File Download

There are no files associated with this item.

  • Find it @ UNIST can give you direct access to the published full text of this article. (UNISTARs only)
Related Researcher

조재원

Cho, Jaeweon
Sense Laboratory
Read More

Views & Downloads

Detailed Information

Cited time in webofscience Cited time in scopus
Metadata Downloads

Enhanced or reduced concentration polarization by membrane fouling in seawater reverse osmosis (SWRO) processes

Author(s)
Kim, SuhanLee, SungyunLee, EunkyungSarper, SarpKim, Chung-HwanCho, Jaeweon
Issued Date
2009-10
DOI
10.1016/j.desal.2008.12.021
URI
https://scholarworks.unist.ac.kr/handle/201301/11735
Fulltext
http://www.sciencedirect.com/science/article/pii/S0011916409004962
Citation
DESALINATION, v.247, no.1-3, pp.162 - 168
Abstract
Salt rejection behaviors coupled with membrane fouling in seawater reverse osmosis (SWRO) processes were studied through a lab-scale membrane fouling test. Seawater was taken from Masan Bay, South Korea and foulants such as humic acid (HA), sodium alginate (SA), and silica nanoparticle (S120; particle diameter = 120 nm), were spiked to the seawater for the rapid fouling test. All the test conditions except model foulant were controlled equally. Salt concentration in permeate increases with flux decline even with no fouling because of increased water permeation and relatively constant salt passage. Salt mass transfer can be altered in the presence of fouling layer. Organic foulants such as HA and SA tend to build up denser fouling layer than S 120 nanoparticles. Thus, S 120 fouling layer induced cake enhanced concentration polarization (CECP) to accelerate salt rejection decreasing rate while HA and SA fouling layer hindered the convection of salt to lead cake reduced concentration polarization (CRCP) decelerating the rate. These combined effects of flux decline, CECP, and CRCP can be the causes of the coupled behaviors of permeate flux and salt rejection
Publisher
ELSEVIER SCIENCE BV
ISSN
0011-9164

qrcode

Items in Repository are protected by copyright, with all rights reserved, unless otherwise indicated.