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EXERGOECONOMIC ANALYSIS in A CEMENT PRODUCTION PLANT

datacite.rightshttp://purl.org/coar/access_right/c_abf2spa
dc.contributor.authorMendoza, A.
dc.contributor.authorValle, H.
dc.contributor.authorFajardo Cuadro, Juan Gabriel
dc.contributor.authorBarreto Ponton, Deibys
dc.date.accessioned2023-07-19T21:29:48Z
dc.date.available2023-07-19T21:29:48Z
dc.date.issued2020
dc.date.submitted2023
dc.description.abstractA dry-type Cement Production Plan of 151 Tons per hour was taken as a case of study to implement an exergoeconomic analysis. In this paper, the exergy destruction and the investment costs of the system's units were calculated to obtain accurate information about the performance of the process, from the exergoeconomic factor and the relative difference cost. Conventional exergoeconomic analysis showed that the total cost of exergy destruction is 4206537 USD/h. The Calciner and the Rotary Kiln cause 62% of the total cost of the exergy destruction. The lowest values of the exergoeconomic factor were calculated for Calciner (0.01%), Clinker Cooler (0.01%), Rotary Kiln (0.02%), and Raw Mill (0.04%). The significant difference in relative cost was calculated for Calciner (42%) and Rotary Kiln (54.21%). The above implies that this equipment should be considered for an investment that allows the decrease of the exergy destruction cost and the increase of the exergetic efficiency. © 2020 ASME.spa
dc.format.mimetypeapplication/pdfspa
dc.identifier.citationFajardo, J., Mendoza, A., Barreto, D., & Valle, H. (2020, November). Exergoeconomic Analysis in a Cement Production Plant. In ASME International Mechanical Engineering Congress and Exposition (Vol. 84560, p. V008T08A069). American Society of Mechanical Engineers.spa
dc.identifier.doi10.1115/IMECE2020-23112
dc.identifier.instnameUniversidad Tecnológica de Bolívarspa
dc.identifier.reponameRepositorio Universidad Tecnológica de Bolívarspa
dc.identifier.urihttps://hdl.handle.net/20.500.12585/12249
dc.language.isoengspa
dc.publisher.placeCartagena de Indiasspa
dc.rights.accessrightsinfo:eu-repo/semantics/openAccessspa
dc.rights.ccAttribution-NonCommercial-NoDerivatives 4.0 Internacional*
dc.rights.urihttp://creativecommons.org/licenses/by-nc-nd/4.0/*
dc.sourceASME International Mechanical Engineering Congress and Exposition, Proceedings (IMECE)spa
dc.subject.armarcLEMB
dc.subject.keywordsCosts And Cost Analysis;spa
dc.subject.keywordsExergy;spa
dc.subject.keywordsCogeneration Systemsspa
dc.titleEXERGOECONOMIC ANALYSIS in A CEMENT PRODUCTION PLANTspa
dc.typeArtículo de revistaspa
dc.type.coarhttp://purl.org/coar/resource_type/c_6501spa
dc.type.driverinfo:eu-repo/semantics/articlespa
dc.type.hasversioninfo:eu-repo/semantics/draftspa
dcterms.bibliographicCitationAtmaca, A., Yumrutas, R. Thermodynamic and exergoeconomic analysis of a cement plant Part I-Methodology (2013) Energy conversion and management, 79, pp. 1-9.spa
dcterms.bibliographicCitationMergenthaler, P., Schinkel, A.-P., Tsatsaronis, G. Application of exergoeconomic, exergoenvironmental and advanced exergy analyses on Carbon Black production (2016) ECOS 2016 - Proceedings of the 29th International Conference on Efficiency, Cost, Optimisation, Simulation and Environmental Impact of Energy Systems ISBN: 978-961698015-9spa
dcterms.bibliographicCitationXiong, J., Zhao, H., Zhang, C., Zheng, C., Luh, P.B. Thermoeconomic operation optimization of a coal-fired power plant (2012) Energy, 42 (1), pp. 486-496. Cited 75 times. www.elsevier.com/inca/publications/store/4/8/3/ doi: 10.1016/j.energy.2012.03.020spa
dcterms.bibliographicCitationAtmaca, A., Yumrutaş, R. Thermodynamic and exergoeconomic analysis of a cement plant: Part II - Application (2014) Energy Conversion and Management, 79, pp. 799-808. Cited 68 times. https://www.journals.elsevier.com/energy-conversion-and-management doi: 10.1016/j.enconman.2013.11.054spa
dcterms.bibliographicCitationXiang, J.Y., Cali, M., Santarelli, M. Calculation for physical and chemical exergy of flows in systems elaborating mixed-phase flows and a case study in an IRSOFC plant (2004) International Journal of Energy Research, 28 (2), pp. 101-115. Cited 125 times. doi: 10.1002/er.953spa
dspace.entity.typePublication
oaire.resourcetypehttp://purl.org/coar/resource_type/c_6501spa
oaire.versionhttp://purl.org/coar/version/c_b1a7d7d4d402bccespa
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relation.isAuthorOfPublication50bc46c2-fd71-44e2-af34-49dab7a9cc22
relation.isAuthorOfPublication.latestForDiscoveryb39413ec-4659-409d-83a6-27b25dd2573e

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