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...

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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
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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
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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
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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
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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
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eu_rights_str_mv openAccess
dc.format.extent.none.fl_str_mv 22 páginas
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 Case Studies in Thermal Engineering - vol. 27
institution Universidad Tecnológica de Bolívar
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spelling 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. Rivero Application of the exergy concept in the petroleum refining and petrochemical industry Energy Convers. Manag., 43 (2002), pp. 1199-1220A. Valero, M.A. Lozano, M. Muñoz A General Theory of Exergy Saving I, II and III ASME, New York (1986)A. Bejan, G. Tsatsaronis y, M. Moran Thermal Designing and Optimization, New York John Wiley & Sons (1996)P. Ifaei, A. Ataei y, C. Yoo Thermoeconomic and environmental analyses of a low water consumption combined steam power plant and refrigeration chillers-Part 2: thermoeconomic and environmental analysis Energy Convers. Manag., 123 (2016), pp. 625-642C. Yan, L. Lv, S. Wei, A. Eslamimanesh, W. Shen Application of retrofitted design and optimization framework based on the exergy analysis to a crude oil distillation plant Appl. Therm. Eng., 154 (2019), pp. 637-649O.J. Odejobi Exergy and economic analyses of crude oil distillation unit Afr. J. Eng. Res., 3 (2015), pp. 44-55K. Altayib, I. Dincer Analysis and assessment of using an integrated solar energy-based system in a crude oil refinery Appl. Therm. Eng., 159 (2019), p. 12Z. Nur Izyan y, M. Shuhaimi Exergy analysis for fuel reduction strategies in crude distillation unit Energy, 66 (2014), pp. 801-807D. Barreto, J. Fajardo y, J. Campillo Determination of the optimal range of the compressor inlet air temperature in a power plant with stig cycle through of advanced exergetic analysis de ASME Int. Mechan. Eng. Congr. Exposit., Proc., Salt Lake City, 6 (2019) EnergyA. Buelvas, H. Valle y, J. Fajardo Avoidable and unavoidable exergetic destruction analysis of a nitric acid production plant de ASME 2018 Int. Mechan. Eng. Congr. Exposit., Pennsylvania, 6B (2018) EnergyL. Tock, F. Marechal Co-production of hydrogen and electricity from lignocellulosic biomass: process design and thermo-economic optimization Energy, 45 (2012), pp. 339-349P. Caliandro, L. Tock, A.V. Ensinas, F. Marechal Thermo-economic optimization of a solid oxide fuel cell- gas turbine system fuelled with gasified lignocellulosic biomass Energy Convers. Manag., 85 (2014), pp. 764-773D. Brown, M. Gassner, T. Fuchino, F. Maréchal Thermo-economic analysis for the optimal conceptual design of biomass gasification energy conversion systems Appl. Therm. Eng., 29 (2009), pp. 2137-2152M. Rivarolo, B. D, M. A, A. Massardo Hydro-methane and methanol combined production from hydroelectricity and biomass: thermo-economic analysis in Paraguay Energy Convers. Manag., 79 (2014), pp. 74-84G. Singh, P. Singh, V. Tyagi, P. Barnwal, A. Pandey Exergy and thermo-economic analysis of ghee production plant in the dairy industry Energy, 167 (2019), pp. 602-618A. Abusoglu, M. Kanoglu Exergetic and thermoeconomic analyses of diesel engine powered cogeneration: Part 2 – Application Appl. Therm. Eng., 29 (2009), pp. 242-249X. Zhang, R. Zeng, K. Mu, X. Liu, X. Sun, H. Li Exergectic and exergoeconomic evaluation of co-firing biomass with natural gas in CCHP system integrated with ground source heat pump Energy Convers. Manag., 180 (2019), pp. 622-640S. Seyyedi, M. Hashemi-Tilehnoee, M.A. Rosen Exergy and exergoeconomic analyses of a novel integration of a 1000 MW pressurized water reactor power plant and a gas turbine cycle through a superheater Ann. Nucl. Energy, 115 (2018), pp. 161-172L. Castellon, J. Fajardo, B. Sarria Thermoeconomic analysis