Department of Chemical Engineering, University of Engineering and Technology, P.O. Box 814, University Campus, Peshawar, 25120, Pakistan.
Faculty of Chemical and Materials Engineering, Shahrood University of Technology, Shahrood, Iran.
Environ Sci Pollut Res Int. 2018 Apr;25(12):12053-12063. doi: 10.1007/s11356-018-1282-1. Epub 2018 Jan 27.
This study presents computational fluid dynamics (CFD) simulation of dispersion-free liquid-liquid extraction of copper(II) with trifluoroacetylacetone (TFA) in hollow fiber membrane contactor (HFMC). Mass and momentum balance Navier-Stokes equations were coupled to address the transport of copper(II) solute across membrane contactor. Model equations were simulated using COMSOL Multiphysics™. The simulation was run to study the detailed concentration distribution of copper(II) and to investigate the effects of various parameters like membrane characteristics, partition coefficient, and flow configuration on extraction efficiency. Once-through extraction was found to be increased from 10 to 100% when partition coefficient was raised from 1 to 10. Similarly, the extraction efficiency was almost doubled when porosity to tortuosity ratio of membrane was increased from 0.05 to 0.81. Furthermore, the study revealed that CFD can be used as an effective optimization tool for the development of economical membrane-based dispersion-free extraction processes.
本研究采用计算流体动力学(CFD)模拟无分散型中空纤维膜接触器(HFMC)中三氟乙酰丙酮(TFA)萃取铜(II)的过程。质量和动量平衡纳维-斯托克斯方程被耦合在一起,以解决铜(II)溶质在膜接触器中的传输问题。模型方程使用 COMSOL Multiphysics™进行模拟。该模拟旨在研究铜(II)的详细浓度分布,并研究各种参数(如膜特性、分配系数和流动配置)对萃取效率的影响。当分配系数从 1 增加到 10 时,一次通过萃取从 10%增加到 100%。同样,当膜的孔隙率与曲折度比从 0.05 增加到 0.81 时,萃取效率几乎增加了一倍。此外,该研究表明,CFD 可以用作经济的无膜分散萃取过程开发的有效优化工具。