己二酸二甲酯反应精馏塔的模拟与优化
己二酸二甲酯反应精馏模拟与优化一直出现这个错误啊 求助Calculations begin ...
> Beginning Convergence Loop $OLVER01 Method: BROYDEN
Block: C1 Model: RADFRAC
*** SEVERE ERROR
A LIQUID FEED/PUMPAROUND TO THE TOP STAGE IS REQUIRED WHEN
"Q1=0" IS SPECIFIED IN "COL-SPECS"; REQUIRED FEED/PUMPAROUND
HAS ZERO FLOW.
* WARNING
REST OF BLOCK BYPASSED DUE TO SEVERE ERROR.
Block: C2 Model: HEATER
Block: C3 Model: DECANTER
* WARNING
NO PHASE SPLITTING OCCURS AT GIVEN SPECIFICATIONS. SINGLE PHASE
SOLUTION IS RETURNED.
> Loop $OLVER01 Method: BROYDEN Iteration 1
# Converged Max Err/Tol 0.10000E+07
->Generating block results ...
Block: C2 Model: HEATER
->Simulation calculations completed ...
***Warning(s) were issued during Input Translation ***
***Check the Run Status Results for more Information ***
***Summary of Simulation Errors***
Physical
Property System Simulation
Terminal Errors 0 0 0
Severe Errors 0 0 1
Errors 0 0 0
Warnings 0 0 2
**ERROR WHILE GENERATING REPORT FOR STREAM: "3BOT"
FLASH CALCULATIONS BYPASSED DUE TO UNREASONABLE SPECIFICATIONS. SPECIFIED
TEMPERATURE (MISSING) IS HIGHER THAN THE UPPER LIMIT (1.0000D+04).
PROPERTIES WILL NOT BE CALCULATED DUE TO FLASH FAILURE.
**ERROR WHILE GENERATING REPORT FOR STREAM: "V"
FLASH CALCULATIONS BYPASSED DUE TO UNREASONABLE SPECIFICATIONS. SPECIFIED
TEMPERATURE (MISSING) IS HIGHER THAN THE UPPER LIMIT (1.0000D+04).
PROPERTIES WILL NOT BE CALCULATED DUE TO FLASH FAILURE.
attach://60535.bkp
可否告知一下反应动力学参数啊，这个找了很久找的不全 光看这个还真不好说，好像是塔顶少了一根进料物流 请问您的问题解决了没
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