING
   ZERO FEED TO THE BLOCK.  BLOCK BYPASSED

Block: F302    Model: FLASH2
  * WARNING
   ZERO FEED TO THE BLOCK.  BLOCK BYPASSED

Block: M301    Model: MIXER
  * WARNING
   ZERO FEED TO BLOCK.

Block: E401    Model: HEATER
  * WARNING
   ZERO FEED TO THE BLOCK.  BLOCK BYPASSED

Block: T401    Model: RADFRAC
  * WARNING
   ZERO FEED - BLOCK BYPASSED.

Block: T402    Model: RADFRAC

   Convergence iterations:
      OL ML IL    Err/Tol
      1 1 2    6.1816
      2 6 14    5.0400
      3 4 8    5.4179
      4 2 4    0.49010
  **  ERROR
   DESIGN SPEC IS NOT SATISFIED BECAUSE ONE OR MORE MANIPULATED
   VARIABLE IS AT ITS BOUND.

Block: V401    Model: VALVE

Block: E402    Model: HEATX

Block: FS401 Model: FSPLIT

Block: P401    Model: PUMP

Block: C401    Model: COMPR

Block: F401    Model: FLASH2

Block: P403    Model: PUMP

Block: FS402 Model: FSPLIT

Block: E403    Model: HEATER

Block: V402    Model: VALVE

Block: FS403 Model: FSPLIT

Block: H1101 Model: HEATER

Block: V1101 Model: VALVE

Block: R1101 Model: RPLUG

Block: E1102 Model: HEATER

Block: C1101 Model: COMPR

> Loop $OLVER01 Method: BROYDEN    Iteration 1
  Converging tear streams: 1108    1208    302    408
                        415    R1       R2
  30 vars not converged, Max Err/Tol 0.10000E+07

Block: M2101 Model: MIXER

Block: E1201 Model: HEATX

Block: H1201 Model: HEATER

Block: V1201 Model: VALVE

Block: R1201 Model: RPLUG

Block: E1202 Model: HEATER

Block: C1201 Model: COMPR

Block: M1101 Model: MIXER

Block: E1101 Model: HEATX

Block: M101    Model: MIXER

Block: E102    Model: HEATER

Block: E103    Model: HEATER

Block: E104    Model: HEATX
  * WARNING
   AT LEAST ONE FEED HAS ZERO FLOW
   BLOCK BYPASSED

Block: C201    Model: MCOMPR

Block: F301    Model: FLASH2

Block: F302    Model: FLASH2

Block: M301    Model: MIXER

Block: E401    Model: HEATER

Block: T401    Model: RADFRAC

   Convergence iterations:
      OL ML IL    Err/Tol
      1 1 2    35.162
      2 1 3    0.81445

Block: T402    Model: RADFRAC

   Convergence iterations:
      OL ML IL    Err/Tol
      1 4 12    44.090
      2 2 4    0.39444
  **  ERROR
   DESIGN SPEC IS NOT SATISFIED BECAUSE ONE OR MORE MANIPULATED
   VARIABLE IS AT ITS BOUND.

Block: V401    Model: VALVE

Block: E402    Model: HEATX

Block: FS401 Model: FSPLIT

Block: P401    Model: PUMP

Block: C401    Model: COMPR

Block: F401    Model: FLASH2

Block: P403    Model: PUMP

Block: FS402 Model: FSPLIT

Block: E403    Model: HEATER

Block: V402    Model: VALVE

Block: FS403 Model: FSPLIT

Block: H1101 Model: HEATER

Block: V1101 Model: VALVE

Block: R1101 Model: RPLUG

Block: E1102 Model: HEATER

Block: C1101 Model: COMPR

> Loop $OLVER01 Method: BROYDEN    Iteration 2
  Converging tear streams: 1108    1208    302    408
                        415    R1       R2
  36 vars not converged, Max Err/Tol 0.10000E+07

