Please use this identifier to cite or link to this item: http://hdl.handle.net/10553/76467
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dc.contributor.authorKhoshgoftar Manesh, M. H.en_US
dc.contributor.authorFirouzi, P.en_US
dc.contributor.authorKabiri, S.en_US
dc.contributor.authorBlanco Marigorta, Ana Maríaen_US
dc.date.accessioned2020-12-09T13:52:06Z-
dc.date.available2020-12-09T13:52:06Z-
dc.date.issued2021en_US
dc.identifier.issn0196-8904en_US
dc.identifier.otherScopus-
dc.identifier.urihttp://hdl.handle.net/10553/76467-
dc.description.abstractIn this paper, the simultaneous production of power and freshwater by the integration of a gas turbine (GT), a supercritical carbon dioxide (S-CO2) cycle, an organic Rankine cycle (ORC) and a reverse osmosis (RO) desalination unit is proposed. The S-CO2 and the ORC are bottoming cycles that recover the waste heat from the exhaust gases of the GT. A RO seawater desalination unit has been added to this power generation cycle to produce low-cost freshwater. The thermodynamic modelling and the simulation of the integrated cycle are performed. In addition, exergetic, exergoeconomic and exergoenvironmental analyses have been carried out. Cyclopentane has been chosen as working fluid of the ORC. The results show that the total energy generated by the cycles is about 75.1 MW; the compressors and pumps consume 44% and the rest is sent to the electricity grid. The integration of the S-CO2 cycle with the gas turbine increases the total efficiency by 10.9%. Also, the addition of the ORC to this integration, improves the efficiency by about 2%. The cost of power generation in the gas turbine is about 0.604 $/s, in the turbine of the S-CO2 cycle about 0.182 $/s and in the turbine of ORC cycle about 0.036 $/s. The cost of freshwater production in the RO unit with 5 MW of power consumption is 0.88 $/m3. The results show that the proposed combined GT/S-CO2/ORC/RO regenerative system is promising in terms of waste heat recovery from gas turbines. As advantages, deep waste heat recovery, high exergetic efficiency, and low power and freshwater costs have been achieved.en_US
dc.languageengen_US
dc.relation.ispartofEnergy Conversion and Managementen_US
dc.sourceEnergy Conversion and Management [ISSN 0196-8904], v. 228, 113607, (Enero 2021)en_US
dc.subject330609 Transmisión y distribuciónen_US
dc.subject332205 Fuentes no convencionales de energíaen_US
dc.subject330303 Procesos químicosen_US
dc.subject330806 Regeneración del aguaen_US
dc.subject332816 Transferencia de caloren_US
dc.subject.otherBrayton Cycleen_US
dc.subject.otherExergeticen_US
dc.subject.otherExergoeconomicen_US
dc.subject.otherExergoenvironmentalen_US
dc.subject.otherORCen_US
dc.subject.otherReverse Osmosis (RO)en_US
dc.subject.otherSCO2en_US
dc.titleEvaluation of power and freshwater production based on integrated gas turbine, S-CO2, and ORC cycles with RO desalination uniten_US
dc.typeinfo:eu-repo/semantics/Articleen_US
dc.typeArticleen_US
dc.identifier.doi10.1016/j.enconman.2020.113607en_US
dc.identifier.scopus85096842168-
dc.contributor.authorscopusid34876845000-
dc.contributor.authorscopusid57215009597-
dc.contributor.authorscopusid57215012009-
dc.contributor.authorscopusid25652860100-
dc.relation.volume228en_US
dc.investigacionIngeniería y Arquitecturaen_US
dc.type2Artículoen_US
dc.utils.revisionen_US
dc.date.coverdateEnero 2021en_US
dc.identifier.ulpgcen_US
dc.contributor.buulpgcBU-INGen_US
dc.description.sjr2,829
dc.description.jcr11,533
dc.description.sjrqQ1
dc.description.jcrqQ1
dc.description.scieSCIE
dc.description.miaricds11,0
item.grantfulltextnone-
item.fulltextSin texto completo-
crisitem.author.deptGIR Group for the Research on Renewable Energy Systems-
crisitem.author.deptDepartamento de Ingeniería de Procesos-
crisitem.author.orcid0000-0003-4635-7235-
crisitem.author.parentorgDepartamento de Ingeniería Mecánica-
crisitem.author.fullNameBlanco Marigorta, Ana María-
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