Disable STREAM O2 due to disabled source AND destination
Disable STREAM NO due to disabled source AND destination
Disable STREAM PRODUCT5 due to disabled source AND destination
Disable STREAM PRODUCT6 due to disabled source AND destination
Disable STREAM CH3OH2 due to disabled source AND destination
Disable STREAM PRODUCT7 due to disabled source AND destination
Disable STREAM V2 due to disabled source AND destination
Disable STREAM L2 due to disabled source AND destination
Flowsheet Analysis :
Block $OLVER01 (Method: SECANT ) has been defined to converge
specs : DS-1
COMPUTATION ORDER FOR THE FLOWSHEET:
MIXER H1 R1 H2
$OLVER01 D1
(RETURN $OLVER01)
->Calculations begin ...
Block: MIXER Model: MIXER
Block: H1 Model: HEATER
Block: R1 Model: RSTOIC
Block: H2 Model: HEATER
Block: D1 Model: DISTL
*** SEVERE ERROR
VAPOR FLOWRATE BELOW THE FEED STAGE IS ZERO.
FEED QUALITY IS 0.10000E+36 REFLUX RATIO IS 1.2000
EITHER FEED QUALITY IS TOO HIGH OR REFLUX RATIO IS TOO LOW.
> Beginning Convergence Loop $OLVER01 Method: SECANT
1 vars not converged, Max Err/Tol -0.60899E+02
Block: D1 Model: DISTL
*** SEVERE ERROR
VAPOR FLOWRATE BELOW THE FEED STAGE IS ZERO.
FEED QUALITY IS 0.10000E+36 REFLUX RATIO IS 1.2000
EITHER FEED QUALITY IS TOO HIGH OR REFLUX RATIO IS TOO LOW.
> Loop $OLVER01 Method: SECANT Iteration 2
* WARNING
SPEC FUNCTION NOT CHANGING, POSSIBLY HAS A FLAT RESPONSE
TO THE MANIPULATED PARAMETER WITHIN THE GIVEN BOUNDS.
1 vars not converged, Max Err/Tol -0.60899E+02
** ERROR
Convergence block $OLVER01 did not converge
normally in the final pass
->Generating block results ...
Block: H1 Model: HEATER
Block: H2 Model: HEATER
->Simulation calculations completed ...
*** No Warnings were issued during Input Translation ***
FEED QUALITY IS 0.10000E+36 REFLUX RATIO IS 1.2000
EITHER FEED QUALITY IS TOO HIGH OR REFLUX RATIO IS TOO LOW.
A FLAT RESPONSE
TO THE MANIPULATED PARAMETER WITHIN THE GIVEN BOUNDS.
初值不合适而导致 操纵变量无变化!调节进料,下调试试!