Conventional and advanced exergoeconomic indicators of a nitric acid production plant concerning the cooling temperature in compression Train’s intermediate stages
In the refining and petrochemical industrial sector, large amounts of energy are used, so using the concept of exergy allows a rational use of this resource. In the different exergy and exergoeconomics studies applied in petrochemical plants, parameters of interest have been determined to evaluate t...
- Autores:
-
Buelvas Hernández, Ana Margarita
Fajardo Cuadro, Juan Gabriel
Barreto Ponton, Deibys
Carrillo Caballero, Gaylord Enrique
Cardenas Escorcia, Yulineth
Vidal Tovar, Carlos Ramón
Hernández, Yimy Gordon
- Tipo de recurso:
- Fecha de publicación:
- 2021
- Institución:
- Universidad Tecnológica de Bolívar
- Repositorio:
- Repositorio Institucional UTB
- Idioma:
- eng
- OAI Identifier:
- oai:repositorio.utb.edu.co:20.500.12585/10386
- Acceso en línea:
- https://hdl.handle.net/20.500.12585/10386
https://doi.org/10.1016/j.csite.2021.101214.
- Palabra clave:
- Exergoconomy
Endogenous exergy
Exogenous exergy
Avoidable exergy
Inevitable exergy
Exergo-economic indicators
LEMB
- Rights
- openAccess
- License
- http://creativecommons.org/licenses/by-nc-nd/4.0/
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dc.title.spa.fl_str_mv |
Conventional and advanced exergoeconomic indicators of a nitric acid production plant concerning the cooling temperature in compression Train’s intermediate stages |
title |
Conventional and advanced exergoeconomic indicators of a nitric acid production plant concerning the cooling temperature in compression Train’s intermediate stages |
spellingShingle |
Conventional and advanced exergoeconomic indicators of a nitric acid production plant concerning the cooling temperature in compression Train’s intermediate stages Exergoconomy Endogenous exergy Exogenous exergy Avoidable exergy Inevitable exergy Exergo-economic indicators LEMB |
title_short |
Conventional and advanced exergoeconomic indicators of a nitric acid production plant concerning the cooling temperature in compression Train’s intermediate stages |
title_full |
Conventional and advanced exergoeconomic indicators of a nitric acid production plant concerning the cooling temperature in compression Train’s intermediate stages |
title_fullStr |
Conventional and advanced exergoeconomic indicators of a nitric acid production plant concerning the cooling temperature in compression Train’s intermediate stages |
title_full_unstemmed |
Conventional and advanced exergoeconomic indicators of a nitric acid production plant concerning the cooling temperature in compression Train’s intermediate stages |
title_sort |
Conventional and advanced exergoeconomic indicators of a nitric acid production plant concerning the cooling temperature in compression Train’s intermediate stages |
dc.creator.fl_str_mv |
Buelvas Hernández, Ana Margarita Fajardo Cuadro, Juan Gabriel Barreto Ponton, Deibys Carrillo Caballero, Gaylord Enrique Cardenas Escorcia, Yulineth Vidal Tovar, Carlos Ramón Hernández, Yimy Gordon |
dc.contributor.author.none.fl_str_mv |
Buelvas Hernández, Ana Margarita Fajardo Cuadro, Juan Gabriel Barreto Ponton, Deibys Carrillo Caballero, Gaylord Enrique Cardenas Escorcia, Yulineth Vidal Tovar, Carlos Ramón Hernández, Yimy Gordon |
dc.subject.keywords.spa.fl_str_mv |
Exergoconomy Endogenous exergy Exogenous exergy Avoidable exergy Inevitable exergy Exergo-economic indicators |
topic |
Exergoconomy Endogenous exergy Exogenous exergy Avoidable exergy Inevitable exergy Exergo-economic indicators LEMB |
dc.subject.armarc.none.fl_str_mv |
LEMB |
description |
