A UNIFAC model for phase equilibrium calculations in aqueous and nonaqueous sugar solutions

被引:54
作者
Spiliotis, N [1 ]
Tassios, D [1 ]
机构
[1] Natl Tech Univ Athens, Dept Chem Engn, Lab Thermodynam & Transport Phenomena, Athens 15780, Greece
关键词
model; solid/liquid equilibria; liquid/liquid equilibria; vapor/liquid equilibria; carbohydrate; aqueous solution; nonaqueous solution;
D O I
10.1016/S0378-3812(00)00387-3
中图分类号
O414.1 [热力学];
学科分类号
摘要
A UNIFAC type model is proposed to describe and predict phase equilibria in aqueous and nonaqueous sugar solutions. One new main UNIFAC group, CHOH(sugar), has been introduced to describe all monosaccharides. This main group contains three different subgroups, CH(2)OH, CHOH(axial) and CHOH(equatorial), which are introduced based on considerations of the actual saccharide ring forms in solution. UNIFAC interaction parameters between the new group and the CH(2); OH; H(2)O; CH(2)-O groups have been estimated from the solubility data of monosaccharides in water, alcohol and their binary solvent mixtures. Another UNIFAC main group, CH-O-CH, has been introduced to describe the disaccharide osidic bond. Interaction parameters between the new group and the CH(2); OH; H(2)O; CH(2)-O; CHOH(sugar) groups have been estimated too. The model gives very satisfactory correlation and prediction of solute activity properties (i.e. solubility and i-butanol/water partition coefficients of sugars are determined by the activity of the solute) as well as satisfactory prediction of solvent activity properties (i.e. bubble and freezing points are: determined by the activity of the solvent). A comparison with the UNIFAC model developed recently by Peres and Macedo [Fluid Phase Equil. 139 (1997) 47-74], which is the only other predictive model applicable to nonaqueous sugar solutions, suggests that both models provide similar results for aqueous sugar solutions, but the proposed model is more suitable for the prediction of phase equilibrium of sugar solutions involving also nonaqueous solvents as well as in such two-phase systems. (C) 2000 Elsevier Science B.V. All rights reserved.
引用
收藏
页码:39 / 55
页数:17
相关论文
共 43 条
[1]   MEASUREMENT AND MODELING OF ATMOSPHERIC-PRESSURE VAPOR-LIQUID-EQUILIBRIUM DATA FOR BINARY, TERNARY AND QUATERNARY MIXTURES OF SUCROSE, GLUCOSE, FRUCTOSE AND WATER COMPONENTS [J].
ABDERAFI, S ;
BOUNAHMIDI, T .
FLUID PHASE EQUILIBRIA, 1994, 93 :337-351
[2]   MEASUREMENT OF LIQUID SOLID-PHASE EQUILIBRIUM IN TERNARY-SYSTEMS OF WATER SUCROSE GLUCOSE AND WATER SUCROSE FRUCTOSE, AND PREDICTIONS WITH UNIFAC [J].
ABED, Y ;
GABAS, N ;
DELIA, ML ;
BOUNAHMIDI, T .
FLUID PHASE EQUILIBRIA, 1992, 73 (1-2) :175-184
[3]  
Achard C., 1992, Industries Alimentaires et Agricoles, V109, P93
[4]   APPLICATION OF UNIQUAC EQUATION TO CALCULATION OF MULTICOMPONENT PHASE-EQUILIBRIA .1. VAPOR-LIQUID-EQUILIBRIA [J].
ANDERSON, TF ;
PRAUSNITZ, JM .
INDUSTRIAL & ENGINEERING CHEMISTRY PROCESS DESIGN AND DEVELOPMENT, 1978, 17 (04) :552-561
[5]   The vapour pressure of saturated aqueous solutions of D(+)-glucose, D(+)-galactose, and β-lactose at temperatures from T = 278 K to T = 318 K [J].
Apelblat, A ;
Korin, E .
JOURNAL OF CHEMICAL THERMODYNAMICS, 1998, 30 (10) :1263-1269
[6]   EXCESS PROPERTIES AND SOLID-LIQUID EQUILIBRIA FOR AQUEOUS-SOLUTIONS OF SUGARS USING A UNIQUAC MODEL [J].
CATTE, M ;
DUSSAP, CG ;
ACHARD, C ;
GROS, JB .
FLUID PHASE EQUILIBRIA, 1994, 96 :33-50
[7]   Investigation of keys parameters of fructose oleate enzymatic synthesis catalyzed by an immobilized lipase [J].
Coulon, D ;
Girardin, M ;
Engasser, JM ;
Ghoul, M .
INDUSTRIAL CROPS AND PRODUCTS, 1997, 6 (3-4) :375-381
[8]  
DAUBERT T, 1989, DIPPR TABLES PHYSICA
[9]  
DURRETTE PL, 1971, ADV CARBOHYD CHEM BI, V26, P49
[10]   Refractive index, viscosity, density, and solubility in the system fructose plus ethanol plus water at 30, 40, and 50 degrees C [J].
Flood, AE ;
Addai-Mensah, J ;
Johns, MR ;
White, ET .
JOURNAL OF CHEMICAL AND ENGINEERING DATA, 1996, 41 (03) :418-421