Calculation of Vapor-Liquid Equilibria for Systems of n- and iso-butanol Purification Process by UNIFAC——Supplement of Group Interaction Parameters,a_(CCON,CHO. ) and a_(CHO,CCOH)
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Calculation of Vapor-Liquid Equilibria for Systems of n- and iso-butanol Purification Process by UNIFAC——Supplement of Group Interaction Parameters,a_(CCON,CHO. ) and a_(CHO,CCOH)
CIESC JournalIssue 2, (1981)
作者机构:
北京化工学院化学工程系
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Online First:25 June 1981,
Published:25 June 1981
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金彰礼. Calculation of Vapor-Liquid Equilibria for Systems of n- and iso-butanol Purification Process by UNIFAC——Supplement of Group Interaction Parameters,a_(CCON,CHO. ) and a_(CHO,CCOH)[J]. CIESC Journal, 1981, (2).
DOI:
金彰礼. Calculation of Vapor-Liquid Equilibria for Systems of n- and iso-butanol Purification Process by UNIFAC——Supplement of Group Interaction Parameters,a_(CCON,CHO. ) and a_(CHO,CCOH)[J]. CIESC Journal, 1981, (2).DOI:
Calculation of Vapor-Liquid Equilibria for Systems of n- and iso-butanol Purification Process by UNIFAC——Supplement of Group Interaction Parameters,a_(CCON,CHO. ) and a_(CHO,CCOH)
has been supplemented from experimental vapor-liquid equilibrium data of iso-butanol iso-butaldehyde system available from literature[5]. The UNIFAC method has heen used in phase equilibrium calculations for systems of n-and iso-butanol purification process with accuracy approaching or attaining that of results calculated by NRTL and other correlations. In view of the fact that the UNIFAC method is based upon the assumption of additive property of group properties
it is necessary to check the calculating results with a few experimental data and to make appropriate choice of the available group parameters.