Mass Transfer Simulation of Gold Extraction in Membrane Extractors

被引:38
作者
Ghadiri, Mehdi [1 ]
Shirazian, Saeed [1 ]
Ashrafizadeh, Seyed N. [1 ]
机构
[1] Iran Univ Sci & Technol, Res Lab Adv Separat Proc, Dept Chem Engn, Tehran 1684613114, Iran
关键词
Mass Transfer; Membrane contactor; Simulation; Solvent extraction; SOLVENT-EXTRACTION; CONTACTORS; AU(CN)(2)(-); TRANSPORT; RECOVERY; CYANIDE;
D O I
10.1002/ceat.201200289
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
The extraction of gold in membrane extractors was theoretically investigated. Extraction of gold in the form of Au(CN)(2)(-) in a solution of n-heptane and synergistic extractants of LIX79+TOPO was studied. The membrane extractor consists of three sections: the tube side, the membrane, and the shell side. Conservation equations were derived for Au(CN)(2)(-) in the membrane module and were numerically solved based on finite element method. Simulations were conducted through solving the momentum and mass transfer equations simultaneously. It was indicated that as the feed flows within the tube side, it moves into the membrane due to the concentration difference, and then gets swept by the moving extractants within the shell side. The distribution of solute concentration in the membrane contactor was obtained. Simulation results showed increasing the feed flow rate reduces the extraction efficiency, while doing the same for the organic phase flow rate does not change the extraction efficiency.
引用
收藏
页码:2177 / 2182
页数:6
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