求助！物料不平衡以及不收敛
在弄一个烟气再循环的，总是报错说质量不平衡，但是用结算结果反算质量是平衡的。请各位高手提点。Block: COMBST Model: RGIBBS
**ERROR
UNABLE TO BALANCE ALL OF ATOM H WITH JUST PRODUCT H2O
CALCULATIONS BYPASSED
**ERROR
BLOCK COMBST IS NOT IN MASS BALANCE:
MASS INLET FLOW = 0.14250000E-02, MASS OUTLET FLOW = 0.37639949E-03
RELATIVE DIFFERENCE = 0.27858712E+01
CHECK BLOCK SPECIFICATIONS
Block: B3 Model: HEATER
Block: B1 Model: FSPLIT
* WARNING
SUM OF SPLITS FOR (1) SPECIFICATIONS (29.648919)
IS NOT EQUAL TO 1 FOR "OUTLETS". VALUES NORMALIZED.
Block: B5 Model: SEP
Block: B2 Model: MIXER
> Loop $OLVER01 Method: WEGSTEIN Iteration 1
Converging tear streams: INLETGAS
* WARNING
VALUE IS MISSING FOR VARIABLE 20.
THIS MAY BE CAUSED BY A ZERO-FLOW STREAM.
THE PREVIOUS VALUE OF THE VARIABLE WILL BE USED.
10 vars not converged, Max Err/Tol 0.10000E+07
Block: COMBST Model: RGIBBS
Block: B3 Model: HEATER
Block: B1 Model: FSPLIT
Block: B5 Model: SEP
Block: B2 Model: MIXER
> Loop $OLVER01 Method: WEGSTEIN Iteration 2
Converging tear streams: INLETGAS
6 vars not converged, Max Err/Tol 0.17146E+10
Block: COMBST Model: RGIBBS
Block: B3 Model: HEATER
Block: B1 Model: FSPLIT
Block: B5 Model: SEP
Block: B2 Model: MIXER
> Loop $OLVER01 Method: WEGSTEIN Iteration 3
Converging tear streams: INLETGAS
8 vars not converged, Max Err/Tol 0.58411E+04
Block: COMBST Model: RGIBBS
Block: B3 Model: HEATER
Block: B1 Model: FSPLIT
Block: B5 Model: SEP
Block: B2 Model: MIXER
> Loop $OLVER01 Method: WEGSTEIN Iteration 4
Converging tear streams: INLETGAS
8 vars not converged, Max Err/Tol-0.55955E+04
Block: COMBST Model: RGIBBS
Block: B3 Model: HEATER
Block: B1 Model: FSPLIT
Block: B5 Model: SEP
Block: B2 Model: MIXER
> Loop $OLVER01 Method: WEGSTEIN Iteration 5
Converging tear streams: INLETGAS
8 vars not converged, Max Err/Tol-0.10003E+04
Block: COMBST Model: RGIBBS
Block: B3 Model: HEATER
Block: B1 Model: FSPLIT
Block: B5 Model: SEP
Block: B2 Model: MIXER
> Loop $OLVER01 Method: WEGSTEIN Iteration 6
Converging tear streams: INLETGAS
8 vars not converged, Max Err/Tol-0.56548E+03
Block: COMBST Model: RGIBBS
Block: B3 Model: HEATER
Block: B1 Model: FSPLIT
Block: B5 Model: SEP
Block: B2 Model: MIXER
> Loop $OLVER01 Method: WEGSTEIN Iteration 7
Converging tear streams: INLETGAS
8 vars not converged, Max Err/Tol 0.82705E+03
Block: COMBST Model: RGIBBS
Block: B3 Model: HEATER
Block: B1 Model: FSPLIT
Block: B5 Model: SEP
Block: B2 Model: MIXER
> Loop $OLVER01 Method: WEGSTEIN Iteration 8
Converging tear streams: INLETGAS
8 vars not converged, Max Err/Tol-0.21845E+02
Block: COMBST Model: RGIBBS
Block: B3 Model: HEATER
Block: B1 Model: FSPLIT
Block: B5 Model: SEP
Block: B2 Model: MIXER
> Loop $OLVER01 Method: WEGSTEIN Iteration 9
Converging tear streams: INLETGAS
6 vars not converged, Max Err/Tol 0.14477E+02
Block: COMBST Model: RGIBBS
Block: B3 Model: HEATER
Block: B1 Model: FSPLIT
Block: B5 Model: SEP
Block: B2 Model: MIXER
> Loop $OLVER01 Method: WEGSTEIN Iteration 10
Converging tear streams: INLETGAS
5 vars not converged, Max Err/Tol 0.40988E+01
Block: COMBST Model: RGIBBS
Block: B3 Model: HEATER
Block: B1 Model: FSPLIT
Block: B5 Model: SEP
Block: B2 Model: MIXER
> Loop $OLVER01 Method: WEGSTEIN Iteration 11
Converging tear streams: INLETGAS
# Converged Max Err/Tol 0.68702E+00
->Simulation calculations completed ...
你这样别人没有兴趣看的，你把模拟的文档分享出来，别人或许可以帮你找原因
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