Publication:
Exergoeconomic and exergetic sustainability analysis of a combined dual-pressure organic rankine cycle and vapor compression refrigeration cycle

dc.contributor.authorÖzdemir Küçük, Esra
dc.contributor.authorKılıç, Muhsin
dc.contributor.buuauthorÖZDEMİR KÜÇÜK, ESRA
dc.contributor.buuauthorKILIÇ, MUHSİN
dc.contributor.departmentMühendislik Fakültesi
dc.contributor.departmentİbrahim Orhan Makina Bölümü
dc.contributor.orcid0000-0001-8146-0495
dc.contributor.orcid0000-0003-2113-4510
dc.contributor.researcheridO-2253-2015
dc.contributor.researcheridIQW-0498-2023
dc.date.accessioned2024-10-24T06:45:54Z
dc.date.available2024-10-24T06:45:54Z
dc.date.issued2023-04-01
dc.description.abstractIn this paper, an exergoeconomic and exergetic sustainability analysis of a dual-pressure organic Rankine cycle (ORC) and vapor compression refrigeration cycle (VCRC) driven by waste heat is performed for power generation and cooling production. In addition, the most suitable fluid couple among the thirty-five different fluid pairs was investigated for the proposed combined system. The results indicate that the highest energy utilization factor, exergy efficiency, the system coefficient of performance, and net power are calculated for the R123-R141b fluid pair. In terms of exergetic sustainability indicators, the best performance results are obtained for the R123-R141b fluid combination. The minimum unit electricity generation cost and the shortest payback period are calculated as 0.0664 $/kWh and 2.5 years, respectively, for the R123-R290 fluid pair. The system component with the highest exergy destruction is the boiler, with 21.67%. The result of the parametric analysis showed that the thermodynamic performance parameters increase with the increment of the ORC's boiling temperature. In addition, with the increasing boiling temperature, the environmental effect factor of the system decreases, while the exergetic sustainability index increases. Additionally, as the boiling temperature increases, the total system cost increases, while the unit electricity production cost and payback period decrease. It is suggested to use a R123-R141b fluid couple among fluid pairs created as a result of thermodynamic, exergoeconomic and sustainability analysis.
dc.identifier.doi10.3390/su15086987
dc.identifier.eissn2071-1050
dc.identifier.issue8
dc.identifier.urihttps://doi.org/10.3390/su15086987
dc.identifier.urihttps://hdl.handle.net/11452/46993
dc.identifier.urihttps://www.mdpi.com/2071-1050/15/8/6987
dc.identifier.volume15
dc.identifier.wos000977857600001
dc.indexed.wosWOS.SCI
dc.indexed.wosWOS.SSCI
dc.language.isoen
dc.publisherMdpi
dc.relation.journalSustainability
dc.relation.publicationcategoryMakale - Uluslararası Hakemli Dergi
dc.rightsinfo:eu-repo/semantics/openAccess
dc.subjectWaste heat-recovery
dc.subjectPerformance analysis
dc.subjectFluid selection
dc.subjectOptimization
dc.subjectOrc
dc.subjectSystem
dc.subjectPower
dc.subjectEnergy
dc.subjectConfigurations
dc.subjectDriven
dc.subjectDual-pressure orc
dc.subjectRefrigeration cycle
dc.subjectFluid pair
dc.subjectExergetic sustainability
dc.subjectCombined cycle
dc.subjectScience & technology - other topics
dc.subjectEnvironmental sciences & ecology
dc.titleExergoeconomic and exergetic sustainability analysis of a combined dual-pressure organic rankine cycle and vapor compression refrigeration cycle
dc.typeArticle
dspace.entity.typePublication
local.contributor.departmentYenişehir Meslek Yüksekokulu/İbrahim Orhan Makina Bölümü
local.contributor.departmentMühendislik Fakültesi/Makine Mühendisliği Bölümü
relation.isAuthorOfPublicationedd02203-2d40-48f1-869b-e0f9adf6517a
relation.isAuthorOfPublication56d98e3d-139a-4bf2-b105-8e1402865346
relation.isAuthorOfPublication.latestForDiscoveryedd02203-2d40-48f1-869b-e0f9adf6517a

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