Evaluation of irreversibility in an ammonia-water absorption refrigeration system using three different mathematical models to calculate the thermodynamic properties

Second Law or Exergy Analyses of Absorption Refrigeration Systems (ARS) are very important for optimisations based on available work; these analyses are derived from the operating conditions and property calculations. There are several methods available for calculating the thermodynamic properties u...

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Fecha de publicación:
2018
Institución:
Universidad Pedagógica y Tecnológica de Colombia
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RiUPTC: Repositorio Institucional UPTC
Idioma:
eng
OAI Identifier:
oai:repositorio.uptc.edu.co:001/14202
Acceso en línea:
https://revistas.uptc.edu.co/index.php/ingenieria/article/view/7746
https://repositorio.uptc.edu.co/handle/001/14202
Palabra clave:
ammonia-water properties
absorption refrigeration
coefficient of performance
irreversibility
coeficiente de desempeño
irreversibilidad
propiedades amoniaco-agua
sistema de refrigeración por absorción
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Copyright (c) 2018 Iván Vera-Romero, Christopher Lionel Heard-Wade
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network_name_str RiUPTC: Repositorio Institucional UPTC
repository_id_str
dc.title.en-US.fl_str_mv Evaluation of irreversibility in an ammonia-water absorption refrigeration system using three different mathematical models to calculate the thermodynamic properties
dc.title.es-ES.fl_str_mv Evaluación de irreversibilidades en un sistema de refrigeración por absorción amoniaco-agua empleando tres modelos matemáticos diferentes para calcular las propiedades termodinámicas
title Evaluation of irreversibility in an ammonia-water absorption refrigeration system using three different mathematical models to calculate the thermodynamic properties
spellingShingle Evaluation of irreversibility in an ammonia-water absorption refrigeration system using three different mathematical models to calculate the thermodynamic properties
ammonia-water properties
absorption refrigeration
coefficient of performance
irreversibility
coeficiente de desempeño
irreversibilidad
propiedades amoniaco-agua
sistema de refrigeración por absorción
title_short Evaluation of irreversibility in an ammonia-water absorption refrigeration system using three different mathematical models to calculate the thermodynamic properties
title_full Evaluation of irreversibility in an ammonia-water absorption refrigeration system using three different mathematical models to calculate the thermodynamic properties
title_fullStr Evaluation of irreversibility in an ammonia-water absorption refrigeration system using three different mathematical models to calculate the thermodynamic properties
title_full_unstemmed Evaluation of irreversibility in an ammonia-water absorption refrigeration system using three different mathematical models to calculate the thermodynamic properties
title_sort Evaluation of irreversibility in an ammonia-water absorption refrigeration system using three different mathematical models to calculate the thermodynamic properties
dc.subject.en-US.fl_str_mv ammonia-water properties
absorption refrigeration
coefficient of performance
irreversibility
topic ammonia-water properties
absorption refrigeration
coefficient of performance
irreversibility
coeficiente de desempeño
irreversibilidad
propiedades amoniaco-agua
sistema de refrigeración por absorción
dc.subject.es-ES.fl_str_mv coeficiente de desempeño
irreversibilidad
propiedades amoniaco-agua
sistema de refrigeración por absorción
description Second Law or Exergy Analyses of Absorption Refrigeration Systems (ARS) are very important for optimisations based on available work; these analyses are derived from the operating conditions and property calculations. There are several methods available for calculating the thermodynamic properties used in modelling these systems. A thermodynamic study on an ARS with the ammonia-water mixture (base case) was carried out with the objective of analysing the sensitivity of the overall and individual component irreversibility to the thermodynamic property. To this end, three existing methods were used: (M1), a model proposed by Ibrahim and Klein (1993) and used in the Engineering Equation Solver (EES) commercial software; (M2), a model proposed by Tillner-Roth and Friend (1998) and embodied in REFPROP v.8.0 developed by the National Institute of Standards and Technology (NIST); and (M3), a method proposed by Xu and Goswami (1999) that was programmed for this analysis. The obtained differences in the properties and the first law performance of the ARS are insignificant in the determination of the coefficient of performance (COP) (base case: 0.595, M1: 0.596, M2: 0.594, M3: 0.599). For the second law analysis, the overall irreversibility was the same (123.339kW) despite the irreversibilities per component had important differences: the solution heat exchanger (M1: 5.783kW, M2: 6.122kW, M3: 8.701kW), the desorber (generator) (M1: 51.302kW, M2: 45.713kW, M3: 49.098kW) and the rectifier (M1: 0.766kW, M2: 3.565kW, M3: 0.427kW). The components that destroy exergy the most are the desorber, the absorber and the condenser.
