- 积分
- 15
- 注册时间
- 2016-2-12
- 积分
- 15
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->Processing input specifications ...
THE PAIR PARAMETERS FOR ELECNRTL OPTION SET HAS BEEN RETRIEVED FROM
DATABANK ENRTL-RK.
INFORMATION
PURE COMPONENT PARAMETERS FOR SOME COMPONENTS ARE RETRIEVED FROM
DATABANK. THESE PARAMETERS ARE USED WITH THE ELECNRTL OPTION SET
UNLESS YOU ENTER YOUR OWN PARAMETERS IN PROP-DATA PARAGRAPHS.
PARAMETER THRSWT(ELEMENT/3) RETRIEVED FOR COMPONENT WATER
PARAMETER PLXANT RETRIEVED FOR COMPONENT WATER
STRUCTURE FOR COMPONENT FORMA-01 HAS NOT BEEN DEFINED.
PCES CANNOT USE GROUP-CONTRIBUTION METHODS TO ESTIMATE MISSING PROPERTIES
USE THE STRUCTURES PARAGRAPH TO DEFINE STRUCTURES OF THIS COMPONENT.
* WARNING IN PHYSICAL PROPERTY SYSTEM
PARAMETER PLXANT (DATA SET 1) FOR COMPONENT DMD:
UNREASONABLE VAPOR PRESSURE CALCULATED AT NORMAL BOILING POINT.
VALUE SHOULD BE WITHIN 10% OF 1D5 N/SQM. PLEASE CHECK YOUR INPUT
FOR THE ANTOINE PARAMETERS.
* WARNING WHILE CHECKING INPUT SPECIFICATIONS
INCONSISTENT FREE WATER SETTING DETECTED FOR 4 STREAMS
SOURCE BLOCK FREE WATER STREAM DESTINATION BLOCK FREE WATER
=================== ========== ======== =================== ==========
B9 NO S2 B10 YES
B8 NO 11 B10 YES
B13 NO S14 B10 YES
B10 YES C4H10O B12 NO
Flowsheet Analysis :
Block $OLVER01 (Method: WEGSTEIN) has been defined to converge
streams: 7
Block $OLVER02 (Method: WEGSTEIN) has been defined to converge
streams: S14
COMPUTATION ORDER FOR THE FLOWSHEET:
B1 B9 B6 B7
$OLVER01 B2 B3 B4
(RETURN $OLVER01)
B5 B8
$OLVER02 B10 B12 B13
(RETURN $OLVER02)
B14 B15 B16 B17 B11 B19
->Calculations begin ...
Block: B1 Model: HEATER
Block: B9 Model: HEATER
Block: B6 Model: HEATER
Block: B7 Model: FSPLIT
> Beginning Convergence Loop $OLVER01 Method: WEGSTEIN
Converging tear streams: 7
Block: B2 Model: RSTOIC
Block: B3 Model: HEATER
Block: B4 Model: RADFRAC
Convergence iterations:
OL ML IL Err/Tol
1 1 7 1727.7
2 1 4 338.63
3 1 4 113.72
4 1 4 16.692
5 1 3 5.4455
6 1 4 1.0772
7 1 4 0.45934
> Loop $OLVER01 Method: WEGSTEIN Iteration 1
Converging tear streams: 7
4 vars not converged, Max Err/Tol 0.10000E+07
Block: B2 Model: RSTOIC
Block: B3 Model: HEATER
Block: B4 Model: RADFRAC
Convergence iterations:
OL ML IL Err/Tol
1 1 6 83.584
2 1 4 29.129
3 1 3 19.210
4 1 3 10.193
5 1 3 0.25013
> Loop $OLVER01 Method: WEGSTEIN Iteration 2
Converging tear streams: 7
3 vars not converged, Max Err/Tol -0.15366E+04
Block: B2 Model: RSTOIC
Block: B3 Model: HEATER
Block: B4 Model: RADFRAC
Convergence iterations:
OL ML IL Err/Tol
1 1 7 96.787
2 1 4 37.818
3 1 3 31.186
4 1 3 15.536
5 1 3 0.49068
> Loop $OLVER01 Method: WEGSTEIN Iteration 3
Converging tear streams: 7
4 vars not converged, Max Err/Tol -0.75693E+03
Block: B2 Model: RSTOIC
Block: B3 Model: HEATER
Block: B4 Model: RADFRAC
Convergence iterations:
OL ML IL Err/Tol
1 1 7 77.496
2 1 4 33.475
3 1 4 33.569
4 1 4 16.139
5 1 3 0.84549
> Loop $OLVER01 Method: WEGSTEIN Iteration 4
Converging tear streams: 7
4 vars not converged, Max Err/Tol 0.34003E+02
