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dc.contributor.authorNarayan, G. Prakash
dc.contributor.authorZubair, Syed M.
dc.contributor.authorMcGovern, Ronan Killian
dc.contributor.authorLienhard, John H
dc.date.accessioned2016-04-01T16:57:53Z
dc.date.available2016-04-01T16:57:53Z
dc.date.issued2011-03
dc.identifier.isbn978-0-7918-3892-1
dc.identifier.urihttp://hdl.handle.net/1721.1/102076
dc.description.abstractNature uses air as a carrier gas to desalinate seawater through evaporation and rain. Several investigators have previously studied desalination cycles based on carrier gas processes. However, single pressure carrier gas cycles suffer from low energy recovery and hence low performance. Here we discuss a novel carrier gas cycle which operates under varied pressure. This cycle operates the evaporation process under a reduced pressure and the condensation process at an elevated pressure to enhance energy recovery. The pressure is varied by using a mechanical compressor. This cycle has been found to be several times as efficient as the existing carrier gas cycles. In this paper, the salient features of this cycle are analyzed in an on-design sense by defining a component effectiveness for the simultaneous heat and mass exchange components and an isentropic efficiency for the compressor and the expander. Based on this study, ways to improve the cycle are proposed. The possibility of using a throttle valve instead of an expander and the effect this would have on the overall performance is reported. Comparison of the new desalination cycle with existing ones is also performed in terms of specific work consumption.en_US
dc.description.sponsorshipCenter for Clean Water and Clean Energy at MIT and KFUPMen_US
dc.language.isoen_US
dc.publisherASME Internationalen_US
dc.relation.isversionofhttp://dx.doi.org/10.1115/AJTEC2011-44095en_US
dc.rightsArticle is made available in accordance with the publisher's policy and may be subject to US copyright law. Please refer to the publisher's site for terms of use.en_US
dc.sourceProf. Lienhard via Angie Locknaren_US
dc.titleVariable Pressure Humidification Dehumidification Desalination Systemen_US
dc.typeArticleen_US
dc.identifier.citationNarayan, G. Prakash, Ronan K. McGovern, John H. Lienhard, and Syed M. Zubair. “Variable Pressure Humidification Dehumidification Desalination System.” ASME/JSME 2011 8th Thermal Engineering Joint Conference (2011). © 2011 ASMEen_US
dc.contributor.departmentMassachusetts Institute of Technology. Abdul Latif Jameel World Water & Food Security Laben_US
dc.contributor.departmentMassachusetts Institute of Technology. Department of Mechanical Engineeringen_US
dc.contributor.mitauthorNarayan, G. Prakashen_US
dc.contributor.mitauthorMcGovern, Ronan Killianen_US
dc.contributor.mitauthorLienhard, John H.en_US
dc.relation.journalProceedings of the ASME/JSME 2011 8th Thermal Engineering Joint Conferenceen_US
dc.eprint.versionFinal published versionen_US
dc.type.urihttp://purl.org/eprint/type/ConferencePaperen_US
eprint.statushttp://purl.org/eprint/status/NonPeerRevieweden_US
dspace.orderedauthorsNarayan, G. Prakash; McGovern, Ronan K.; Lienhard, John H.; Zubair, Syed M.en_US
dc.identifier.orcidhttps://orcid.org/0000-0002-2901-0638
dc.identifier.orcidhttps://orcid.org/0000-0002-3808-8824
mit.licensePUBLISHER_POLICYen_US


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