Block: M2101 Model: MIXER

Block: E1201 Model: HEATX

Block: H1201 Model: HEATER

Block: V1201 Model: VALVE

Block: R1201 Model: RPLUG

Block: E1202 Model: HEATER

Block: C1201 Model: COMPR

Block: M1101 Model: MIXER

Block: E1101 Model: HEATX

Block: M101    Model: MIXER

Block: E102    Model: HEATER

Block: E103    Model: HEATER

Block: E104    Model: HEATX

Block: C201    Model: MCOMPR

Block: F301    Model: FLASH2

Block: F302    Model: FLASH2

Block: M301    Model: MIXER

Block: E401    Model: HEATER

Block: T401    Model: RADFRAC

   Convergence iterations:
      OL ML IL    Err/Tol
      1 1 3    1.6687
      2 1 3    0.19834

Block: T402    Model: RADFRAC

   Convergence iterations:
      OL ML IL    Err/Tol
      1 3 10    1.5213
      2 2 3    0.32102E-01
  **  ERROR
   DESIGN SPEC IS NOT SATISFIED BECAUSE ONE OR MORE MANIPULATED
   VARIABLE IS AT ITS BOUND.

Block: V401    Model: VALVE

Block: E402    Model: HEATX

Block: FS401 Model: FSPLIT

Block: P401    Model: PUMP

Block: C401    Model: COMPR

Block: F401    Model: FLASH2

Block: P403    Model: PUMP

Block: FS402 Model: FSPLIT

Block: E403    Model: HEATER

Block: V402    Model: VALVE

Block: FS403 Model: FSPLIT

Block: H1101 Model: HEATER

Block: V1101 Model: VALVE

Block: R1101 Model: RPLUG

Block: E1102 Model: HEATER

Block: C1101 Model: COMPR

> Loop $OLVER01 Method: BROYDEN    Iteration 3
  Converging tear streams: 1108    1208    302    408
                        415    R1       R2
  37 vars not converged, Max Err/Tol 0.85876E+04

Block: M2101 Model: MIXER

Block: E1201 Model: HEATX

Block: H1201 Model: HEATER

Block: V1201 Model: VALVE

Block: R1201 Model: RPLUG

Block: E1202 Model: HEATER

Block: C1201 Model: COMPR

Block: M1101 Model: MIXER

Block: E1101 Model: HEATX

Block: M101    Model: MIXER

Block: E102    Model: HEATER

Block: E103    Model: HEATER

Block: E104    Model: HEATX

Block: C201    Model: MCOMPR

Block: F301    Model: FLASH2

Block: F302    Model: FLASH2

Block: M301    Model: MIXER

Block: E401    Model: HEATER

Block: T401    Model: RADFRAC

   Convergence iterations:
      OL ML IL    Err/Tol
      1 1 2    0.79368

Block: T402    Model: RADFRAC

   Convergence iterations:
      OL ML IL    Err/Tol
      1 3 10    2.1467
      2 2 4    0.44682E-01
  **  ERROR
   DESIGN SPEC IS NOT SATISFIED BECAUSE ONE OR MORE MANIPULATED
   VARIABLE IS AT ITS BOUND.

Block: V401    Model: VALVE

Block: E402    Model: HEATX

Block: FS401 Model: FSPLIT

Block: P401    Model: PUMP

Block: C401    Model: COMPR

Block: F401    Model: FLASH2

Block: P403    Model: PUMP

Block: FS402 Model: FSPLIT

Block: E403    Model: HEATER

Block: V402    Model: VALVE

Block: FS403 Model: FSPLIT

Block: H1101 Model: HEATER

Block: V1101 Model: VALVE

Block: R1101 Model: RPLUG

Block: E1102 Model: HEATER

Block: C1101 Model: COMPR

> Loop $OLVER01 Method: BROYDEN    Iteration 4
  Converging tear streams: 1108    1208    302    408
                        415    R1       R2
  37 vars not converged, Max Err/Tol 0.41984E+04