In the refining and petrochemical industrial sector, large amounts of energy are used, so using the concept of exergy allows a rational use of this resource. In the different exergy and exergoeconomics studies applied in petrochemical plants, parameters of interest have been determined to evaluate the thermal efficiency, the potential for process improvement, the irreversibilities produced by the interaction between the components of the system and the operation of each one, and the energy costs associated with each of these irreversibilities. This paper presents an advanced exergy analysis and an exergy-economic analysis applied to a nitric acid production plant with an installed capacity of 350 metric tons per day, whose operating principle is based on the Ostwald method, and both the behavior of endogenous exergy destruction and the behavior of exogenous, avoidable and unavoidable exergy destruction are studied, exogenous, avoidable and unavoidable exergy destruction and the associated exergy costs in each of the heat transfer equipment and reactive equipment that make up the plant, about the cooling temperature in the intermediate stages of the compression train are studied using a mathematical model. The chemical reactions involved in the production process are the points of interest in the research of this work. Some of the results show that 54 % of the total exergy destruction can be recovered by intervening in the components. On the other hand, in the Catalytic Converter (CONV), it is convenient to consider the investment costs to reduce the exergy destruction costs. Similarly, in the Tail Gas Heater (TGH), it is beneficial to reduce the total investment to improve the process economics. On the other hand, the cost of exergy destruction of the plant resulted in 770.77 USD/h. In addition, it could be determined that the interactions between the components significantly affect the investment costs |
publishDate |
2021 |
dc.date.issued.none.fl_str_mv |
2021-07-30 |
dc.date.accessioned.none.fl_str_mv |
2022-01-17T20:57:34Z |
dc.date.available.none.fl_str_mv |
2022-01-17T20:57:34Z |
dc.date.submitted.none.fl_str_mv |
2022-01-07 |
dc.type.driver.spa.fl_str_mv |
info:eu-repo/semantics/article |
dc.type.hasversion.spa.fl_str_mv |
info:eu-repo/semantics/restrictedAccess |
dc.type.spa.spa.fl_str_mv |
http://purl.org/coar/resource_type/c_2df8fbb1 |
dc.identifier.citation.spa.fl_str_mv |
Ana Buelvas Hernández, Juan Gabriel Fajardo, Deibys Barreto, Gaylord Enrique Carrillo Caballero, Yulineth Cárdenas Escorcia, Carlos Ramón Vidal Tovar, Yimy Gordon Hernández, Conventional and advanced exergoeconomic indicators of a nitric acid production plant concerning the cooling temperature in compression Train's intermediate stages, Case Studies in Thermal Engineering, Volume 27, 2021, 101214, ISSN 2214-157X, https://doi.org/10.1016/j.csite.2021.101214. |
dc.identifier.uri.none.fl_str_mv |
https://hdl.handle.net/20.500.12585/10386 |
dc.identifier.doi.none.fl_str_mv |
https://doi.org/10.1016/j.csite.2021.101214. |
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 |
Ana Buelvas Hernández, Juan Gabriel Fajardo, Deibys Barreto, Gaylord Enrique Carrillo Caballero, Yulineth Cárdenas Escorcia, Carlos Ramón Vidal Tovar, Yimy Gordon Hernández, Conventional and advanced exergoeconomic indicators of a nitric acid production plant concerning the cooling temperature in compression Train's intermediate stages, Case Studies in Thermal Engineering, Volume 27, 2021, 101214, ISSN 2214-157X, https://doi.org/10.1016/j.csite.2021.101214. Universidad Tecnológica de Bolívar Repositorio Universidad Tecnológica de Bolívar |
url |
https://hdl.handle.net/20.500.12585/10386 https://doi.org/10.1016/j.csite.2021.101214. |
dc.language.iso.spa.fl_str_mv |
eng |
language |
eng |
dc.rights.coar.fl_str_mv |
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http://creativecommons.org/licenses/by-nc-nd/4.0/ |
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info:eu-repo/semantics/openAccess |
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Attribution-NonCommercial-NoDerivatives 4.0 Internacional |
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http://creativecommons.org/licenses/by-nc-nd/4.0/ Attribution-NonCommercial-NoDerivatives 4.0 Internacional http://purl.org/coar/access_right/c_abf2 |
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openAccess |
dc.format.extent.none.fl_str_mv |
22 páginas |
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application/pdf |
