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. https://bbs.mahoupao.net/forum.php?mod=attachment&aid=NjA1MzV8NDc5OThmNWU1MmE5MDIyN2ExNDMxZDhhNWFlMWJmM2R8MTUyMzU1Mjg4Nw%3D%3D&request=yes&_f=.bkp