Block: M2101 Model: MIXER

Block: E1201 Model: HEATX

Block: H1201 Model: HEATER

Block: V1201 Model: VALVE

Block: R1201 Model: RPLUG

Block: E1202 Model: HEATER

Block: C1201 Model: COMPR

Block: M1101 Model: MIXER

Block: E1101 Model: HEATX

Block: M101    Model: MIXER

Block: E102    Model: HEATER

Block: E103    Model: HEATER

Block: E104    Model: HEATX

Block: C201    Model: MCOMPR

Block: F301    Model: FLASH2

Block: F302    Model: FLASH2

Block: M301    Model: MIXER

Block: E401    Model: HEATER

Block: T401    Model: RADFRAC

   Convergence iterations:
      OL ML IL    Err/Tol
      1 1 3    1.2157
      2 1 3    0.47745E-01

Block: T402    Model: RADFRAC

   Convergence iterations:
      OL ML IL    Err/Tol
      1 3 10    3.3115
      2 2 4    0.64661E-01
  **  ERROR
   DESIGN SPEC IS NOT SATISFIED BECAUSE ONE OR MORE MANIPULATED
   VARIABLE IS AT ITS BOUND.

Block: V401    Model: VALVE

Block: E402    Model: HEATX

Block: FS401 Model: FSPLIT

Block: P401    Model: PUMP

Block: C401    Model: COMPR
  * WARNING
   FEED STREAM IS BELOW DEW POINT

Block: F401    Model: FLASH2

Block: P403    Model: PUMP

Block: FS402 Model: FSPLIT

Block: E403    Model: HEATER

Block: V402    Model: VALVE

Block: FS403 Model: FSPLIT

Block: H1101 Model: HEATER

Block: V1101 Model: VALVE

Block: R1101 Model: RPLUG

Block: E1102 Model: HEATER

Block: C1101 Model: COMPR

> Loop $OLVER01 Method: BROYDEN    Iteration 5
  Converging tear streams: 1108    1208    302    408
                        415    R1       R2
  37 vars not converged, Max Err/Tol 0.20829E+04

Block: M2101 Model: MIXER

Block: E1201 Model: HEATX

Block: H1201 Model: HEATER

Block: V1201 Model: VALVE

Block: R1201 Model: RPLUG

Block: E1202 Model: HEATER

Block: C1201 Model: COMPR

Block: M1101 Model: MIXER

Block: E1101 Model: HEATX

Block: M101    Model: MIXER

Block: E102    Model: HEATER

Block: E103    Model: HEATER

Block: E104    Model: HEATX

Block: C201    Model: MCOMPR

Block: F301    Model: FLASH2

Block: F302    Model: FLASH2

Block: M301    Model: MIXER

Block: E401    Model: HEATER

Block: T401    Model: RADFRAC

   Convergence iterations:
      OL ML IL    Err/Tol
      1 1 3    1.9794
      2 1 3    0.73360E-01

Block: T402    Model: RADFRAC

   Convergence iterations:
      OL ML IL    Err/Tol
      1 4 14    6.3515
      2 5 15    6.7556
      3 5 21    23.766
      4 2 5    11.818
      5 2 5    1.3146
      6 2 4    0.45447
  **  ERROR
   DESIGN SPEC IS NOT SATISFIED BECAUSE ONE OR MORE MANIPULATED
   VARIABLE IS AT ITS BOUND.

Block: V401    Model: VALVE

Block: E402    Model: HEATX

Block: FS401 Model: FSPLIT

Block: P401    Model: PUMP

Block: C401    Model: COMPR
  * WARNING
   FEED STREAM IS BELOW DEW POINT

Block: F401    Model: FLASH2

Block: P403    Model: PUMP

Block: FS402 Model: FSPLIT

Block: E403    Model: HEATER

Block: V402    Model: VALVE

Block: FS403 Model: FSPLIT

Block: H1101 Model: HEATER

Block: V1101 Model: VALVE

Block: R1101 Model: RPLUG

Block: E1102 Model: HEATER

Block: C1101 Model: COMPR

> Loop $OLVER01 Method: BROYDEN    Iteration 6
  Converging tear streams: 1108    1208    302    408
                        415    R1       R2
  37 vars not converged, Max Err/Tol 0.29930E+04

