Advanced exergy analysis of an integrated solid waste fueled cogeneration system based on organic Rankine Cycle for different working fluids

dc.contributor.authorUstaoğlu, Abid
dc.contributor.authorTorlakli, Hande
dc.contributor.authorErgun, Alper
dc.contributor.authorErdoğmuş, Ertuğrul
dc.contributor.authorAkay, Mehmet Emin
dc.contributor.authorErdoğmuş, Ertuğrul
dc.contributor.authorUstaoğlu, Abid
dc.date.accessioned2025-10-18T13:22:36Z
dc.date.created2022
dc.date.issued2022
dc.departmentFakülteler, Mühendislik Mimarlık ve Tasarım Fakültesi, Makine Mühendisliği Bölümü
dc.departmentFakülteler, Mühendislik Mimarlık ve Tasarım Fakültesi, Çevre Mühendisliği Bölümü
dc.description.abstractIn this study, the performance evaluation of an ORC-based solid waste-powered cogeneration system was carried out using conventional and advanced exergy analysis methods. Eight different working fluids including dry (isopentane, n-pentane, n-octane, n-heptane), isentropic (R141b, R123), and wet (methanol, water) types were selected for the evaluation. The total capacity of the heat source was determined with the data obtained from the assessment of municipal solid wastes with different calorific values by the characterization method. Energy and exergy analyses were carried out for each component to examine the effect of selected cycle parameters, including evaporator pressure, intermediate pressure, and condenser pressure, and determine the optimum working fluid for the system. The exergy destruction in the components was split into avoidable/unavoidable and endogenous/exogenous parts in the advanced exergy analysis to identify the improvement potentials and the interaction between the components. The thermal and exergy efficiency values reach the highest values of 81.36 % and 40.76 %, respectively. R141b performs as the best working fluid, while the lowest performance is obtained from water. About 121.3 kW of power generation and 918.2 kW of process heat were obtained from the ORC-CHP system using R141b at 1400 kPa evaporator pressure. Conventional exergy analysis states that the evap-orator, process heater, and turbine are the most critical components, accounting for 67.94 %, 19 %, and 4.92 % of the total exergy destruction rate, respectively. The advanced exergy analysis shows that the priority should be on the turbine having the largest share of the avoidable part. The avoidable part, which accounts for 14.5 % of the total exergy destruction, can be reduced by system improvements.
dc.description.sponsorshipBart?n University Scientific Research Projects Coordinator (BAP); [2018 -FEN -A-014]
dc.description.sponsorshipThe authors gratefully acknowledge the financial supports from the Bart?n University Scientific Research Projects Coordinator (BAP) (ID 2018 -FEN -A-014) .
dc.identifier.doi10.1016/j.enconman.2022.116294
dc.identifier.issn0196-8904
dc.identifier.issn1879-2227
dc.identifier.orcidUSTAOGLU, Abid/0000-0003-3391-5015
dc.identifier.orcidErgun, Alper/0000-0003-0402-4088
dc.identifier.scopus2-s2.0-85139309805
dc.identifier.scopusqualityQ1
dc.identifier.urihttps://doi.org/10.1016/j.enconman.2022.116294
dc.identifier.urihttps://hdl.handle.net/11772/22393
dc.identifier.volume270
dc.identifier.wosWOS:000874589100002
dc.identifier.wosqualityQ1
dc.indekslendigikaynakWeb of Science
dc.indekslendigikaynakScopus
dc.language.isoen
dc.publisherPergamon-Elsevier Science Ltd
dc.relation.ispartofEnergy Conversion and Management
dc.relation.publicationcategoryMakale - Uluslararası Hakemli Dergi - Kurum Öğretim Elemanı
dc.relation.sdgGoal-11: Sustainable Cities And Communities
dc.relation.sdgGoal-12: Responsible Consumption and Production
dc.rightsinfo:eu-repo/semantics/closedAccess
dc.snmzWoS_20251016
dc.subjectOrganic Rankine Cycle
dc.subjectCogeneration
dc.subjectSolid Waste
dc.subjectConventional Exergy Analysis
dc.subjectAdvanced Exergy Analysis
dc.subjectExergy Destruction
dc.titleAdvanced exergy analysis of an integrated solid waste fueled cogeneration system based on organic Rankine Cycle for different working fluids
dc.typeArticle
dspace.entity.typePublication
relation.isAuthorOfPublicationbdef771b-3467-4bf3-a41d-1823272672f7
relation.isAuthorOfPublication831ef1cf-f629-4a76-966d-53534977a411
relation.isAuthorOfPublication.latestForDiscoverybdef771b-3467-4bf3-a41d-1823272672f7

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