of wheat flour agroindustrial planta Proceedings of the 15 the International Mechanical Engineering Congress and Exposition, Texas, Houston (2015)M. Bin Shams, E. Elkanzi, Z. Ramadhan, S. Rahma y, M. Khamis Gas turbine inlet air cooling system for enhancing propane recovery in a gas plant: theorical and cost analyses Nat. Gas Sci. Eng. (2017), p. 34M. Callak, F. Balkan, A. Hepbalsi Avoidable and unavoidable exergy destructions of a fluidized bed coal combustor and heat recovery steam generator Energy Convers. Manag., 98 (2015), pp. 54-58H. Nami, A. Nemati, F.J. Fard Conventional and advanced exergy analyses of a geothermal driven dual fluid organic Rankine cycle (ORC) Appl. Therm. Eng. (2017), p. 46O. Balli Advanced exergy analyses to evaluate the performance of a military aircraft turbojet engine (TJE) with afterburner system: splitting exergy destruction into unavoidable/avoidable and endogenous/exogenous Appl. Therm. Eng., 111 (2017), pp. 152-169M. Yari, S.M. Mahmoudi, M. Fallah Advanced exergy analysis for an anode gas recirculation solid oxide fuel cell Energy, 141 (2017), pp. 1097-1112Z. Wang, W. Xion, D.S.-K. Ting, R. Carriveau, Z. Wang Conventional and advanced exergy analyses of an underwater compressed air energy storage system Appl. Energy, 180 (2016), pp. 810-822S. Fellaou, T. Bounahmidi Analyzing thermodynamic improvement potential of a selected cement manufacturing process: advanced exergy analysis Energy, 154 (2018), pp. 190-200A. Pazildar y, S. Sadrameli Conventional and advanced exergoeconomic analyses applied to ethylene refrigeration system of an existing olefin plant Energy Convers. Manag., 138 (2017), pp. 474-485A. Palizdar, T. Ramezani, Z. Nargessi, S. AmirAfshar, M. Abbasi, A. Vatani Advanced exergoeconomic evaluation of a mini-scale nitrogen dual expander process for liquefaction of natural gas Energy, 168 (2019), pp. 542-557M. Mehrpooya, H. Ansarinasab Advanced exergoeconomic evaluation of single mixed refrigerant natural gas liquefaction processes J. Nat. Gas Sci. Eng., 26 (2015), pp. 782-791M. Mehrpooya, S. Ali Mousavi Advanced exergoeconomic assessment of a solar-driven Kalina cycle Energy Convers. Manag., 178 (2018), pp. 78-91H. Ansarinasab, M. Mehrpooya, M. Pouriman Advanced exergoeconomic evaluation of a new cryogenic Helium recovery process from natural gas based on the flash separation - APCI modified process Appl. Therm. Eng., 132 (5) (2017), pp. 368-380D. Barreto, J. Fajardo, G. Carrillo y, Y. Cardenas Advanced and exergoeconomic analysis of a gas power system with steam injection and air cooling with a compression refrigeration machine Energy Technol., 9 (2021), p. 16Y. Cengel Termodinámica, Mexico (2011)S. Turn An introduction to combustion concepts and application (2000)A. Buelvas, J. Fajardo y, H. Valle Conventional and advanced exergoeconomic analysis in a nitric acid production plant Int. Mechan. Eng. Congr. Exposit., Salt Lake City, 6 (2020) EnergyJ. Egzergia Szargut Poradnik obliczania I stosowania Editor: widawnictwo politechniki shlaskej, Gliwice (2007) 129 pagesA. Abusoglu y, M. Kanoglu Exergetic and thermoeconomic analyses of diesel engine powered Appl. Therm. Eng., 29 (2008), pp. 234-241A. Bejan, G. Tsatsaronis y, M. Moran Thermal Design & Optimization JOHN WILEY & SONS, INC, Toronto (1996)L. Wang, Y. Yang, T. Morosuk y, G. Tsatsaronis Advanced thermodynamic analysis and evaluation of a supercritical power plant Energies, 5 (2012), pp. 1850-1863G. Tsatsaronis, K. Solange y, T. Morosuk Endogenous and exogenous exergy destruction in thermal systems Proceedings of International Mechanical Engineering Congress and Exposition-IMECE, vol. 2006 (2006), pp. 311-317G. Tsatsaronis y, M. Park On Avoidable and unavoidable exergy destructions and investment costs in thermal systems Energy Convers. Manag., 43 (2002), pp. 1259-1270J. Couper, W. Penney, J. Fair y, S. Walas Chemical Process Equipment: Selection and Design Butterworth-Heinemann (2010)G. Towler y, R. Sinnott Chemical Engineering Design: Principles, Practice, and Economics of Plant and Process Design Butterworth-Heinemann (2013)J. Fajardo, H. Valley, A. Buelvas Avoidable and unavoidable exergetic destruction analysis of a nitric acid production plant ASME Int. Mechan. Eng. Congr. 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