Comparison of physico-chemical pretreatment methods to seawater reverse osmosis: Detailed analyses of molecular weight distribution of organic matter in initial stage

被引:45
作者
Shon, H. K. [1 ]
Vigneswaran, S. [1 ]
Cho, J. [2 ]
机构
[1] Tech Univ, Fac Engn, Broadway, NSW 2007, Australia
[2] Gwangju Inst Sci & Technol, Kwangju, South Korea
基金
澳大利亚研究理事会;
关键词
adsorption; flocculation; microfiltration molecular weight distribution; pretreatment; seawater reverses osmosis; ultrafiltration;
D O I
10.1016/j.memsci.2008.03.063
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
In desalination, effective pretreatment is the key to reduce membrane fouling that occurs during the seawater reverse osmosis (SWRO) process. However, it is difficult to compare the flux decline after different pretreatments using a small-scale reverse osmosis filtration unit. In this study, we successfully evaluated the effect of pretreatment on SWRO in terms of molecular weight distribution (MWD) of seawater organic matter (SWOM) after 20h of SWRO operation. Microfiltration (MF), ultrafiltration (UF), ferric chloride (FeCl(3)) flocculation and powdered activated carbon (PAC) adsorption, were used as pretreatment. The effluents and the retentates after each pretreatment and 20 h of SWRO operation were characterized in terms of MWD. Although the normalized flux of SWRO showed similar flux decline (J/J(0) = 0.17) with/without pretreatment, SWOM concentration in the retentates after different pretreatments was different in quantity and it increased linearly with time. The slope of the SWOM increase was 0.110, 0.096, 0.077 and 0.059 after MF, FeCl(3) flocculation, UF and PAC adsorption pretreatments, respectively. MW peaks for the seawater used in this study consisted of 1200 Da (biopolymers), 950 Da (fulvic acids), 650 Da (hydrolysates of humic substances), 250 Da (low MW acids) and 90 Da (low MW neutrals and amphiphilics). FeCl(3) flocculation preferentially removed 1200 Da (biopolymers), while PAC adsorption mostly removed 950 Da (fulvic acids). UF and NF removed only a marginal amount of relatively large organics, while RO removed the majority of organics. The intensity of 1200, 950, 650 and 250 Da MW in the RO retentates increased with the RO operation time. The organics of MW around 1200 Da (biopolymers) had a relatively low rate of increase with time compared with those of lower MW. This suggests that the SWOM of 1200 Da MW was preferentially retained on the membrane surface. (C) 2008 Elsevier B.V. All rights reserved.
引用
收藏
页码:151 / 158
页数:8
相关论文
共 18 条
[1]   Comparison of MF/UF pretreatment with conventional filtration prior to RO membranes for surface seawater desalination [J].
Brehant, A ;
Bonnelye, V ;
Perez, M .
DESALINATION, 2002, 144 (1-3) :353-360
[2]   Pretreatment of seawater: Results of pilot trials in Singapore [J].
Chua, KT ;
Hawlader, MNA ;
Malek, A .
DESALINATION, 2003, 159 (03) :225-243
[3]  
DUDLEY LY, 1996, P IDA WORLD C DES WA, V4, P45
[4]  
Gaid K, 2007, DESALINATION, V203, P1, DOI 10.1016/j.desal.2006.03.523
[5]   Evidence for membrane fouling by specific TOC constituents [J].
Huber, SA .
DESALINATION, 1998, 119 (1-3) :229-234
[6]  
HUBER SA, 2007, APPL LC OCD MARINE W
[7]  
Khedr G., 2000, DESALIN WATER REUSE, V10, P3
[8]   A case study of RO plant failure due to membrane fouling, analysis and diagnosis [J].
Khedr, MG .
DESALINATION, 1998, 120 (1-2) :107-113
[9]   Investigation of seawater reverse osmosis fouling and its relationship to pretreatment type [J].
Kumar, M ;
Adham, SS ;
Pearce, WR .
ENVIRONMENTAL SCIENCE & TECHNOLOGY, 2006, 40 (06) :2037-2044
[10]   Water quality and performance evaluation at seawater reverse osmosis plants through the use of advanced analytical tools [J].
Leparc, Jerome ;
Rapenne, Sophie ;
Courties, Claude ;
Lebaron, Philippe ;
Croue, Jean Philippe ;
Jacquemet, Valerie ;
Turner, Greg .
DESALINATION, 2007, 203 (1-3) :243-255