Block: M2101 Model: MIXER

Block: E1201 Model: HEATX

Block: H1201 Model: HEATER

Block: V1201 Model: VALVE

Block: R1201 Model: RPLUG

Block: E1202 Model: HEATER

Block: C1201 Model: COMPR

Block: M1101 Model: MIXER

Block: E1101 Model: HEATX

Block: M101    Model: MIXER

Block: E102    Model: HEATER

Block: E103    Model: HEATER

Block: E104    Model: HEATX

Block: C201    Model: MCOMPR

Block: F301    Model: FLASH2

Block: F302    Model: FLASH2

Block: M301    Model: MIXER

Block: E401    Model: HEATER

Block: T401    Model: RADFRAC

   Convergence iterations:
      OL ML IL    Err/Tol
      1 1 2    0.67834

Block: T402    Model: RADFRAC

   Convergence iterations:
      OL ML IL    Err/Tol
      1 7 33    32.966
      2 3 12    19.847
      3 5 17    5.8414
      4 2 5    2.9435
      5 2 4    0.17356
  **  ERROR
   DESIGN SPEC IS NOT SATISFIED BECAUSE ONE OR MORE MANIPULATED
   VARIABLE IS AT ITS BOUND.

Block: V401    Model: VALVE

Block: E402    Model: HEATX

Block: FS401 Model: FSPLIT

Block: P401    Model: PUMP

Block: C401    Model: COMPR
  * WARNING
   FEED STREAM IS BELOW DEW POINT

Block: F401    Model: FLASH2

Block: P403    Model: PUMP

Block: FS402 Model: FSPLIT

Block: E403    Model: HEATER

Block: V402    Model: VALVE

Block: FS403 Model: FSPLIT

Block: H1101 Model: HEATER

Block: V1101 Model: VALVE

Block: R1101 Model: RPLUG

Block: E1102 Model: HEATER

Block: C1101 Model: COMPR

> Loop $OLVER01 Method: BROYDEN    Iteration 7
  Converging tear streams: 1108    1208    302    408
                        415    R1       R2
  35 vars not converged, Max Err/Tol 0.15142E+04

Block: M2101 Model: MIXER

Block: E1201 Model: HEATX

Block: H1201 Model: HEATER

Block: V1201 Model: VALVE

Block: R1201 Model: RPLUG

Block: E1202 Model: HEATER

Block: C1201 Model: COMPR

Block: M1101 Model: MIXER

Block: E1101 Model: HEATX

Block: M101    Model: MIXER

Block: E102    Model: HEATER

Block: E103    Model: HEATER

Block: E104    Model: HEATX

Block: C201    Model: MCOMPR

Block: F301    Model: FLASH2

Block: F302    Model: FLASH2

Block: M301    Model: MIXER

Block: E401    Model: HEATER

Block: T401    Model: RADFRAC

   Convergence iterations:
      OL ML IL    Err/Tol
      1 1 2    0.37997

Block: T402    Model: RADFRAC

   Convergence iterations:
      OL ML IL    Err/Tol
      1 4 12    0.95289
  **  ERROR
   DESIGN SPEC IS NOT SATISFIED BECAUSE ONE OR MORE MANIPULATED
   VARIABLE IS AT ITS BOUND.

Block: V401    Model: VALVE

Block: E402    Model: HEATX

Block: FS401 Model: FSPLIT

Block: P401    Model: PUMP

Block: C401    Model: COMPR
  * WARNING
   FEED STREAM IS BELOW DEW POINT

Block: F401    Model: FLASH2

Block: P403    Model: PUMP

Block: FS402 Model: FSPLIT

Block: E403    Model: HEATER

Block: V402    Model: VALVE

Block: FS403 Model: FSPLIT

Block: H1101 Model: HEATER

Block: V1101 Model: VALVE

Block: R1101 Model: RPLUG

Block: E1102 Model: HEATER

Block: C1101 Model: COMPR

> Loop $OLVER01 Method: BROYDEN    Iteration 8
  Converging tear streams: 1108    1208    302    408
                        415    R1       R2
  35 vars not converged, Max Err/Tol  -0.13075E+04

