Omniphobic membrane using layer-by-layer technique to treat RO brine from CSG produced water by AGMD

Woo, Y; Tijing, L; Shon, H

Omniphobic membrane using layer-by-layer technique to treat RO brine from CSG produced water by AGMD

Woo, Y

Tijing, L

Shon, H

Permalink

Publication Type:: Conference Proceeding
Citation:: 2016
Issue Date:: 2016-11-15

Open Access

Copyright Clearance Process

Recently Added
In Progress
Open Access

This item is open access.

Microsoft Word XML

Download Accepted Manuscript versionMicrosoft Word XML (3.68 MB)

View statistics

Full metadata record

Field	Value	Language
dc.contributor.author	Woo, Y https://orcid.org/0000-0003-0847-3067	en_US
dc.contributor.author	Tijing, L https://orcid.org/0000-0001-9398-6355	en_US
dc.contributor.author	Shon, H https://orcid.org/0000-0002-3777-7169	en_US
dc.contributor.editor	Kim, S-H	en_US
dc.date	2016-11-12	en_US
dc.date.available	2016-11-15	en_US
dc.date.issued	2016-11-15	en_US
dc.identifier.citation	2016	en_US
dc.identifier.uri	http://hdl.handle.net/10453/63438
dc.description.abstract	The worldwide problem on water scarcity has led to innovations in desalination technologies. The main desalination technologies used nowadays are multi-stage flash distillation and reverse osmosis; however both require large amounts of energy for pure water production. Scarcities in energy and water are considered as two of the top challenges in the world, thus there is a necessity to provide desalination technologies that can address both of these issues. Membrane distillation (MD) is gaining momentum as a potential alternative for water purification and desalination because it can possibly utilize low grade/waste heat, and solar energy with very high recovery (100% theoretical). MD is a thermally-driven membrane separation process utilizing low operating temperature (below 90oC) that allows only water vapor to pass through a hydrophobic, porous membrane, and is operated at ambient pressure or at vacuum pressure. MD is driven by the difference in partial vapor pressure between the hot feed and cold permeate streams.	en_US
dc.relation.ispartof	The 9th International Desalination Workshop (IDW 2016)	en_US
dc.title	Omniphobic membrane using layer-by-layer technique to treat RO brine from CSG produced water by AGMD	en_US
dc.type	Conference Proceeding
utslib.location.activity	Abu Dhabi, UAE	en_US
utslib.for	090404 Membrane and Separation Technologies	en_US
utslib.for	090409 Wastewater Treatment Processes	en_US
utslib.for	090407 Process Control and Simulation	en_US
pubs.embargo.period	Not known	en_US
pubs.organisational-group	/University of Technology Sydney
pubs.organisational-group	/University of Technology Sydney/Faculty of Engineering and Information Technology
pubs.organisational-group	/University of Technology Sydney/Faculty of Engineering and Information Technology/School of Civil and Environmental Engineering
pubs.organisational-group	/University of Technology Sydney/Strength - CTWW - Centre for Technology in Water and Wastewater Treatment
utslib.copyright.status	open_access
pubs.consider-herdc	false	en_US
pubs.finish-date	2016-11-15	en_US
pubs.start-date	2016-11-12	en_US

Abstract:

The worldwide problem on water scarcity has led to innovations in desalination technologies. The main desalination technologies used nowadays are multi-stage flash distillation and reverse osmosis; however both require large amounts of energy for pure water production. Scarcities in energy and water are considered as two of the top challenges in the world, thus there is a necessity to provide desalination technologies that can address both of these issues. Membrane distillation (MD) is gaining momentum as a potential alternative for water purification and desalination because it can possibly utilize low grade/waste heat, and solar energy with very high recovery (100% theoretical). MD is a thermally-driven membrane separation process utilizing low operating temperature (below 90oC) that allows only water vapor to pass through a hydrophobic, porous membrane, and is operated at ambient pressure or at vacuum pressure. MD is driven by the difference in partial vapor pressure between the hot feed and cold permeate streams.

Please use this identifier to cite or link to this item:

http://hdl.handle.net/10453/63438