Please use this identifier to cite or link to this item: https://hdl.handle.net/2440/64209
Full metadata record
DC FieldValueLanguage
dc.contributor.authorWu, J.-
dc.contributor.authorBiggs, M.-
dc.contributor.authorHu, E.-
dc.date.issued2010-
dc.identifier.citationProceedings of Chemeca 2010: pp. 1-9-
dc.identifier.isbn9780858259713-
dc.identifier.urihttp://hdl.handle.net/2440/64209-
dc.description.abstractAdsorption-based desalination (AD) is attracting increasing attention because of its ability to use low-grade thermal energy to co-generate fresh water and cooling. Various mathematic models have been developed under the different assumptions by researchers to understand and simulate the thermodynamic cycle and the performance of the AD systems. In this paper a comparison study has been carried out for a static model using the Langmuir isotherm, a zero–dimensional dynamic model using a Toth isotherm and a one-dimensional dynamic model. The simulated results of the fresh water production rate (FWPR) and energy consumption for a two-beds AD system from various models are compared with published experimental data.-
dc.description.statementofresponsibilityJunWei Wu, Eric Hu, Mark Biggs-
dc.description.urihttp://www.chemeca2010.com/abstract/28.asp-
dc.language.isoen-
dc.publisherEngineers Australia-
dc.rightsCopyright status unknown-
dc.titleComparison of adsorption-based desalination plant performance models-
dc.typeConference paper-
dc.contributor.conferenceCHEMECA (38th : 2010 : Adelaide, Australia)-
dc.publisher.placeAustralia-
pubs.publication-statusPublished-
dc.identifier.orcidHu, E. [0000-0002-7390-0961]-
Appears in Collections:Aurora harvest 5
Chemical Engineering publications
Environment Institute publications
Mechanical Engineering conference papers

Files in This Item:
There are no files associated with this item.


Items in DSpace are protected by copyright, with all rights reserved, unless otherwise indicated.