Block: M2101 Model: MIXER

Block: E1201 Model: HEATX

Block: H1201 Model: HEATER

Block: V1201 Model: VALVE

Block: R1201 Model: RPLUG

Block: E1202 Model: HEATER

Block: C1201 Model: COMPR

Block: M1101 Model: MIXER

Block: E1101 Model: HEATX

Block: M101    Model: MIXER

Block: E102    Model: HEATER

Block: E103    Model: HEATER

Block: E104    Model: HEATX

Block: C201    Model: MCOMPR

Block: F301    Model: FLASH2

Block: F302    Model: FLASH2

Block: M301    Model: MIXER

Block: E401    Model: HEATER

Block: T401    Model: RADFRAC

   Convergence iterations:
      OL ML IL    Err/Tol
      1 1 2    0.77745

Block: T402    Model: RADFRAC

   Convergence iterations:
      OL ML IL    Err/Tol
      1 4 13    3.7182
      2 5 15    6.4073
      3 5 20    21.001
      4 2 5    9.8185
      5 2 5    1.7264
      6 2 4    0.52931
  **  ERROR
   DESIGN SPEC IS NOT SATISFIED BECAUSE ONE OR MORE MANIPULATED
   VARIABLE IS AT ITS BOUND.

Block: V401    Model: VALVE

Block: E402    Model: HEATX

Block: FS401 Model: FSPLIT

Block: P401    Model: PUMP

Block: C401    Model: COMPR
  * WARNING
   FEED STREAM IS BELOW DEW POINT

Block: F401    Model: FLASH2

Block: P403    Model: PUMP

Block: FS402 Model: FSPLIT

Block: E403    Model: HEATER

Block: V402    Model: VALVE

Block: FS403 Model: FSPLIT

Block: H1101 Model: HEATER

Block: V1101 Model: VALVE

Block: R1101 Model: RPLUG

Block: E1102 Model: HEATER

Block: C1101 Model: COMPR

> Loop $OLVER01 Method: BROYDEN    Iteration 9
  Converging tear streams: 1108    1208    302    408
                        415    R1       R2
  35 vars not converged, Max Err/Tol 0.20323E+04

Block: M2101 Model: MIXER

Block: E1201 Model: HEATX

Block: H1201 Model: HEATER

Block: V1201 Model: VALVE

Block: R1201 Model: RPLUG

Block: E1202 Model: HEATER

Block: C1201 Model: COMPR

Block: M1101 Model: MIXER

Block: E1101 Model: HEATX

Block: M101    Model: MIXER

Block: E102    Model: HEATER

Block: E103    Model: HEATER

Block: E104    Model: HEATX

Block: C201    Model: MCOMPR

Block: F301    Model: FLASH2

Block: F302    Model: FLASH2

Block: M301    Model: MIXER

Block: E401    Model: HEATER

Block: T401    Model: RADFRAC

   Convergence iterations:
      OL ML IL    Err/Tol
      1 1 2    0.48395

Block: T402    Model: RADFRAC

   Convergence iterations:
      OL ML IL    Err/Tol
      1 5 19    3.6521
      2 3 6    0.16667

Block: V401    Model: VALVE

Block: E402    Model: HEATX

Block: FS401 Model: FSPLIT

Block: P401    Model: PUMP

Block: C401    Model: COMPR
  * WARNING
   FEED STREAM IS BELOW DEW POINT

Block: F401    Model: FLASH2

Block: P403    Model: PUMP

Block: FS402 Model: FSPLIT

Block: E403    Model: HEATER

Block: V402    Model: VALVE

Block: FS403 Model: FSPLIT

Block: H1101 Model: HEATER

Block: V1101 Model: VALVE

Block: R1101 Model: RPLUG

Block: E1102 Model: HEATER

Block: C1101 Model: COMPR

> Loop $OLVER01 Method: BROYDEN    Iteration 10
  Converging tear streams: 1108    1208    302    408
                        415    R1       R2
  30 vars not converged, Max Err/Tol 0.15375E+04

