Determination and calculation for solubility of m-nitroaniline and its mixture in supercritical carbon dioxide

被引:7
作者
Zhu, Jing [1 ]
Li, Mengxi [1 ]
Zhang, Haifei [2 ]
Ning, Yanying [1 ]
Jin, Junsu [1 ]
机构
[1] Beijing Univ Chem Technol, Coll Chem Engn, Beijing Key Lab Membrane Sci & Technol, Beijing 100029, Peoples R China
[2] Univ Liverpool, Dept Chem, Liverpool L69 7ZD, Merseyside, England
基金
中国国家自然科学基金;
关键词
Solid mixture solubility; m-Nitroaniline; p-Nitroaniline; Supercritical carbon dioxide; Model; SOLIDS; ACID; LIQUIDS;
D O I
10.1016/j.cherd.2014.04.019
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Equilibrium solubility of m-nitroaniline and p-nitroaniline in supercritical carbon dioxide (SCCO2) is essential to design the process of SCCO2 extraction and to investigate the effect of each solute on the solubility in SCCO2 ternary system. However, the solubility data is not reported so far. We performed the solubility measurements at the temperatures of 308-328 K and in the pressure range of 11.0-21.0 MPa. The experimental results showed the solubility of m-nitroaniline and p-nitroaniline was enhanced in m-nitroaniline +p-nitroaniline +SCCO2 ternary system. The improvement factor (i), separation factor (mu) and separation efficiency (HE) in the ternary system were defined and calculated, and the best separation result could be obtained at 21.0 MPa and 328 K using SCCO2 extraction, where the separation efficiency was up to 90.9%. Based on the chemical association theory, a new model was developed to calculate the solubility of mixed solutes in SCCO2. The correlation result of the new model was tested by about 500 solubility data from 15 kinds of two solutes mixtures in SCCO2. The correlated result showed that the new model could achieve much better AARD (%) than those of frequently used Sovova and Sovova-T models. (C) 2014 The Institution of Chemical Engineers. Published by Elsevier B.V. All rights reserved.
引用
收藏
页码:2806 / 2813
页数:8
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