TY - JOUR
T1 - Theoretical analysis of a seawater desalination process integrating forward osmosis, crystallization, and reverse osmosis
AU - Kim, Do Yeon
AU - Gu, Boram
AU - Ha Kim, Joon
AU - Ryook Yang, Dae
N1 - Funding Information:
This work was partially supported by the grant ( 07seaheroB02-01-01 ) from the Plant Technology Advancement Program funded by the Ministry of Land, Transport and Maritime Affairs of the Korean government , and by the Human Resources Development Program(No. 20114010203050) of the Korea Institute of Energy Technology Evaluation and Planning (KETEP) grant funded by the Korea government Ministry of Trade, Industry and Energy.
PY - 2013/10/1
Y1 - 2013/10/1
N2 - 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 2.15kWh/m3. Thus, it is concluded that the proposed process can be highly competitive.
AB - 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 2.15kWh/m3. Thus, it is concluded that the proposed process can be highly competitive.
KW - Crystallization
KW - Desalination
KW - Draw solute
KW - Forward osmosis
KW - Reverse osmosis
UR - http://www.scopus.com/inward/record.url?scp=84879562953&partnerID=8YFLogxK
U2 - 10.1016/j.memsci.2013.05.035
DO - 10.1016/j.memsci.2013.05.035
M3 - Article
AN - SCOPUS:84879562953
SN - 0376-7388
VL - 444
SP - 440
EP - 448
JO - Jornal of Membrane Science
JF - Jornal of Membrane Science
ER -