EXERGOECONOMIC ANALYSIS in A CEMENT PRODUCTION PLANT

A 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,...

Full description

Autores:
Fajardo, J.
Mendoza, A.
Barreto, D
Valle, H.
Tipo de recurso:
Fecha de publicación:
2020
Institución:
Universidad Tecnológica de Bolívar
Repositorio:
Repositorio Institucional UTB
Idioma:
eng
OAI Identifier:
oai:repositorio.utb.edu.co:20.500.12585/12249
Acceso en línea:
https://hdl.handle.net/20.500.12585/12249
Palabra clave:
Costs And Cost Analysis;
Exergy;
Cogeneration Systems
LEMB
Rights
openAccess
License
http://creativecommons.org/licenses/by-nc-nd/4.0/
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dc.title.spa.fl_str_mv EXERGOECONOMIC ANALYSIS in A CEMENT PRODUCTION PLANT
title EXERGOECONOMIC ANALYSIS in A CEMENT PRODUCTION PLANT
spellingShingle EXERGOECONOMIC ANALYSIS in A CEMENT PRODUCTION PLANT
Costs And Cost Analysis;
Exergy;
Cogeneration Systems
LEMB
title_short EXERGOECONOMIC ANALYSIS in A CEMENT PRODUCTION PLANT
title_full EXERGOECONOMIC ANALYSIS in A CEMENT PRODUCTION PLANT
title_fullStr EXERGOECONOMIC ANALYSIS in A CEMENT PRODUCTION PLANT
title_full_unstemmed EXERGOECONOMIC ANALYSIS in A CEMENT PRODUCTION PLANT
title_sort EXERGOECONOMIC ANALYSIS in A CEMENT PRODUCTION PLANT
dc.creator.fl_str_mv Fajardo, J.
Mendoza, A.
Barreto, D
Valle, H.
dc.contributor.author.none.fl_str_mv Fajardo, J.
Mendoza, A.
Barreto, D
Valle, H.
dc.subject.keywords.spa.fl_str_mv Costs And Cost Analysis;
Exergy;
Cogeneration Systems
topic Costs And Cost Analysis;
Exergy;
Cogeneration Systems
LEMB
dc.subject.armarc.none.fl_str_mv LEMB
description A 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.
publishDate 2020
dc.date.issued.none.fl_str_mv 2020
dc.date.accessioned.none.fl_str_mv 2023-07-19T21:29:48Z
dc.date.available.none.fl_str_mv 2023-07-19T21:29:48Z
dc.date.submitted.none.fl_str_mv 2023
dc.type.coarversion.fl_str_mv http://purl.org/coar/version/c_b1a7d7d4d402bcce
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dc.identifier.citation.spa.fl_str_mv Fajardo, 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.
dc.identifier.uri.none.fl_str_mv https://hdl.handle.net/20.500.12585/12249
dc.identifier.doi.none.fl_str_mv 10.1115/IMECE2020-23112
dc.identifier.instname.spa.fl_str_mv Universidad Tecnológica de Bolívar
dc.identifier.reponame.spa.fl_str_mv Repositorio Universidad Tecnológica de Bolívar
identifier_str_mv Fajardo, 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.
10.1115/IMECE2020-23112
Universidad Tecnológica de Bolívar
Repositorio Universidad Tecnológica de Bolívar
url https://hdl.handle.net/20.500.12585/12249
dc.language.iso.spa.fl_str_mv eng
language eng
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dc.rights.accessrights.spa.fl_str_mv info:eu-repo/semantics/openAccess
dc.rights.cc.*.fl_str_mv Attribution-NonCommercial-NoDerivatives 4.0 Internacional
rights_invalid_str_mv http://creativecommons.org/licenses/by-nc-nd/4.0/
Attribution-NonCommercial-NoDerivatives 4.0 Internacional
http://purl.org/coar/access_right/c_abf2
eu_rights_str_mv openAccess
dc.format.mimetype.spa.fl_str_mv application/pdf
dc.publisher.place.spa.fl_str_mv Cartagena de Indias
dc.source.spa.fl_str_mv ASME International Mechanical Engineering Congress and Exposition, Proceedings (IMECE)
institution Universidad Tecnológica de Bolívar
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spelling Fajardo, J.89e39209-aa6c-4020-a507-9c56a27d4943Mendoza, A.8f3bbe3b-70bc-4c5e-a375-4063d6733be7Barreto, D2857c702-720f-454a-8b6f-725302964923Valle, H.9f24a7ec-1afb-4a69-a521-ad7dd5eaf9af2023-07-19T21:29:48Z2023-07-19T21:29:48Z20202023Fajardo, 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.https://hdl.handle.net/20.500.12585/1224910.1115/IMECE2020-23112Universidad Tecnológica de BolívarRepositorio Universidad Tecnológica de BolívarA 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.application/pdfenghttp://creativecommons.org/licenses/by-nc-nd/4.0/info:eu-repo/semantics/openAccessAttribution-NonCommercial-NoDerivatives 4.0 Internacionalhttp://purl.org/coar/access_right/c_abf2ASME International Mechanical Engineering Congress and Exposition, Proceedings (IMECE)EXERGOECONOMIC ANALYSIS in A CEMENT PRODUCTION PLANTinfo:eu-repo/semantics/articleinfo:eu-repo/semantics/drafthttp://purl.org/coar/resource_type/c_6501http://purl.org/coar/version/c_b1a7d7d4d402bccehttp://purl.org/coar/resource_type/c_2df8fbb1Costs And Cost Analysis;Exergy;Cogeneration SystemsLEMBCartagena de IndiasAtmaca, A., Yumrutas, R. Thermodynamic and exergoeconomic analysis of a cement plant Part I-Methodology (2013) Energy conversion and management, 79, pp. 1-9.Mergenthaler, 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: 978-961698015-9Xiong, 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.2012.03.020Atmaca, 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.2013.11.054Xiang, 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. 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