calculator计算遇到这个问题怎么解决

dfaz3011 · 发表于 2015-4-8 11:18:14

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