Phase equilibria behaviour of n-heptane with o-xylene, m-xylene, p-xylene and ethylbenzene at 101.3kPa

被引:16
作者
Díaz, C [1 ]
Tojo, J [1 ]
机构
[1] Vigo Univ, Dept Chem Engn, Vigo 36200, Spain
关键词
vapour-liquid equilibria; activity coefficients; alkylbenzenes; n-heptane; group-contribution models;
D O I
10.1016/S0021-9614(02)00227-6
中图分类号
O414.1 [热力学];
学科分类号
摘要
Isobaric vapour-liquid equilibria were measured for the binary systems In-heptane + (o-xylene, m-xylene, p-xylene or ethylbenzene)l at 101.3 kPa using a dynamic method with circulation in both phases. In thermodynamic calculations using the data, the vapour phase was considered to be non-ideal, and activity coefficients of the components in the mixtures indicate positive deviations from Raoult's law. After reduction of the data and verification of thermodynamic consistency, various group-contribution models were applied to estimate the isobaric VLE data. (C) 2002 Elsevier Science Ltd. All rights reserved.
引用
收藏
页码:1975 / 1984
页数:10
相关论文
共 33 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]  
DAUBERT TE, 1986, PHYSICAL THERMODYNAM
[3]   Phase equilibria of the binary systems 1-hexene with o-xylene, m-xylene, p-xylene, toluene, and ethylbenzene at 101.3 kPa [J].
Díaz, C ;
Dominguez, A ;
Tojo, J .
JOURNAL OF CHEMICAL AND ENGINEERING DATA, 2002, 47 (04) :867-871
[4]   Isobaric vapor-liquid equilibria of the binary systems cyclohexane with ο-xylene, m-xylene, p-xylene, and ethylbenzene at 101.3 kPa [J].
Díaz, C ;
Tojo, J .
JOURNAL OF CHEMICAL AND ENGINEERING DATA, 2002, 47 (05) :1154-1158
[5]   Densities, refractive indices, and derived properties of (cyclohexane, or n-heptane plus an aromatic hydrocarbon) at T=298.15 K [J].
Díaz, C ;
Orge, B ;
Marino, G ;
Tojo, J .
JOURNAL OF CHEMICAL THERMODYNAMICS, 2001, 33 (09) :1015-1026
[6]  
DIAZPENA M, 1980, J CHEM THERMODYN, V12, P259
[7]  
DOMINGUEZ A, 2002, UNPUB COMPUT CHEM EN
[8]  
Fredenslund Aa., 1977, VAPOUR LIQUID EQUILI
[9]   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
[10]  
GMEHLING J, 1996, MANUAL DORMUND DATA