Block: B2 Model: RSTOIC
Block: B3 Model: HEATER
Block: B4 Model: RADFRAC
Convergence iterations:
OL ML IL Err/Tol
1 1 6 6.6100
2 1 4 2.9334
3 1 4 1.9169
4 1 4 0.15103
> Loop $OLVER01 Method: WEGSTEIN Iteration 5
Converging tear streams: 7
4 vars not converged, Max Err/Tol -0.46550E+02
Block: B2 Model: RSTOIC
Block: B3 Model: HEATER
Block: B4 Model: RADFRAC
Convergence iterations:
OL ML IL Err/Tol
1 1 4 0.22657
> Loop $OLVER01 Method: WEGSTEIN Iteration 6
Converging tear streams: 7
4 vars not converged, Max Err/Tol 0.55753E+01
Block: B2 Model: RSTOIC
Block: B3 Model: HEATER
Block: B4 Model: RADFRAC
Convergence iterations:
OL ML IL Err/Tol
1 1 4 0.51223E-01
> Loop $OLVER01 Method: WEGSTEIN Iteration 7
Converging tear streams: 7
1 vars not converged, Max Err/Tol -0.16082E+01
Block: B2 Model: RSTOIC
Block: B3 Model: HEATER
Block: B4 Model: RADFRAC
Convergence iterations:
OL ML IL Err/Tol
1 1 4 0.90102E-01
> Loop $OLVER01 Method: WEGSTEIN Iteration 8
Converging tear streams: 7
# Converged Max Err/Tol -0.63486E+00
Block: B5 Model: HEATER
Block: B8 Model: HEATER
> Beginning Convergence Loop $OLVER02 Method: WEGSTEIN
Converging tear streams: S14
Block: B10 Model: RSTOIC
Block: B12 Model: HEATER
Block: B13 Model: RADFRAC
Convergence iterations:
OL ML IL Err/Tol
1 1 7 1821.0
2 1 6 246.75
3 1 5 199.88
4 1 3 23.417
5 1 4 10.049
6 1 4 4.4820
7 1 3 0.92160
> Loop $OLVER02 Method: WEGSTEIN Iteration 1
Converging tear streams: S14
4 vars not converged, Max Err/Tol 0.10000E+07
Block: B10 Model: RSTOIC
Block: B12 Model: HEATER
Block: B13 Model: RADFRAC
Convergence iterations:
OL ML IL Err/Tol
1 1 9 3568.0
2 1 3 425.54
3 1 4 122.29
4 1 4 43.389
5 1 3 10.044
6 1 3 3.2077
7 1 3 0.60469
> Loop $OLVER02 Method: WEGSTEIN Iteration 2
Converging tear streams: S14
3 vars not converged, Max Err/Tol -0.10000E+05
Block: B10 Model: RSTOIC
Block: B12 Model: HEATER
Block: B13 Model: RADFRAC
Convergence iterations:
OL ML IL Err/Tol
1 1 5 0.71925
> Loop $OLVER02 Method: WEGSTEIN Iteration 3
Converging tear streams: S14
# Converged Max Err/Tol -0.12363E+00
Block: B14 Model: HEATER
Block: B15 Model: RSTOIC
Block: B16 Model: HEATER
Block: B17 Model: RADFRAC
Convergence iterations:
OL ML IL Err/Tol
1 1 7 275.87
2 1 5 101.55
3 1 3 12.209
4 1 3 1.6514
5 1 3 0.38471
Block: B11 Model: RADFRAC
Convergence iterations:
OL ML IL Err/Tol
1 1 3 31.329
2 1 3 4.6355
3 1 3 2.0701
4 1 3 0.72121E-01
Block: B19 Model: RADFRAC
Convergence iterations:
OL ML IL Err/Tol
1 1 2 6.9072
2 1 4 0.22476
->Generating block results ...
Block: B6 Model: HEATER
Block: B9 Model: HEATER
Block: B3 Model: HEATER
Block: B5 Model: HEATER
Block: B12 Model: HEATER
Block: B14 Model: HEATER
Block: B8 Model: HEATER
Block: B16 Model: HEATER
Block: B1 Model: HEATER
->Simulation calculations completed ...
*** Warning(s) were issued during Input Translation ***
*** Check the Run Status Results for more Information ***
*** No Errors or Warnings were issued during Simulation ***
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