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dc.contributor.authorBouma, Andrew Thomas
dc.contributor.authorLienhard, John H.
dc.date.accessioned2018-09-07T19:18:41Z
dc.date.available2018-09-07T19:18:41Z
dc.date.issued2018-08
dc.date.submitted2018-07
dc.identifier.issn0011-9164
dc.identifier.urihttp://hdl.handle.net/1721.1/117682
dc.description.abstractBrine concentration allows for increased recovery ratios in water treatment systems, reduction of waste volumes, and the production of minerals from saline brines. Existing methods of brine concentration, while robust, are often very energy intensive. Better efficiency may be possible using Counterflow Reverse Osmosis (CFRO), a membrane-based, pressure-driven brine concentration technology. The present work develops a model for CFRO. Using this model, a single CFRO module is simulated and its performance characterized. Exergy destruction within a single-stage system is analyzed, which provides insights for configuring and optimizing multistaged systems. Additionally, a parametric analysis of membrane parameters provides direction for the development of CFRO-specific membranes. Two existing configurations of CFRO are discussed, and compared with a new third configuration, split-feed CFRO, which is presented here for the first time. Split-feed CFRO systems are simulated and optimized to provide guidance for system design. A variety of multistage systems operating at a range of recovery ratios are simulated, and the results compared are with existing desalination and brine concentration technologies, showing the potential for improved recovery ratios and reduced energy consumption. Keywords: Brine concentration, Desalination, Energy efficiency, Counterflow reverse osmosis, Zero liquid dischargeen_US
dc.description.sponsorshipKuwait Foundation for the Advancement of Sciencesen_US
dc.language.isoen_US
dc.publisherElsevieren_US
dc.relation.isversionofhttps://doi.org/10.1016/j.desal.2018.07.011en_US
dc.rightsCreative Commons Attribution-Noncommercial-Share Alikeen_US
dc.rights.urihttp://creativecommons.org/licenses/by-nc-sa/4.0/en_US
dc.sourceProf. Lienharden_US
dc.titleSplit-feed counterflow reverse osmosis for brine concentrationen_US
dc.typeArticleen_US
dc.identifier.citationBouma, Andrew T., and John H. Lienhard. “Split-Feed Counterflow Reverse Osmosis for Brine Concentration.” Desalination, vol. 445, Nov. 2018, pp. 280–91.en_US
dc.contributor.departmentMassachusetts Institute of Technology. Department of Mechanical Engineeringen_US
dc.contributor.mitauthorBouma, Andrew Thomas
dc.contributor.mitauthorLienhard, John H.
dc.relation.journalDesalinationen_US
dc.eprint.versionAuthor's final manuscripten_US
dc.type.urihttp://purl.org/eprint/type/JournalArticleen_US
eprint.statushttp://purl.org/eprint/status/PeerRevieweden_US
dspace.orderedauthorsBouma, Andrew T.; Lienhard, John H.en_US
dspace.embargo.termsNen_US
dc.identifier.orcidhttps://orcid.org/0000-0002-6420-9677
dc.identifier.orcidhttps://orcid.org/0000-0002-2901-0638
mit.licenseOPEN_ACCESS_POLICYen_US


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