Block: M2101 Model: MIXER

Block: E1201 Model: HEATX

Block: H1201 Model: HEATER

Block: V1201 Model: VALVE

Block: R1201 Model: RPLUG

Block: E1202 Model: HEATER

Block: C1201 Model: COMPR

Block: M1101 Model: MIXER

Block: E1101 Model: HEATX

Block: M101    Model: MIXER

Block: E102    Model: HEATER

Block: E103    Model: HEATER

Block: E104    Model: HEATX

Block: C201    Model: MCOMPR

Block: F301    Model: FLASH2

Block: F302    Model: FLASH2

Block: M301    Model: MIXER

Block: E401    Model: HEATER

Block: T401    Model: RADFRAC

   Convergence iterations:
      OL ML IL    Err/Tol
      1 1 2    0.75005

Block: T402    Model: RADFRAC

   Convergence iterations:
      OL ML IL    Err/Tol
      1 7 35    31.007
      2 3 12    18.910
      3 5 16    5.7956
      4 2 5    2.8236
      5 2 4    0.16583
  **  ERROR
   DESIGN SPEC IS NOT SATISFIED BECAUSE ONE OR MORE MANIPULATED
   VARIABLE IS AT ITS BOUND.

Block: V401    Model: VALVE

Block: E402    Model: HEATX

Block: FS401 Model: FSPLIT

Block: P401    Model: PUMP

Block: C401    Model: COMPR
  * WARNING
   FEED STREAM IS BELOW DEW POINT

Block: F401    Model: FLASH2

Block: P403    Model: PUMP

Block: FS402 Model: FSPLIT

Block: E403    Model: HEATER

Block: V402    Model: VALVE

Block: FS403 Model: FSPLIT

Block: H1101 Model: HEATER

Block: V1101 Model: VALVE

Block: R1101 Model: RPLUG

Block: E1102 Model: HEATER

Block: C1101 Model: COMPR

> Loop $OLVER01 Method: BROYDEN    Iteration 11
  Converging tear streams: 1108    1208    302    408
                        415    R1       R2
  35 vars not converged, Max Err/Tol 0.15276E+04

Block: M2101 Model: MIXER

Block: E1201 Model: HEATX

Block: H1201 Model: HEATER

Block: V1201 Model: VALVE

Block: R1201 Model: RPLUG

Block: E1202 Model: HEATER

Block: C1201 Model: COMPR

Block: M1101 Model: MIXER

Block: E1101 Model: HEATX

Block: M101    Model: MIXER

Block: E102    Model: HEATER

Block: E103    Model: HEATER

Block: E104    Model: HEATX

Block: C201    Model: MCOMPR

Block: F301    Model: FLASH2

Block: F302    Model: FLASH2

Block: M301    Model: MIXER

Block: E401    Model: HEATER

Block: T401    Model: RADFRAC

   Convergence iterations:
      OL ML IL    Err/Tol
      1 1 2    0.34356

Block: T402    Model: RADFRAC

   Convergence iterations:
      OL ML IL    Err/Tol
      1 4 12    0.84783
  **  ERROR
   DESIGN SPEC IS NOT SATISFIED BECAUSE ONE OR MORE MANIPULATED
   VARIABLE IS AT ITS BOUND.

