盐酸吸收塔模拟
* WARNING IN THE "STREAM" PARAGRAPH WHICH BEGINS ON LINE 183STREAM 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 missingproperty 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 这是没成功？ 参考CO2吸收塔计算即可！ {:1110_550:} 学习，已保存 已学习，谢谢楼主分享 可以年地看看一下{:1110_553:} {:1110_549:} fdas dfsa fdsa fdas fdas fdsa
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