Please use this identifier to cite or link to this item: http://bura.brunel.ac.uk/handle/2438/28517
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dc.contributor.authorAlkhalidi, A-
dc.contributor.authorAlmomani, B-
dc.contributor.authorOlabi, AG-
dc.contributor.authorJouhara, H-
dc.date.accessioned2024-03-12T14:49:05Z-
dc.date.available2024-03-12T14:49:05Z-
dc.date.issued2024-02-23-
dc.identifierORCiD: Ammar Alkhalidi https://orcid.org/0000-0002-3501-2664-
dc.identifierORCiD: Hussam Jouhara https://orcid.org/0000-0002-6910-6116-
dc.identifier113030-
dc.identifier.citationAlkhalidi, A. et al. (2024) 'Techno-economic feasibility study of coupling low-temperature evaporation desalination plant with advanced pressurized water reactor', Nuclear Engineering and Design, 420, 113030, pp. 1 - 11. doi: 10.1016/j.nucengdes.2024.113030.en_US
dc.identifier.issn0029-5493-
dc.identifier.urihttps://bura.brunel.ac.uk/handle/2438/28517-
dc.descriptionData availability: Data will be made available on request.en_US
dc.description.abstractThe increasing demand for freshwater necessitates sustainable desalination solutions, and nuclear power plants offer a promising avenue by utilizing their low-grade waste heat. This study assesses a techno-economic feasibility of coupling a 5 MWth low-temperature evaporation plant with a UAE-based Advanced Pressurized Water Reactor (APR1400). The system addresses freshwater demand, aligning with sustainability goals through low-grade heat utilization. The investigation explores three extraction points for low-grade heat steam, with temperatures ranging from 80 °C to 130 °C. Thermodynamic evaluations using DE-TOP illustrate power requirements and losses, considering variations in maximum brine temperature from 50 °C to 65 °C. Economic analysis using DEEP estimates water production costs. Findings reveal negligible variances in power plant parameters and a minimal reduction in overall efficiency (<0.5 %). The power loss ratio increases proportionally (10 % to 18.6 %) with higher-temperature heat extraction, while the total power requirements for the desalination plant rises by around 30 %, with a negligible power output reduction ratios (0.03 % to 0.07 %). A consistent linear correlation between water production rate and maximum brine temperature doubles water production (∼900 to 1800 m3/day). Applying multiple extraction points across low-grade heat sources demonstrates scalability, reaching three times that of single-point extraction, with marginal increases in power requirements and losses, while maintaining the power reduction ratio below 0.15 %. Economic feasibility indicates competitive water production costs, ranging from 1.53 to 0.87 $/m3 for desalination capacities between 900 and 5400 m3/day. This study provides valuable insights into sustainable water production at the nexus of nuclear energy and desalination, with implications for necessary policy intervention.en_US
dc.description.sponsorshipThe Research Institute of Science and Engineering (RISE) at the University of Sharjah, Nuclear Energy System Simulation and Safety (NE3S) research group supported and funded this research.en_US
dc.format.extent1 - 11-
dc.format.mediumPrint-Electronic-
dc.languageEnglish-
dc.language.isoen_USen_US
dc.publisherElsevieren_US
dc.rightsCopyright © 2024 Elsevier. All rights reserved. This manuscript version is made available under the CC-BY-NC-ND 4.0 license, https://creativecommons.org/licenses/by-nc-nd/4.0/ (see: https://www.elsevier.com/about/policies/sharing).-
dc.rights.urihttps://creativecommons.org/licenses/by-nc-nd/4.0/-
dc.subjectAPR-1400en_US
dc.subjectnuclear desalinationen_US
dc.subjecttechno-economic analysisen_US
dc.subjectUnited Arab Emiratesen_US
dc.subjectwaste heat recoveryen_US
dc.titleTechno-economic feasibility study of coupling low-temperature evaporation desalination plant with advanced pressurized water reactoren_US
dc.typeArticleen_US
dc.identifier.doihttps://doi.org/10.1016/j.nucengdes.2024.113030-
dc.relation.isPartOfNuclear Engineering and Design-
pubs.publication-statusPublished-
pubs.volume420-
dc.identifier.eissn1872-759X-
dc.rights.licensehttps://creativecommons.org/licenses/by-nc-nd/4.0/legalcode.en-
dc.rights.holderElsevier-
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