Binary and ternary solid-liquid phase equilibrium for the systems formed by succinic acid, urea and diethylene glycol: Determination and modelling

被引:9
作者
Li, Yanxun [1 ]
Li, Congcong [1 ]
Han, Shuo [2 ]
Zhao, Hongkun [2 ]
机构
[1] Henan Inst Engn, Mat & Chem Engn Coll, Zhengzhou 450007, Henan, Peoples R China
[2] YangZhou Univ, Sch Chem & Chem Engn, Yangzhou 225002, Jiangsu, Peoples R China
基金
中国国家自然科学基金;
关键词
Solid-liquid phase equilibrium; Phase diagram; Succinic acid; Urea; Diethylene glycol; NRTL model; 9; ORGANIC-SOLVENTS; SOLUBILITY DETERMINATION; PLUS WATER; 318.15; K; MIXING PROPERTIES; TEMPERATURES; MIXTURES; ETHANOL;
D O I
10.1016/j.jct.2017.01.010
中图分类号
O414.1 [热力学];
学科分类号
摘要
In this work, the solid-liquid phase equilibrium for binary system of succinic acid + diethylene glycol at the temperatures ranging from (298.15 to 333.15) K and ternary system of (succinic acid + urea + diethylene glycol) at 298.15 K, 313.15 K and 333.15 K was built by using the isothermal saturation method under atmospheric pressure (101.2 kPa), and the solubilities were determined by a high-performance liquid chromatography. The solid-phases formed in the ternary system of ((succinic acid + urea + diethylene glycol)) were confirmed by Schreinemaker's method of wet residue, which corresponded to urea, succinic acid, and adduct 2:1 urea-succinic acid (mole ratio). Three isothermal phase diagrams for the ternary system were constructed based on the measured mutual solubility. Each isothermal phase diagram included six crystallization fields, three invariant curves, two invariant points and two co-saturated points. The crystalline region of adduct 2:1 urea-succinic acid is larger than those of the other two solids. The solubility of succinic acid in diethylene glycol was correlated with the modified Apelblat equation, nth equation and NRTL model; and the mutual solubility of the ternary ((succinic acid + urea + diethylene glycol)) system was correlated and calculated by the NRTL model. The interaction parameters' values of succinic acid-urea were acquired. The value of RMSD was 7.11 x 10(-3) for the ternary system. The calculation results had good agreement with the experiment values. Furthermore, the densities of equilibrium liquid phase were acquired. The phase diagrams and the thermodynamic model of the ternary system could provide the basis for design of the adductive crystallization process which was used to separate succinic acid with high purity from dicarboxylic acid mixtures. (C) 2017 Elsevier Ltd.
引用
收藏
页码:97 / 104
页数:8
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