publishDate 2018
dc.date.accessioned.none.fl_str_mv 2024-07-05T19:11:34Z
dc.date.available.none.fl_str_mv 2024-07-05T19:11:34Z
dc.date.none.fl_str_mv 2018-01-15
dc.type.en-US.fl_str_mv research
dc.type.es-ES.fl_str_mv investigación
dc.type.none.fl_str_mv info:eu-repo/semantics/article
dc.type.coar.fl_str_mv http://purl.org/coar/resource_type/c_2df8fbb1
dc.type.coarversion.fl_str_mv http://purl.org/coar/version/c_970fb48d4fbd8a85
dc.type.version.spa.fl_str_mv info:eu-repo/semantics/publishedVersion
dc.type.coarversion.spa.fl_str_mv http://purl.org/coar/version/c_970fb48d4fbd8a359
status_str publishedVersion
dc.identifier.none.fl_str_mv https://revistas.uptc.edu.co/index.php/ingenieria/article/view/7746
10.19053/01211129.v27.n47.2018.7746
dc.identifier.uri.none.fl_str_mv https://repositorio.uptc.edu.co/handle/001/14202
url https://revistas.uptc.edu.co/index.php/ingenieria/article/view/7746
https://repositorio.uptc.edu.co/handle/001/14202
identifier_str_mv 10.19053/01211129.v27.n47.2018.7746
dc.language.none.fl_str_mv eng
dc.language.iso.spa.fl_str_mv eng
language eng
dc.relation.none.fl_str_mv https://revistas.uptc.edu.co/index.php/ingenieria/article/view/7746/6136
https://revistas.uptc.edu.co/index.php/ingenieria/article/view/7746/7178
dc.rights.en-US.fl_str_mv Copyright (c) 2018 Iván Vera-Romero, Christopher Lionel Heard-Wade
dc.rights.coar.fl_str_mv http://purl.org/coar/access_right/c_abf2
dc.rights.coar.spa.fl_str_mv http://purl.org/coar/access_right/c_abf276
rights_invalid_str_mv Copyright (c) 2018 Iván Vera-Romero, Christopher Lionel Heard-Wade
http://purl.org/coar/access_right/c_abf276
http://purl.org/coar/access_right/c_abf2
dc.format.none.fl_str_mv application/pdf
application/xml
dc.publisher.en-US.fl_str_mv Universidad Pedagógica y Tecnológica de Colombia
dc.source.en-US.fl_str_mv Revista Facultad de Ingeniería; Vol. 27 No. 47 (2018); 9-19
dc.source.es-ES.fl_str_mv Revista Facultad de Ingeniería; Vol. 27 Núm. 47 (2018); 9-19
dc.source.none.fl_str_mv 2357-5328
0121-1129
institution Universidad Pedagógica y Tecnológica de Colombia
repository.name.fl_str_mv Repositorio Institucional UPTC
repository.mail.fl_str_mv repositorio.uptc@uptc.edu.co
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spelling 2018-01-152024-07-05T19:11:34Z2024-07-05T19:11:34Zhttps://revistas.uptc.edu.co/index.php/ingenieria/article/view/774610.19053/01211129.v27.n47.2018.7746https://repositorio.uptc.edu.co/handle/001/14202Second Law or Exergy Analyses of Absorption Refrigeration Systems (ARS) are very important for optimisations based on available work; these analyses are derived from the operating conditions and property calculations. There are several methods available for calculating the thermodynamic properties used in modelling these systems. A thermodynamic study on an ARS with the ammonia-water mixture (base case) was carried out with the objective of analysing the sensitivity of the overall and individual component irreversibility to the thermodynamic property. To this end, three existing methods were used: (M1), a model proposed by Ibrahim and Klein (1993) and used in the Engineering Equation Solver (EES) commercial software; (M2), a model proposed by Tillner-Roth and Friend (1998) and embodied in REFPROP v.8.0 developed by the National Institute of Standards and Technology (NIST); and (M3), a method proposed by Xu and Goswami (1999) that was programmed for this analysis. The obtained