CSTR模拟结果出错。。。? 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 << Run Saved >> 查看更多2个回答 . 3人已关注