Correlation and prediction for isobaric vapor-liquid equilibria of the diethyl ether + methanol + 1-butanol ternary system and the constituent binary systems at 101.325 kPa

Industrial and Engineering Chemistry Research

Volumn 51, Issue 1, 2012, Pages 567-575

  Gao, Daming ^a,b   Zhang, Hui ^a,b   Zhu, Dechun ^a,b   Sun, Hong ^a,b   Chen, Hong ^a   Shi, Jianjun ^a,b   Lücking, Peter ^b,c   Winter, Bernhard ^b,c   Zhan, Yamei ^c  

^a HEFEI UNIVERSITY   (China)

^b Sino German Research Center for Process Engineering and Energy Technology   (China)

^c JADE UNIVERSITY OF APPLIED SCIENCES   (Germany)

Author keywords

[No Author keywords available]

Indexed keywords

1-BUTANOL; BINARY INTERACTION PARAMETER; BINARY SYSTEMS; BUBBLE POINTS; CORRELATION AND PREDICTION; DIETHYL ETHERS; EXPERIMENTAL DATA; GROUP CONTRIBUTION METHOD; ISOBARIC VAPOR-LIQUID EQUILIBRIUM; LEAST SQUARES METHODS; LIQUID PHASE COMPOSITIONS; MODEL PARAMETERS; NON RANDOM TWO LIQUIDS; THERMODYNAMIC CONSISTENCY; UNIQUAC; UNIQUAC MODELS; UNIVERSAL QUASI CHEMICALS; VAPOR PHASE COMPOSITIONS; VAPOR-LIQUID EQUILIBRIUM; VLE DATA;

ACTIVITY COEFFICIENTS; BINARY MIXTURES; ETHERS; LEAST SQUARES APPROXIMATIONS; LIQUIDS; METHANOL; ORGANIC COMPOUNDS; PHASE COMPOSITION; TERNARY SYSTEMS; VAPORS;

PHASE EQUILIBRIA;

EID: 84862919387     PISSN: 08885885     EISSN: 15205045     Source Type: Journal    
DOI: 10.1021/ie201805m     Document Type: Article

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