模拟吸收塔时出现的问题,跪求大神解决。? 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 missing property parameters 查看更多0个回答 . 5人已关注