Please use this identifier to cite or link to this item: https://hdl.handle.net/11147/12608
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dc.contributor.authorNazerifard, Rezaen_US
dc.contributor.authorMohammadpourfard, Mousaen_US
dc.contributor.authorHeris, Saeed Zeinalien_US
dc.date.accessioned2022-11-21T06:30:32Z-
dc.date.available2022-11-21T06:30:32Z-
dc.date.issued2022-12-
dc.identifier.urihttps://doi.org/10.1016/j.jcou.2022.102289-
dc.identifier.urihttps://hdl.handle.net/11147/12608-
dc.description.abstractTo recover waste heat and reduce the CO2 emissions into the atmosphere, an integrated system of organic Rankine cycle and post-combustion carbon capture unit coupled with furnaces of a refinery located in Tabriz, East Azerbaijan, Iran has been presented. To assess the performances of the proposed system, thermodynamic and economic analyses are performed. The organic Rankine cycle was optimized by selecting the suitable working fluid with optimal operating conditions among the primary considered ones through multi-objective optimization. Then, the response surface methodology combined with the Box-Behnken design was employed to evaluate the effects of decision variables and their interaction on the CO2 capture cost and attain the optimal conditions. The results indicate that the R-245fa is the best working fluids among the selected ones. According to the results, the flue gas inlet temperature into the absorber and lean loading are the terms of the model that have a significant impact on the output response. In the optimum setting of the decision variables, the CO2 capture cost equals 81.60 $/tCO2 and 81.90 $/tCO2 for ORC+CC and DCC+CC processes, respectively. Furthermore, due to the absence of a turbine in the DCC+CC system, its equivalent work is 28 % higher than the ORC+CC system. Also, the amine regeneration energy is responsible for 91.47 % and 86.15 % of the variable operating cost of the optimal ORC+CC and optimal DCC+CC, respectively.en_US
dc.language.isoenen_US
dc.publisherElsevieren_US
dc.relation.ispartofJournal of CO2 Utilizationen_US
dc.rightsinfo:eu-repo/semantics/embargoedAccessen_US
dc.subjectOrganic Rankine Cycle (ORC)en_US
dc.subjectCO2 emissionsen_US
dc.subjectRefinery furnaceen_US
dc.subjectResponse surface methodologyen_US
dc.titleOptimization of the integrated ORC and carbon capture units coupled to the refinery furnace with the RSM-BBD methoden_US
dc.typeArticleen_US
dc.authorid0000-0002-6098-924Xen_US
dc.institutionauthorMohammadpourfard, Mousaen_US
dc.departmentİzmir Institute of Technology. Energy Systems Engineeringen_US
dc.identifier.wosWOS:000892644100004en_US
dc.identifier.scopus2-s2.0-85141180117en_US
dc.relation.publicationcategoryMakale - Uluslararası Hakemli Dergi - Kurum Öğretim Elemanıen_US
dc.identifier.doi10.1016/j.jcou.2022.102289-
dc.relation.issn2212-9820en_US
dc.description.volume66en_US
dc.identifier.scopusqualityQ1-
item.fulltextWith Fulltext-
item.openairetypeArticle-
item.cerifentitytypePublications-
item.grantfulltextembargo_20250101-
item.languageiso639-1en-
item.openairecristypehttp://purl.org/coar/resource_type/c_18cf-
crisitem.author.dept03.06. Department of Energy Systems Engineering-
Appears in Collections:Energy Systems Engineering / Enerji Sistemleri Mühendisliği
Scopus İndeksli Yayınlar Koleksiyonu / Scopus Indexed Publications Collection
WoS İndeksli Yayınlar Koleksiyonu / WoS Indexed Publications Collection
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