Trace organic solutes in closed-loop forward osmosis applications: Influence of membrane fouling and modeling of solute build-up

被引:81
作者
D'Haese, Arnout [1 ]
Le-Clech, Pierre [2 ]
Van Nevel, Sam [3 ]
Verbeken, Kim [4 ]
Cornelissen, Emile R. [5 ]
Khan, Stuart J. [6 ]
Verliefde, Arne R. D. [1 ,7 ]
机构
[1] Univ Ghent, Particle & Interfacial Technol Grp, B-9000 Ghent, Belgium
[2] UNSW Sydney, UNESCO Ctr Membrane Sci & Technol, Sydney, NSW 2052, Australia
[3] Univ Ghent, Lab Microbial Ecol & Technol, B-9000 Ghent, Belgium
[4] Univ Ghent, Dept Mat Sci & Engn, B-9052 Zwijnaarde, Belgium
[5] KWR Watercycle Inst, NL-3433 PE Nieuwegein, Netherlands
[6] UNSW Sydney, Sch Civil & Environm Engn, Sydney, NSW 2052, Australia
[7] Delft Univ Technol, Dept Sanit Engn, NL-2628 CN Delft, Netherlands
关键词
Forward osmosis; Organic micro pollutant; Membrane fouling; Biofilm; Modeling; ENDOCRINE DISRUPTION; TREATMENT PLANTS; REJECTION; NANOFILTRATION; PHARMACEUTICALS; REMOVAL; CONTAMINANTS; PERFORMANCE; TRANSPORT; WATER;
D O I
10.1016/j.watres.2013.06.006
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
In this study, trace organics transport in closed-loop forward osmosis (FO) systems was assessed. The FO systems considered, consisted of an FO unit and a nanofiltration (NF) or reverse osmosis (RO) unit, with the draw solution circulating between both units. The rejection of trace organics by FO, NF and RO was tested. It was found that the rejection rates of FO were generally comparable with NF and lower than RO rejection rates. To assess the influence of fouling in FO on trace organics rejection, FO membranes were fouled with sodium alginate, bovine serum albumin or by biofilm growth, after which trace organics rejection was tested. A negative influence of fouling on FO rejection was found which was limited in most cases, while it was significant for some compounds such as paracetamol and naproxen, indicating specific compound-foulant interactions. The transport mechanism of trace organics in FO was tested, in order to differentiate between diffusive and convective transport. The concentration of trace organics in the final product water and the build-up of trace organics in the draw solution were modeled assuming the draw solution was reconcentrated by NF/RO and taking into account different transport mechanisms for the FO membrane and different rejection rates by NF/RO. Modeling results showed that if the FO rejection rate is lower than the RO rejection rate (as is the case for most compounds tested), the added value of the FO-RO cycle compared to RO only at steady-state was small for diffusively and negative for convectively transported trace organics. Modeling also showed that trace organics accumulate in the draw solution. (C) 2013 Elsevier Ltd. All rights reserved.
引用
收藏
页码:5232 / 5244
页数:13
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