Block: V401    Model: VALVE

Block: E402    Model: HEATX

Block: FS401 Model: FSPLIT

Block: P401    Model: PUMP

Block: C401    Model: COMPR
  * WARNING
   FEED STREAM IS BELOW DEW POINT

Block: F401    Model: FLASH2

Block: P403    Model: PUMP

Block: FS402 Model: FSPLIT

Block: E403    Model: HEATER

Block: V402    Model: VALVE

Block: FS403 Model: FSPLIT

Block: H1101 Model: HEATER

Block: V1101 Model: VALVE

Block: R1101 Model: RPLUG

Block: E1102 Model: HEATER

Block: C1101 Model: COMPR

> Loop $OLVER01 Method: BROYDEN    Iteration 12
  Converging tear streams: 1108    1208    302    408
                        415    R1       R2
  30 vars not converged, Max Err/Tol 0.13257E+04

Block: M2101 Model: MIXER

Block: E1201 Model: HEATX

Block: H1201 Model: HEATER

Block: V1201 Model: VALVE

Block: R1201 Model: RPLUG

Block: E1202 Model: HEATER

Block: C1201 Model: COMPR

Block: M1101 Model: MIXER

Block: E1101 Model: HEATX

Block: M101    Model: MIXER

Block: E102    Model: HEATER

Block: E103    Model: HEATER

Block: E104    Model: HEATX

Block: C201    Model: MCOMPR

Block: F301    Model: FLASH2

Block: F302    Model: FLASH2

Block: M301    Model: MIXER

Block: E401    Model: HEATER

Block: T401    Model: RADFRAC

   Convergence iterations:
      OL ML IL    Err/Tol
      1 1 2    0.67562

Block: T402    Model: RADFRAC

   Convergence iterations:
      OL ML IL    Err/Tol
      1 4 14    3.5931
      2 5 15    6.6133
      3 5 21    22.465
      4 2 5    10.852
      5 2 5    1.6078
      6 2 4    0.54973
  **  ERROR
   DESIGN SPEC IS NOT SATISFIED BECAUSE ONE OR MORE MANIPULATED
   VARIABLE IS AT ITS BOUND.

Block: V401    Model: VALVE

Block: E402    Model: HEATX

Block: FS401 Model: FSPLIT

Block: P401    Model: PUMP

Block: C401    Model: COMPR
  * WARNING
   FEED STREAM IS BELOW DEW POINT

Block: F401    Model: FLASH2

Block: P403    Model: PUMP

Block: FS402 Model: FSPLIT

Block: E403    Model: HEATER

Block: V402    Model: VALVE

Block: FS403 Model: FSPLIT

Block: H1101 Model: HEATER

Block: V1101 Model: VALVE

Block: R1101 Model: RPLUG

Block: E1102 Model: HEATER

Block: C1101 Model: COMPR

> Loop $OLVER01 Method: BROYDEN    Iteration 13
  Converging tear streams: 1108    1208    302    408
                        415    R1       R2
  36 vars not converged, Max Err/Tol 0.23002E+04

Block: M2101 Model: MIXER

Block: E1201 Model: HEATX

Block: H1201 Model: HEATER

Block: V1201 Model: VALVE

Block: R1201 Model: RPLUG

Block: E1202 Model: HEATER

Block: C1201 Model: COMPR

Block: M1101 Model: MIXER

Block: E1101 Model: HEATX

Block: M101    Model: MIXER

Block: E102    Model: HEATER

Block: E103    Model: HEATER

Block: E104    Model: HEATX

Block: C201    Model: MCOMPR

Block: F301    Model: FLASH2

Block: F302    Model: FLASH2

Block: M301    Model: MIXER

Block: E401    Model: HEATER

Block: T401    Model: RADFRAC

   Convergence iterations:
      OL ML IL    Err/Tol
      1 1 2    0.36627

Block: T402    Model: RADFRAC

   Convergence iterations:
      OL ML IL    Err/Tol
      1 5 19    5.7208
      2 3 9    0.88011

Block: V401    Model: VALVE

Block: E402    Model: HEATX

Block: FS401 Model: FSPLIT

Block: P401    Model: PUMP

Block: C401    Model: COMPR
  * WARNING
   FEED STREAM IS BELOW DEW POINT

            ***  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             27

希望大神给看看

tdl522 · 发表于 1970-1-1 08:00:00

无！

，，， · 发表于 1970-1-1 08:00:00

tdl522 发表于 2016-5-28 20:54

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谢啦