Forward Osmosis Desalination Using Ferric Sulfate Draw Solute

Lack of suitable draw solutes is one of the major limiting factors hindering commercial realization of forward osmosis (FO) desalination process. This study investigates the feasibility of ferric sulfate as draw solute in FO desalination. A laboratory-scale, cross-flow FO apparatus utilizing commerc...

وصف كامل

محفوظ في:
التفاصيل البيبلوغرافية
المؤلف الرئيسي: Qasim, Muhammad (author)
مؤلفون آخرون: Mohammed, Faisal Waleed (author), Aidan, Ahmed (author), Darwish, Naif A. (author)
التنسيق: article
منشور في: 2017
الموضوعات:
الوصول للمادة أونلاين:http://hdl.handle.net/11073/16279
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author Qasim, Muhammad
author2 Mohammed, Faisal Waleed
Aidan, Ahmed
Darwish, Naif A.
author2_role author
author
author
author_facet Qasim, Muhammad
Mohammed, Faisal Waleed
Aidan, Ahmed
Darwish, Naif A.
author_role author
dc.creator.none.fl_str_mv Qasim, Muhammad
Mohammed, Faisal Waleed
Aidan, Ahmed
Darwish, Naif A.
dc.date.none.fl_str_mv 2017-12-01
2018-10-31T09:01:01Z
2018-10-31T09:01:01Z
dc.format.none.fl_str_mv application/pdf
dc.identifier.none.fl_str_mv Qasim, Muhammad, Faisal Mohammed, Ahmad Aidan, and Naif A. Darwish. "Forward Osmosis Desalination Using Ferric Sulfate Draw Solute." Desalination 423 (2017): 12.
0011-9164
http://hdl.handle.net/11073/16279
10.1016/j.desal.2017.08.019
dc.language.none.fl_str_mv en_US
dc.publisher.none.fl_str_mv Elsevier
dc.relation.none.fl_str_mv Desalination
https://doi.org/10.1016/j.desal.2017.08.019
dc.subject.none.fl_str_mv Forward osmosis
Desalination
Ferric sulfate
Draw solution
Water flux
dc.title.none.fl_str_mv Forward Osmosis Desalination Using Ferric Sulfate Draw Solute
dc.type.none.fl_str_mv info:eu-repo/semantics/publishedVersion
info:eu-repo/semantics/article
description Lack of suitable draw solutes is one of the major limiting factors hindering commercial realization of forward osmosis (FO) desalination process. This study investigates the feasibility of ferric sulfate as draw solute in FO desalination. A laboratory-scale, cross-flow FO apparatus utilizing commercial FO membrane (cellulose triacetate-based) was used to desalinate synthesized (5000 ppm NaCl) brackish water and (40,000 ppm NaCl) seawater using 280,000 ppm ferric sulfate draw solution at ambient conditions. The observed average water flux was 3.75 and 1.61 L/m2 h in case of brackish and seawater, respectively. Using deionized water as feed solution, reverse ferric sulfate flux of 1.88 g/m2 h was observed. Product water was recovered from the diluted draw solution by precipitation reaction using barium hydroxide. Pure water samples with salt contents of 60 and 80 ppm were obtained by desalinating brackish and seawater feed, respectively.
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identifier_str_mv Qasim, Muhammad, Faisal Mohammed, Ahmad Aidan, and Naif A. Darwish. "Forward Osmosis Desalination Using Ferric Sulfate Draw Solute." Desalination 423 (2017): 12.
0011-9164
10.1016/j.desal.2017.08.019
language_invalid_str_mv en_US
network_acronym_str aus
network_name_str aus
oai_identifier_str oai:repository.aus.edu:11073/16279
publishDate 2017
publisher.none.fl_str_mv Elsevier
repository.mail.fl_str_mv
repository.name.fl_str_mv
repository_id_str
spelling Forward Osmosis Desalination Using Ferric Sulfate Draw SoluteQasim, MuhammadMohammed, Faisal WaleedAidan, AhmedDarwish, Naif A.Forward osmosisDesalinationFerric sulfateDraw solutionWater fluxLack of suitable draw solutes is one of the major limiting factors hindering commercial realization of forward osmosis (FO) desalination process. This study investigates the feasibility of ferric sulfate as draw solute in FO desalination. A laboratory-scale, cross-flow FO apparatus utilizing commercial FO membrane (cellulose triacetate-based) was used to desalinate synthesized (5000 ppm NaCl) brackish water and (40,000 ppm NaCl) seawater using 280,000 ppm ferric sulfate draw solution at ambient conditions. The observed average water flux was 3.75 and 1.61 L/m2 h in case of brackish and seawater, respectively. Using deionized water as feed solution, reverse ferric sulfate flux of 1.88 g/m2 h was observed. Product water was recovered from the diluted draw solution by precipitation reaction using barium hydroxide. Pure water samples with salt contents of 60 and 80 ppm were obtained by desalinating brackish and seawater feed, respectively.Elsevier2018-10-31T09:01:01Z2018-10-31T09:01:01Z2017-12-01info:eu-repo/semantics/publishedVersioninfo:eu-repo/semantics/articleapplication/pdfQasim, Muhammad, Faisal Mohammed, Ahmad Aidan, and Naif A. Darwish. "Forward Osmosis Desalination Using Ferric Sulfate Draw Solute." Desalination 423 (2017): 12.0011-9164http://hdl.handle.net/11073/1627910.1016/j.desal.2017.08.019en_USDesalinationhttps://doi.org/10.1016/j.desal.2017.08.019oai:repository.aus.edu:11073/162792024-08-22T12:18:52Z
spellingShingle Forward Osmosis Desalination Using Ferric Sulfate Draw Solute
Qasim, Muhammad
Forward osmosis
Desalination
Ferric sulfate
Draw solution
Water flux
status_str publishedVersion
title Forward Osmosis Desalination Using Ferric Sulfate Draw Solute
title_full Forward Osmosis Desalination Using Ferric Sulfate Draw Solute
title_fullStr Forward Osmosis Desalination Using Ferric Sulfate Draw Solute
title_full_unstemmed Forward Osmosis Desalination Using Ferric Sulfate Draw Solute
title_short Forward Osmosis Desalination Using Ferric Sulfate Draw Solute
title_sort Forward Osmosis Desalination Using Ferric Sulfate Draw Solute
topic Forward osmosis
Desalination
Ferric sulfate
Draw solution
Water flux
url http://hdl.handle.net/11073/16279