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用CSTR模拟气体在液相的反应,,结果有问题
Beginning Convergence Loop $OLVER01 Method: WEGSTEIN
Converging tear streams: CATARE
Block: R-101 Model: RCSTR
Block: R-102 Model: RCSTR
Block: F-1 Model: FLASH2
Block: F-2 Model: FLASH2
* WARNING
ZERO FEED TO THE BLOCK. BLOCK BYPASSED
> Loop $OLVER01 Method: WEGSTEIN Iteration 1
Converging tear streams: CATARE
2 vars not converged, Max Err/Tol -0.10000E+05
Block: R-101 Model: RCSTR
HENRY CONSTANT MODEL HENRY1 HAS MISSING PARAMETERS. PLEASE
PROVIDE THE MISSING PARAMETERS FOR MAJOR SOLVENTS. THIS ERROR MAY OCCUR
BECAUSE THE STREAM IS ALL VAPOR, BUT VLE CALCULATION IS REQUESTED.
TRY SPECIFY VALID-PHASES=VAPOR-ONLY
HENRY/1ST ELEMENT (DATA SET 1) MISSING FOR SUPERCRITICAL COMPONENT
H2 WITH ALL SOLVENTS:
PE
CO WITH ALL SOLVENTS:
PE
****PROPERTY PARAMETER ERROR
ERRORS ENCOUNTERED IN CALCULATION OF LIQUID MIXTURE PROPS USING
OPTION SET UNIQ-RK FOR PHIMX
! Calculations stopped because of missing property parameters
->By-passing economic evaluation because simulation case failed
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