Effect of draw solution concentration and operating conditions on forward osmosis and pressure retarded osmosis performance in a spiral wound module

被引:285
作者
Xu, Yuan [2 ]
Peng, Xiaoyu [2 ]
Tang, Chuyang Y. [1 ,3 ]
Fu, Q. Shiang [4 ]
Nie, Shengzhe [2 ]
机构
[1] Nanyang Technol Univ, Dept Civil & Environm Engn, Sch Civil & Environm Engn, Singapore 639798, Singapore
[2] Sichuan Univ, Suzhou Inst, Environm & Clean Technol Lab, Suzhou, Peoples R China
[3] Nanyang Technol Univ, Singapore Membrane Technol Ctr, Singapore 639798, Singapore
[4] Chinese Acad Sci, Nanjing Inst Geog & Limnol, Nanjing, Peoples R China
关键词
Forward osmosis (FO); Pressure retarded osmosis (PRO); Reverse osmosis (RO); Internal concentration polarization (ICP); Osmotic driving force; AMMONIA-CARBON DIOXIDE; INTERNAL CONCENTRATION POLARIZATION; ENHANCED CONCENTRATION POLARIZATION; COMPOSITE POLYAMIDE RO; OSMOTIC POWER-PLANTS; REVERSE-OSMOSIS; PHYSIOCHEMICAL PROPERTIES; MEMBRANE BIOREACTORS; COATING LAYER; WASTE-WATER;
D O I
10.1016/j.memsci.2009.11.013
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Forward osmosis (FO) and pressure retarded osmosis (PRO) are concentration-driven membrane processes. While they can be potentially used in water, wastewater, and energy applications, these processes suffer from the concentration polarization inside the porous membrane support resulting in severe flux decrease, a phenomenon known as internal concentration polarization (ICP). Researchers have investigated the effect of ICP both in theoretical and experimental studies. The current study extends the existing ICP model to include the effect ofdraw solution dilution by membrane permeate flow in a spiral wound FO module (SWFO). FO and PRO experiments were performed using a Hydrowell (R) SWFO under both submerged and cross-flow conditions. The effect ofdraw solution concentration, draw solution flow rate, feed water flow rate, and membrane orientation on FO and PRO water flux performance was systematically investigated. Permeate flow increased with greater draw solution concentration in both FO and PRO modes. ICP was found to drastically limit the available membrane flux in the concentration-driven membrane processes, and its adverse effect was more severe at greater draw solution concentration. Membrane flux was also affected by the dilution ofdraw solution when the permeate flow rate was comparable or greater than the draw solution flow rate. The submerged FO configuration performed nearly as good as the cross-flow configuration with feed water circulating outside of the membrane envelope (shorter flow path). In this case, the feed water flow rate only had limited effect on membrane flux likely due to its low mass transfer resistance. In contrary, the membrane flux can be adversely affected at low feed water flow rate when it was circulated inside of the membrane envelope (longer flow path). (C) 2009 Elsevier B.V. All rights reserved.
引用
收藏
页码:298 / 309
页数:12
相关论文
共 40 条
[1]  
Aaberg R.J., 2003, Refocus, V4, P48, DOI DOI 10.1016/S1471-0846(04)00045-9
[2]   Power generation with pressure retarded osmosis: An experimental and theoretical investigation [J].
Achilli, Andrea ;
Cath, Tzahi Y. ;
Childress, Amy E. .
JOURNAL OF MEMBRANE SCIENCE, 2009, 343 (1-2) :42-52
[3]   Ultrafiltration of natural organic matter [J].
Aoustin, E ;
Schäfer, AI ;
Fane, AG ;
Waite, TD .
SEPARATION AND PURIFICATION TECHNOLOGY, 2001, 22-3 (1-3) :63-78
[4]   A unifying model for concentration polarization, gel-layer formation and particle deposition in cross-flow membrane filtration of colloidal suspensions [J].
Bacchin, P ;
Si-Hassen, D ;
Starov, V ;
Clifton, MJ ;
Aimar, P .
CHEMICAL ENGINEERING SCIENCE, 2002, 57 (01) :77-91
[5]   Design considerations for wastewater treatment by reverse osmosis [J].
Bartels, CR ;
Wilf, M ;
Andes, K ;
Iong, J .
WATER SCIENCE AND TECHNOLOGY, 2005, 51 (6-7) :473-482
[6]   Performance advancement in the spiral wound RO/NF element design [J].
Bartels, Craig ;
Hirose, Masahiko ;
Fujioka, Hiroki .
DESALINATION, 2008, 221 (1-3) :207-214
[7]  
Bennett A, 2003, FILTR SEPARAT, V40, P20
[8]   Membrane contactor processes for wastewater reclamation in space II. Combined direct osmosis, osmotic distillation, and membrane distillation for treatment of metabolic wastewater [J].
Cath, TY ;
Adams, D ;
Childress, AE .
JOURNAL OF MEMBRANE SCIENCE, 2005, 257 (1-2) :111-119
[9]   Forward osmosis: Principles, applications, and recent developments [J].
Cath, Tzahi Y. ;
Childress, Amy E. ;
Elimelech, Menachem .
JOURNAL OF MEMBRANE SCIENCE, 2006, 281 (1-2) :70-87
[10]   Implications of critical flux and cake enhanced osmotic pressure (CEOP) on colloidal fouling in reverse osmosis: Experimental observations [J].
Chong, T. H. ;
Wong, F. S. ;
Fane, A. G. .
JOURNAL OF MEMBRANE SCIENCE, 2008, 314 (1-2) :101-111