盐酸吸收塔模拟

2254474225 · 发表于 1970-1-1 08:00:00

* WARNING IN THE "STREAM" PARAGRAPH WHICH BEGINS ON LINE 183
   STREAM NAME: 11
   COMPONENT MASS FLOWS OF SUBSTREAM: "MIXED"
   ARE NORMALIZED TO THE TOTAL MASS FLOW VALUE.

  * WARNING IN THE "STREAM" PARAGRAPH WHICH BEGINS ON LINE 187
   STREAM NAME: 12
   COMPONENT MOLE FLOWS OF SUBSTREAM: "MIXED"
   ARE NORMALIZED TO THE TOTAL MOLE FLOW VALUE.

  * WARNING IN PHYSICAL PROPERTY SYSTEM
   NRTL BINARY PARAMETERS FOR ALL COMPONENT PAIRS ARE ZERO,
   YOUR RESULTS MAY NOT BE ACCURATE. PLEASE REVIEW AND PROVIDE BINARY
   PARAMETERS AS APPROPRIATE.

  Flowsheet Analysis :

COMPUTATION ORDER FOR THE FLOWSHEET:
B2

->Calculations begin ...

  * WARNING WHILE PERFORMING INITIAL ENTHALPY CALCULATIONS FOR STREAM: "12"

   LIQUID PHASE CALCULATIONS REQUESTED FOR A MIXTURE WHERE ALL COMPONENTS
   ARE DEFINED AS HENRY COMPONENTS (" GLOBAL "), YET AT LEAST ONE OF THEM IS
   SUB-CRITICAL (" HCL "). FLASH CALCULATIONS MAY BE INCORRECT.

Block: B2    Model: RADFRAC
   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
   HCL WITH ALL SOLVENTS:
      H2O

  ****PROPERTY PARAMETER ERROR
   ERRORS ENCOUNTERED IN CALCULATION OF LIQUID MIXTURE PROPS USING
   OPTION SET ELECNRTL FOR PHIMX,DPHIMX

! Calculations stopped because of missing  property parameters
想做一个盐酸填料塔模拟，但是老是出现问题，想问问大神们有没有解决办法

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