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Theoretical analysis of a seawater desalination process integrating forward osmosis, crystallization, and reverse osmosis

Authors
Kim, Do YeonGu, BoramKim, Joon HaYang, Dae Ryook
Issue Date
1-10월-2013
Publisher
ELSEVIER
Keywords
Desalination; Forward osmosis; Draw solute; Crystallization; Reverse osmosis
Citation
JOURNAL OF MEMBRANE SCIENCE, v.444, pp.440 - 448
Indexed
SCIE
SCOPUS
Journal Title
JOURNAL OF MEMBRANE SCIENCE
Volume
444
Start Page
440
End Page
448
URI
https://scholar.korea.ac.kr/handle/2021.sw.korea/101915
DOI
10.1016/j.memsci.2013.05.035
ISSN
0376-7388
Abstract
A hybrid forward osmosis (FO)/crystallization/reverse osmosis (RO) process for seawater desalination was proposed, and the theoretical analysis of the process was conducted. When the FO unit is considered as the main desalination unit, the crystallization and RO units can be regarded as a draw solute recovery process. First, in the FO process, fresh water is extracted from seawater and permeates into draw solution. This diluted draw solution is cooled down in the crystallization process and the draw solute is precipitated up to the saturation at low temperature. As a result, the feed stream of the RO process has lower concentration, and consequently, total energy consumption is expected to be reduced. In order to apply the proposed process in practice, the selection of suitable draw solute should be carefully determined. In the present work, five substances were suggested as draw solutes in the proposed system: ammonium oxalate, ammonium aluminum sulfate, sodium periodate, sodium phosphate and sodium sulfate. Based on properties of the substances, total energy consumption was analyzed for each draw solute. The total energy was calculated by the sum of cooling energy in crystallization process and pumping energy in RO process. Through the hybridization of these three unit processes, the energy requirement for fresh water production can be reduced to 2.15 kW h/m(3). Thus, it is concluded that the proposed process can be highly competitive. (C) 2013 Elsevier B.V. All rights reserved.
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