calculator计算遇到这个问题怎么解决? 模拟煤气化,动不了了,求指教 Calculator Block C-1 Block: DEC Model: RSTOIC INFORMATION ELEMENT NO. 2 IN ATTRIBUTE ULTANAL IS SET TO ZERO. VALUE IS MISSING IN COMP-ATTR FORM AND IN INLET STREAM. INFORMATION ELEMENT NO. 3 IN ATTRIBUTE ULTANAL IS SET TO ZERO. VALUE IS MISSING IN COMP-ATTR FORM AND IN INLET STREAM. INFORMATION ELEMENT NO. 4 IN ATTRIBUTE ULTANAL IS SET TO ZERO. VALUE IS MISSING IN COMP-ATTR FORM AND IN INLET STREAM. INFORMATION ELEMENT NO. 5 IN ATTRIBUTE ULTANAL IS SET TO ZERO. VALUE IS MISSING IN COMP-ATTR FORM AND IN INLET STREAM. INFORMATION ELEMENT NO. 6 IN ATTRIBUTE ULTANAL IS SET TO ZERO. VALUE IS MISSING IN COMP-ATTR FORM AND IN INLET STREAM. INFORMATION ELEMENT NO. 7 IN ATTRIBUTE ULTANAL IS SET TO ZERO. VALUE IS MISSING IN COMP-ATTR FORM AND IN INLET STREAM. EQUATION OF STATE MODEL ESPR HAS MISSING PARAMETERS: TCPR AND ITS DEFAULT TC (DATA SET 1) MISSING FOR COMPONENT O2 PCPR AND ITS DEFAULT PC (DATA SET 1) MISSING FOR COMPONENT O2 OMGPR AND ITS DEFAULT OMEGA (DATA SET 1) MISSING FOR COMPONENT O2 ** ERROR IN PHYSICAL PROPERTY SYSTEM VAPOR ROOT NOT CONVERGED IN EOS MODEL ESPR T= 1673. K, SPECIFIED P= 0.1000E+06 N/SQM, CALCULATED P= -0.4171E-05 N/SQM EQUATION OF STATE MODEL ESPR FAILED DUE TO INFEASIBLE CONDITIONS (DATA SET 1) AT TEMPERATURE 0.167E+04K AND PRESSURE 0.100E+06 PA. COMPONENT MOLE FRACTION COMPONENT MOLE FRACTION CO 0.1221 CO2 0.1221 H2 0.1221 N2 0.1221 O2 0.1644E-01 H2O 0.2078 H2S 0.1221 C 0.4326E-01 S 0.1221 ****PROPERTY PARAMETER ERROR ERRORS ENCOUNTERED IN CALCULATION OF VAPOR-LIQUID K-VALUES USING OPTION SET PR-BM FOR KVL ! Calculations stopped because of missing property parameters 查看更多0个回答 . 4人已关注