Dual stage PRO process: impact of the membrane materials of the process performance

A dual stage pressure retarded osmosis (PRO) process was investigated for power generation using different types of membranes. Polyamide (PA) and cellulose triacetate (CTA) membranes were used in the first and second stage of the PRO process to improve the process performance due to the high water p...

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Main Authors: Altaee, A., Ismail, A. F., Sharif, A., Zaragoza, G.
Format: Article
Published: Taylor and Francis Inc. 2016
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Online Access:http://eprints.utm.my/id/eprint/73718/
https://www.scopus.com/inward/record.uri?eid=2-s2.0-84955736271&doi=10.1080%2f19443994.2015.1007173&partnerID=40&md5=df85c541fe1e6acf2ac34349d0645929
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spelling my.utm.737182017-11-18T01:21:06Z http://eprints.utm.my/id/eprint/73718/ Dual stage PRO process: impact of the membrane materials of the process performance Altaee, A. Ismail, A. F. Sharif, A. Zaragoza, G. TP Chemical technology A dual stage pressure retarded osmosis (PRO) process was investigated for power generation using different types of membranes. Polyamide (PA) and cellulose triacetate (CTA) membranes were used in the first and second stage of the PRO process to improve the process performance due to the high water permeability of PA membranes. A comparison between dual stage PA–CTA and CTA–CTA membrane systems were carried out using seawater as a draw solution, while fresh water and wastewater effluent were the feed solution in the first and second stage of the process. The impact of draw solution flow rate on the process performance was evaluated. The performance of first and second stage of the PRO process increased by 11.5 and 28.6%, respectively, when the draw solution flow rate increased by a factor of 2.5. In return, there was a negligible increase in the total specific power consumption of the PRO process. In general, power consumption of the dual stage PRO process was as low as 0.3 kWh/m3. Furthermore, the results showed that the performance of the dual stage PRO process increased with increasing seawater salinity from 32 to 50 g/L due to the higher net driving pressure across the membrane. Finally, power generation in the PA–CTA system was up to 33% higher than that in the CTA–CTA system. Taylor and Francis Inc. 2016 Article PeerReviewed Altaee, A. and Ismail, A. F. and Sharif, A. and Zaragoza, G. (2016) Dual stage PRO process: impact of the membrane materials of the process performance. Desalination and Water Treatment, 57 (14). pp. 6172-6183. ISSN 1944-3994 https://www.scopus.com/inward/record.uri?eid=2-s2.0-84955736271&doi=10.1080%2f19443994.2015.1007173&partnerID=40&md5=df85c541fe1e6acf2ac34349d0645929
institution Universiti Teknologi Malaysia
building UTM Library
collection Institutional Repository
continent Asia
country Malaysia
content_provider Universiti Teknologi Malaysia
content_source UTM Institutional Repository
url_provider http://eprints.utm.my/
topic TP Chemical technology
spellingShingle TP Chemical technology
Altaee, A.
Ismail, A. F.
Sharif, A.
Zaragoza, G.
Dual stage PRO process: impact of the membrane materials of the process performance
description A dual stage pressure retarded osmosis (PRO) process was investigated for power generation using different types of membranes. Polyamide (PA) and cellulose triacetate (CTA) membranes were used in the first and second stage of the PRO process to improve the process performance due to the high water permeability of PA membranes. A comparison between dual stage PA–CTA and CTA–CTA membrane systems were carried out using seawater as a draw solution, while fresh water and wastewater effluent were the feed solution in the first and second stage of the process. The impact of draw solution flow rate on the process performance was evaluated. The performance of first and second stage of the PRO process increased by 11.5 and 28.6%, respectively, when the draw solution flow rate increased by a factor of 2.5. In return, there was a negligible increase in the total specific power consumption of the PRO process. In general, power consumption of the dual stage PRO process was as low as 0.3 kWh/m3. Furthermore, the results showed that the performance of the dual stage PRO process increased with increasing seawater salinity from 32 to 50 g/L due to the higher net driving pressure across the membrane. Finally, power generation in the PA–CTA system was up to 33% higher than that in the CTA–CTA system.
format Article
author Altaee, A.
Ismail, A. F.
Sharif, A.
Zaragoza, G.
author_facet Altaee, A.
Ismail, A. F.
Sharif, A.
Zaragoza, G.
author_sort Altaee, A.
title Dual stage PRO process: impact of the membrane materials of the process performance
title_short Dual stage PRO process: impact of the membrane materials of the process performance
title_full Dual stage PRO process: impact of the membrane materials of the process performance
title_fullStr Dual stage PRO process: impact of the membrane materials of the process performance
title_full_unstemmed Dual stage PRO process: impact of the membrane materials of the process performance
title_sort dual stage pro process: impact of the membrane materials of the process performance
publisher Taylor and Francis Inc.
publishDate 2016
url http://eprints.utm.my/id/eprint/73718/
https://www.scopus.com/inward/record.uri?eid=2-s2.0-84955736271&doi=10.1080%2f19443994.2015.1007173&partnerID=40&md5=df85c541fe1e6acf2ac34349d0645929
_version_ 1643656728446763008
score 13.1944895