Liquid-liquid equilibria for pseudoternary systems:: isooctane-benzene-(methanol plus water)

被引:18
作者
García-Flores, BE
de Doz, MG
Trejo, A
机构
[1] Inst Mexicano Petr, Programa Ingn Mol, Ciencias Basicas, Mexico City 07730, DF, Mexico
[2] Area Invest Termofis, Mexico City 07730, DF, Mexico
关键词
experiments; hydrocarbons; isowater curves; liquid-liquid equilibrium; methanol; tie-lines;
D O I
10.1016/j.fluid.2004.12.003
中图分类号
O414.1 [热力学];
学科分类号
摘要
Liquid-liquid equilibrium data are presented for the pseudoternary systems isooctane-benzene-(90 mass% methanol + 10 mass% water) at 298.15 K and isooctane-benzene-(80 mass% methanol + 20 mass% water) at 298.15 and 308.15 K, under atmospheric pressure. The experimental tie-line data obtained define the binodal curve for each one of the studied systems which depending on the amount of water present show type I or type II liquid-liquid phase diagrams. In order to obtain a general view of the effect of water on the partitioning of methanol and hence on the size of the two-phase region we have also determined experimentally 'isowater' tolerance curves for the system isooctane-benzene-methanol at 298.15 K, hence the tie-line data were also obtained for the ternary system. The experimental tie-line data for the four systems studied were correlated with the NRTL and UNIQUAC solution models obtaining a very good reproduction of the experimental behaviour. (c) 2004 Elsevier B.V. All rights reserved.
引用
收藏
页码:121 / 130
页数:10
相关论文
共 21 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]   Liquid-liquid equilibria of water plus MTBE plus reformate [J].
Alkandary, JA ;
Ajimaz, AS ;
Fandary, MS ;
Fahim, MA .
FLUID PHASE EQUILIBRIA, 2001, 187 :131-138
[3]  
ANCILLOTTI F, 1971, HYDROCARB PROCESS, P295
[4]  
BARKER LE, 1982, SOC PET ENG J, V22, P731
[5]   Effect of temperature on liquid-liquid equilibrium - Benzene-acetone-water system and docosane-1,6-diphenylhexane-furfural system [J].
Briggs, SW ;
Comings, EW .
INDUSTRIAL AND ENGINEERING CHEMISTRY, 1943, 35 :411-417
[6]  
de Doz MBG, 2003, FLUID PHASE EQUILIBR, V205, P53
[7]   Liquid-liquid phase diagrams of ternary systems as a function of temperature:: isooctane plus aromatic plus methanol with and without water [J].
García-Flores, BE ;
Galicia-Aguilar, G ;
Eustaquio-Rincón, R ;
Trejo, A .
FLUID PHASE EQUILIBRIA, 2001, 185 (1-2) :275-293
[8]  
GARCIASANCHEZ F, 1977, REV MEX FIS, V43, P59
[9]   LIQUID-LIQUID EQUILIBRIA OF FUEL OXYGENATE PLUS WATER PLUS HYDROCARBON MIXTURES .2. [J].
HELLINGER, S ;
SANDLER, SI .
JOURNAL OF CHEMICAL AND ENGINEERING DATA, 1995, 40 (01) :321-325
[10]   MEASUREMENT AND CORRELATION OF LIQUID LIQUID EQUILIBRIA OF METHANOL ALKANE AROMATIC COMPOUND TERNARY-SYSTEMS [J].
HIGASHIUCHI, H ;
SAKURAGI, Y ;
ARAI, Y ;
NAGATANI, M .
FLUID PHASE EQUILIBRIA, 1990, 58 (1-2) :147-157