Solute Coupled Diffusion in Osmotically Driven Membrane Processes

被引:374
作者
Hancock, Nathan T. [1 ]
Cath, Tzahi Y. [1 ]
机构
[1] Colorado Sch Mines, Div Environm Sci & Engn, Golden, CO 80401 USA
关键词
AMMONIA-CARBON DIOXIDE; OSMOSIS; PRESSURE; DESALINATION; PERFORMANCE; REUSE;
D O I
10.1021/es901132x
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
Forward osmosis (FO) is an emerging water treatment technology with potential applications in desalination and wastewater reclamation. In FO, water is extracted from a feed solution using the high osmotic pressure of a hypertonic solution that flows on the opposite side of a semipermeable membrane; however, solutes diffuse simultaneously through the membrane in both directions and may jeopardize the process. In this study, we have comprehensively explored the effects of different operating conditions on the forward diffusion of solutes commonly found in brackish water and seawater, and reverse diffusion of common draw solution solutes. Results show that reverse transport of solutes through commercially available FO membranes range between 80 mg to nearly 3,000 mg per liter of water produced. Divalent feed solutes have low permeation rates (less than 1 mmol/m(2)-hr) while monovalent ions and uncharged solutes exhibit higher permeation. Findings have significant implications on the performance and sustainability of the FO process.
引用
收藏
页码:6769 / 6775
页数:7
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