Rejection and modeling of arsenate by nanofiltration: Contributions of convection, diffusion and electromigration to arsenic transport

被引:70
作者
Fang, Jun [1 ]
Deng, Baolin [2 ]
机构
[1] Dist Columbia Water & Sewer Author, OMAP Programa, Washington, DC 20032 USA
[2] Univ Missouri, Dept Civil & Environm Engn, Columbia, MO 65211 USA
基金
美国国家科学基金会;
关键词
Arsenate; Nanofiltration; Transport; Convection; Diffusion; Electromigration; CADMIUM SALTS TRANSPORT; ELECTROLYTE TRANSPORT; DRINKING-WATER; CONCENTRATION POLARIZATION; MEMBRANE PERFORMANCE; AS(III) OXIDATION; SURFACE-WATER; REMOVAL; DIAFILTRATION; PREDICTION;
D O I
10.1016/j.memsci.2013.10.056
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Nanofiltration (NF) membranes, OK and DL, were characterized by attenuated total reflection Fourier transform infrared spectroscopy, out charge titration, pore size determination and salt rejection. The results showed both membranes have amide l and carbonyl groups on their surfaces, and have the same basic structure of polyamide layer sitting On the top of a polysullone layer. The DK membrane carries more negative charges in the entire pH range investigated. At rejections by the NF membranes were evaluated with a crossflow test setup. The effects of pH, ionic strength, operating pressure, arsenate initial concentration on the membrane performance were investigated. Mass transfer coefficients of the membranes were determined experimentally. The Donann Steric Pore Model and concentration polarization film theory were applied to calculate the arsenic rejection rate. The rejection mechanism was interpreted by calculating the contributions of convection, diffusion, and electrostatic migration to arsenic transport through the membranes. The calculated results showed that the contribution of diffusive transport dominated at low flux, and convection and electromigrative transport, especially the latter, play an increasingly important role at a high flux. (C) 2013 Elsevier B.V. All rights reserved.
引用
收藏
页码:42 / 51
页数:10
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