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dc.contributor.authorAli, Emad
dc.contributor.authorOrfi, Jamel
dc.contributor.authorAlAnsary, Hany
dc.contributor.authorAlsaadi, Ahmad S.
dc.contributor.authorGhaffour, NorEddine
dc.date.accessioned2022-09-18T12:16:13Z
dc.date.available2022-09-18T12:16:13Z
dc.date.issued2022-09-02
dc.identifier.citationAli, E., Orfi, J., AlAnsary, H., Alsaadi, A. S., & Ghaffour, N. (2022). Novel multistage flash reversal Concept: Modelling and analysis. Applied Thermal Engineering, 217, 119223. https://doi.org/10.1016/j.applthermaleng.2022.119223
dc.identifier.issn1359-4311
dc.identifier.doi10.1016/j.applthermaleng.2022.119223
dc.identifier.urihttp://hdl.handle.net/10754/681575
dc.description.abstractIn this study, a rigorous modeling and simulation of a novel multi-stage flash (MSF) configuration consisting of reversing the brine circulation, termed MSF reversal (MSF-RV), is developed. Its performance is theoretically investigated and compared with conventional MSF Once Through (MSF-OT) with and without brine mixing. The MSF-RV concept is suitable for treating geothermal streams and can be driven by low grade thermal energy such as solar and geothermal energy and waste heat for direct seawater desalination. Hence, two options of MSF-RV are proposed, i) driven by a direct hot stream (MSF-RVc), and ii) powered by external heat to treat raw seawater (MSF-RVh). The analysis showed that the temperature distribution throughout the stages plays a significant role in the thermal efficiency and heat transfer area requirements for both configurations. Hence, careful selection of the design parameters is necessary to achieve the best performance. For the same recovery ratio, the MSF-RVc was found superior to MSF-OT in terms of gain output ratio (GOR) and specific energy consumption (SEC) by 52% and 60%, respectively. However, the specific area (sA) requirement of MSF-RVc is higher than that of MSF-OT by 50%. Brine mixing by recycling the rejected brine enhances the recovery ratio, GOR, and SEC for both structures. Conversely, the sA requirement increases with brine mixing but marginally for MSF-RV and remarkably for MSF-OT. Moreover, the design parameters of MSF-RVc such as the coolant inlet temperature, the temperature drop on the coolant side, and the coolant to brine ratio affect the overall performance. However, a trade-off between the thermal efficiency (GOR, SEC) and surface area requirement is still observed.
dc.description.sponsorshipThis project is funded by the Researchers Supporting Project number (RSP2022R510), King Saud University, Riyadh, Saudi Arabia.
dc.publisherElsevier BV
dc.relation.urlhttps://linkinghub.elsevier.com/retrieve/pii/S1359431122011541
dc.rightsNOTICE: this is the author’s version of a work that was accepted for publication in Applied Thermal Engineering. Changes resulting from the publishing process, such as peer review, editing, corrections, structural formatting, and other quality control mechanisms may not be reflected in this document. Changes may have been made to this work since it was submitted for publication. A definitive version was subsequently published in Applied Thermal Engineering, [217, , (2022-09-02)] DOI: 10.1016/j.applthermaleng.2022.119223 . © 2022. This manuscript version is made available under the CC-BY-NC-ND 4.0 license http://creativecommons.org/licenses/by-nc-nd/4.0/
dc.titleNovel multistage flash reversal Concept: Modelling and analysis
dc.typeArticle
dc.contributor.departmentEnvironmental Science and Engineering Program
dc.contributor.departmentBiological and Environmental Science and Engineering (BESE) Division
dc.contributor.departmentWater Desalination and Reuse Research Center (WDRC)
dc.identifier.journalApplied Thermal Engineering
dc.rights.embargodate2024-09-02
dc.eprint.versionPost-print
dc.contributor.institutionChemical Engineering Department, King Saud University, Riyadh 11421, Saudi Arabia
dc.contributor.institutionMechanical Engineering Department, King Saud University, Riyadh 11421, Saudi Arabia
dc.contributor.institutionKA.CARE Energy Research and Innovation Center at Riyadh, Saudi Arabia
dc.contributor.institutionChemical Engineering Department, University of Jeddah, Jeddah 21589, Saudi Arabia
dc.identifier.volume217
dc.identifier.pages119223
kaust.personGhaffour, Noreddine
dc.identifier.eid2-s2.0-85137295182


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