Phase equilibria of the binary systems 1-hexene with o-xylene, m-xylene, p-xylene, toluene, and ethylbenzene at 101.3 kPa

被引:22
作者
Díaz, C [1 ]
Dominguez, A [1 ]
Tojo, J [1 ]
机构
[1] Univ Vigo, Fac Ciencias, Dept Ingn Quim, Vigo 36200, Spain
关键词
D O I
10.1021/je010295b
中图分类号
O414.1 [热力学];
学科分类号
摘要
Isobaric vapor-liquid equilibria are measured for 1-hexene + o-xylene, + m-xylene, + p-xylene, + toluene, and + ethylbenzene at 101.3 kPa, using a dynamic still with circulation in both of the phases. The experimental data are tested for thermodynamic consistency and could be represented well by the Wilson and UNIQUAC equations, with the latter being far better. A comparative analysis of the application of the group contribution methods ASOG, original UNIFAC, modified UNIFAC-Dortmund, and modified UNIFAC-Lyngby to the mixtures of this study showed that UNIFAC-Lyngby gives better results.
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页码:867 / 871
页数:5
相关论文
共 26 条
[1]   STATISTICAL THERMODYNAMICS OF LIQUID-MIXTURES - NEW EXPRESSION FOR EXCESS GIBBS ENERGY OF PARTLY OR COMPLETELY MISCIBLE SYSTEMS [J].
ABRAMS, DS ;
PRAUSNITZ, JM .
AICHE JOURNAL, 1975, 21 (01) :116-128
[2]   Automatic implementation of thermodynamic models using computer algebra [J].
Castier, M .
COMPUTERS & CHEMICAL ENGINEERING, 1999, 23 (09) :1229-1245
[3]  
DAUBERT TE, 1986, PHYSICAL THERMODYNAM
[4]  
DIAZ C, 2001, THESIS U VIGO VIGO
[5]  
Fredenslund A., 1977, VAPOR LIQUID EQUILIB
[6]  
Gmehling, 1996, MANUAL DORTMUND DATA
[7]   A MODIFIED UNIFAC MODEL .2. PRESENT PARAMETER MATRIX AND RESULTS FOR DIFFERENT THERMODYNAMIC PROPERTIES [J].
GMEHLING, J ;
LI, JD ;
SCHILLER, M .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1993, 32 (01) :178-193
[8]   VAPOR-LIQUID-EQUILIBRIA BY UNIFAC GROUP CONTRIBUTION .5. REVISION AND EXTENSION [J].
HANSEN, HK ;
RASMUSSEN, P ;
FREDENSLUND, A ;
SCHILLER, M ;
GMEHLING, J .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1991, 30 (10) :2352-2355
[9]   GENERALIZED METHOD FOR PREDICTING 2ND VIRIAL-COEFFICIENTS [J].
HAYDEN, JG ;
OCONNELL, JP .
INDUSTRIAL & ENGINEERING CHEMISTRY PROCESS DESIGN AND DEVELOPMENT, 1975, 14 (03) :209-216
[10]   INTBIS, A PORTABLE INTERVAL NEWTON BISECTION PACKAGE [J].
KEARFOTT, RB ;
NOVOA, M .
ACM TRANSACTIONS ON MATHEMATICAL SOFTWARE, 1990, 16 (02) :152-157