Concentration polarization model of spiral-wound membrane modules with application to batch-mode RO desalination of brackish water

被引:46
作者
Qiu, T. Y. [1 ]
Davies, P. A. [1 ]
机构
[1] Aston Univ, Sch Engn & Appl Sci, Sustainable Environm Res Grp, Birmingham B4 7ET, W Midlands, England
关键词
Batch-mode reverse osmosis (batch-RU); Solar; High recovery; Concentration polarization (CP); Spiral-wound membrane (SWM); Mass transfer; OF-THE-ART; POWERED REVERSE-OSMOSIS; ORGANIC RANKINE-CYCLE; HIGH-RECOVERY; ULTRAFILTRATION MEMBRANES; NANOFILTRATION MEMBRANES; SHERWOOD CORRELATIONS; SALT REJECTION; TRANSPORT; SYSTEM;
D O I
10.1016/j.desal.2014.12.048
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Batch-mode reverse osmosis (batch-RU) operation is considered a promising desalination method due to its low energy requirement compared to other RO system arrangements. To improve and predict batch-RO performance, studies on concentration polarization (CP) are carried out. The Kimura-Sourirajan mass-transfer model is applied and validated by experimentation with two different spiral-wound RO elements. Explicit analytical Sherwood correlations are derived based on experimental results. For batch-RO operation, a new genetic algorithm method is developed to estimate the Sherwood correlation parameters, taking into account the effects of variation in operating parameters. Analytical procedures are presented, then the mass transfer coefficient models are developed for different operation processes, i.e., batch-RO and continuous RO. The CF related energy loss in batch-RO operation is quantified based on the resulting relationship between feed flow rates and mass transfer coefficients. It is found that CP increases energy consumption in batch-RO by about 25% compared to the ideal case in which CF is absent. For continuous RO process, the derived Sherwood correlation predicted CP accurately. In addition, we determined the optimum feed flow rate of our batch-RO system. (C) 2015 Elsevier B.V. All rights reserved.
引用
收藏
页码:36 / 47
页数:12
相关论文
共 34 条
[1]  
[Anonymous], 2024, P INT SCI CONFERENCE
[2]   Solute transport in solvent-resistant nanofiltration membranes for non-aqueous systems: experimental results and the role of solute-solvent coupling [J].
Bhanushali, D ;
Kloos, S ;
Bhattacharyya, D .
JOURNAL OF MEMBRANE SCIENCE, 2002, 208 (1-2) :343-359
[3]  
Bird RB, 2007, TRANSPORT PHENOMENA, DOI [10.4236/jsea.2020.138011, DOI 10.4236/JSEA.2020.138011]
[4]   CONCENTRATION POLARIZATION IN REVERSE OSMOSIS DESALINATION WITH VARIABLE FLUX AND INCOMPLETE SALT REJECTION [J].
BRIAN, PLT .
INDUSTRIAL & ENGINEERING CHEMISTRY FUNDAMENTALS, 1965, 4 (04) :439-&
[5]   Water and ions transport mechanism in hyperfiltration with symmetric cellulose acetate membranes [J].
Chaudry, MA .
JOURNAL OF MEMBRANE SCIENCE, 2002, 206 (1-2) :319-332
[6]  
Cussler E. L., 2009, Diffusion: Mass transfer in fluid systems
[7]   A solar-powered reverse osmosis system for high recovery of freshwater from saline groundwater [J].
Davies, P. A. .
DESALINATION, 2011, 271 (1-3) :72-79
[8]   Closed circuit desalination series no-5: high recovery, reduced fouling and low energy nitrate decontamination by a cost-effective BWRO-CCD method [J].
Efraty, Avi ;
Septon, Joseph .
DESALINATION AND WATER TREATMENT, 2012, 49 (1-3) :384-389
[9]   Closed circuit desalination series no-4: high recovery low energy desalination of brackish water by a new single stage method without any loss of brine energy [J].
Efraty, Avi .
DESALINATION AND WATER TREATMENT, 2012, 42 (1-3) :262-268
[10]   MASS-TRANSFER IN THE MEMBRANE CONCENTRATION POLARIZATION LAYER UNDER TURBULENT CROSS FLOW .1. CRITICAL LITERATURE-REVIEW AND ADAPTATION OF EXISTING SHERWOOD CORRELATIONS TO MEMBRANE OPERATIONS [J].
GEKAS, V ;
HALLSTROM, B .
JOURNAL OF MEMBRANE SCIENCE, 1987, 30 (02) :153-170