良人青衣 发表于 2017-5-23 20:06:01

脱硫塔遇到的问题,跪求大神帮助

Processing input specifications ...
      INFORMATION
      THERE ARE HENRY COMPONENTS DEFINED IN THIS CASE, THE BINARY DATABANK
      WILL BE SEARCHED AUTOMATICALLY FOR ANY AVAILABLE HENRY CONSTANTS.
      THE PAIR PARAMETERS FOR ELECNRTL OPTION SET HAS BEEN RETRIEVED FROM
      DATABANK ENRTL-RK.
      INFORMATION
      PURE COMPONENT PARAMETERS FOR SOME COMPONENTS ARE RETRIEVED FROM
      DATABANK.THESE PARAMETERS ARE USED WITH THE ELECNRTL OPTION SET
      UNLESS YOU ENTER YOUR OWN PARAMETERS IN PROP-DATA PARAGRAPHS.
      PARAMETER PLXANT RETRIEVED FOR COMPONENT H2O
      PARAMETER THRSWT(ELEMENT/3) RETRIEVED FOR COMPONENT H2O
*   WARNING IN PHYSICAL PROPERTY SYSTEM
      PARAMETER PLXANT (DATA SET 1) FOR COMPONENT NAOH:
      UNREASONABLE VAPOR PRESSURE CALCULATED AT NORMAL BOILING POINT.
      VALUE SHOULD BE WITHIN 10% OF 1D5 N/SQM.PLEASE CHECK YOUR INPUT
      FOR THE ANTOINE PARAMETERS.
Flowsheet Analysis :
COMPUTATION ORDER FOR THE FLOWSHEET:
B1
->Calculations begin ...
      WATSON HEAT OF VAPORIZATION MODEL HAS MISSING PARAMETERS:
      DHVLWT/1ST ELEMENT (DATA SET 1) MISSING FOR COMPONENT NAOH
      DHVLWT/2ND ELEMENT (DATA SET 1) MISSING FOR COMPONENT NAOH
****PROPERTY PARAMETER ERROR
      ERRORS ENCOUNTERED IN CALCULATION OF IDEAL GAS PROPS FOR
      HIG
      PLEASE FIX THE ERRORS, RE-INITIALIZE, AND RUN AGAIN.
! Calculations stopped because of missingproperty parameters
- 本文出自马后炮化工-让天下没有难学的化工技术,原文地址:http://meng.horse/thread-167782-1-1.html
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