dc.publisher.place.spa.fl_str_mv |
Cartagena de Indias |
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Case Studies in Thermal Engineering - vol. 27 |
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Universidad Tecnológica de Bolívar |
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Buelvas Hernández, Ana Margaritaf7c52408-054a-4928-93a6-b801c648ed9cFajardo Cuadro, Juan Gabriel5e1ca4a8-dc2e-42da-99db-58be11634d3eBarreto Ponton, Deibys9295bc7a-88e7-4c5c-a26a-b285014a141eCarrillo Caballero, Gaylord Enrique095c857b-71a5-4ca2-bb54-94ecb72d2f6dCardenas Escorcia, Yulineth35b31f1a-b0e0-450b-b52e-9f46d2fb6993Vidal Tovar, Carlos Ramóne1015c4b-08ae-4487-a35e-48a8a4716952Hernández, Yimy Gordon89094e91-04e5-4ed7-a0ba-4fbbcbe65bfb2022-01-17T20:57:34Z2022-01-17T20:57:34Z2021-07-302022-01-07Ana Buelvas Hernández, Juan Gabriel Fajardo, Deibys Barreto, Gaylord Enrique Carrillo Caballero, Yulineth Cárdenas Escorcia, Carlos Ramón Vidal Tovar, Yimy Gordon Hernández, Conventional and advanced exergoeconomic indicators of a nitric acid production plant concerning the cooling temperature in compression Train's intermediate stages, Case Studies in Thermal Engineering, Volume 27, 2021, 101214, ISSN 2214-157X, https://doi.org/10.1016/j.csite.2021.101214.https://hdl.handle.net/20.500.12585/10386https://doi.org/10.1016/j.csite.2021.101214.Universidad Tecnológica de BolívarRepositorio Universidad Tecnológica de BolívarIn the refining and petrochemical industrial sector, large amounts of energy are used, so using the concept of exergy allows a rational use of this resource. In the different exergy and exergoeconomics studies applied in petrochemical plants, parameters of interest have been determined to evaluate the thermal efficiency, the potential for process improvement, the irreversibilities produced by the interaction between the components of the system and the operation of each one, and the energy costs associated with each of these irreversibilities. This paper presents an advanced exergy analysis and an exergy-economic analysis applied to a nitric acid production plant with an installed capacity of 350 metric tons per day, whose operating principle is based on the Ostwald method, and both the behavior of endogenous exergy destruction and the behavior of exogenous, avoidable and unavoidable exergy destruction are studied, exogenous, avoidable and unavoidable exergy destruction and the associated exergy costs in each of the heat transfer equipment and reactive equipment that make up the plant, about the cooling temperature in the intermediate stages of the compression train are studied using a mathematical model. The chemical reactions involved in the production process are the points of interest in the research of this work. Some of the results show that 54 % of the total exergy destruction can be recovered by intervening in the components. On the other hand, in the Catalytic Converter (CONV), it is convenient to consider the investment costs to reduce the exergy destruction costs. Similarly, in the Tail Gas Heater (TGH), it is beneficial to reduce the total investment to improve the process economics. On the other hand, the cost of exergy destruction of the plant resulted in 770.77 USD/h. In addition, it could be determined that the interactions between the components significantly affect the investment costs22 páginasapplication/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_abf2Case Studies in Thermal Engineering - vol. 27Conventional and advanced exergoeconomic indicators of a nitric acid production plant concerning the cooling temperature in compression Train’s intermediate stagesinfo:eu-repo/semantics/articleinfo:eu-repo/semantics/restrictedAccesshttp://purl.org/coar/resource_type/c_2df8fbb1ExergoconomyEndogenous exergyExogenous exergyAvoidable exergyInevitable exergyExergo-economic indicatorsLEMBCartagena de IndiasK. Iftekhar, F. Alam y, Q. Alam The global climate change and its effect on power generation Energy Pol. (2013), pp. 1460-1470R. 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