differences in the properties and the first law performance of the ARS are insignificant in the determination of the coefficient of performance (COP) (base case: 0.595, M1: 0.596, M2: 0.594, M3: 0.599). For the second law analysis, the overall irreversibility was the same (123.339kW) despite the irreversibilities per component had important differences: the solution heat exchanger (M1: 5.783kW, M2: 6.122kW, M3: 8.701kW), the desorber (generator) (M1: 51.302kW, M2: 45.713kW, M3: 49.098kW) and the rectifier (M1: 0.766kW, M2: 3.565kW, M3: 0.427kW). The components that destroy exergy the most are the desorber, the absorber and the condenser.Los análisis por Segunda Ley, o de Exergia, en los Sistemas de Refrigeración por Absorción (SRA) son muy importantes, ya que permiten realizar análisis de optimización de acuerdo con el trabajo disponible, los cuales se establecen a partir de las condiciones de operación y del cálculo de sus propiedades. Para el modelado de estos sistemas existen diversas metodologías de cálculo para las propiedades termodinámicas. En este trabajo se realiza un estudio termodinámico sobre un SRA con mezcla amoniaco-agua propuesto (Caso Base), con la finalidad de evaluar la sensibilidad en las irreversibilidades globales y por equipo. Para tal efecto se emplearon tres metodologías existentes: (M1) el modelo de Ibrahim y Klein (1993), a través del software comercial Engineering Equation Solver (EES); (M2) el modelo propuesto por Tillner-Roth y Friend (1998), a través del software REFPROP v.8.0, desarrollado por el National Institute of Standars and Technology (NIST), y (M3) la metodología propuesta por Xu y Goswami (1999), programada para este análisis. Las diferencias entre las propiedades obtenidas y el funcionamiento del SRA por Primera Ley no son significativas en la evaluación del COP, obteniendo variaciones mínimas (Caso Base: 0.595, M1: 0.596, M2: 0.594, M3: 0.599). Para el análisis por Segunda Ley, la irreversibilidad total del sistema para los tres modelos resultó ser la misma (Irr Global: 123.339 kW), a pesar de que en la irreversibilidad por equipo sobresalen las diferencias entre el Intercambiador de la Solución (M1: 5.783kW, M2: 6.122kW, M3: 8.701kW), el Desorbedor (M1: 51.302kW, M2: 45.713kW, M3: 49.098kW) y el Rectificador (M1: 0.766kW, M2: 3.565kW, M3: 0.427kW). Los equipos que más destruyen exergia son el Desorbedor, el Absorbedor y el Condensador, respectivamente.application/pdfapplication/xmlengengUniversidad Pedagógica y Tecnológica de Colombiahttps://revistas.uptc.edu.co/index.php/ingenieria/article/view/7746/6136https://revistas.uptc.edu.co/index.php/ingenieria/article/view/7746/7178Copyright (c) 2018 Iván Vera-Romero, Christopher Lionel Heard-Wadehttp://purl.org/coar/access_right/c_abf276http://purl.org/coar/access_right/c_abf2Revista Facultad de Ingeniería; Vol. 27 No. 47 (2018); 9-19Revista Facultad de Ingeniería; Vol. 27 Núm. 47 (2018); 9-192357-53280121-1129ammonia-water propertiesabsorption refrigerationcoefficient of performanceirreversibilitycoeficiente de desempeñoirreversibilidadpropiedades amoniaco-aguasistema de refrigeración por absorciónEvaluation of irreversibility in an ammonia-water absorption refrigeration system using three different mathematical models to calculate the thermodynamic propertiesEvaluación de irreversibilidades en un sistema de refrigeración por absorción amoniaco-agua empleando tres modelos matemáticos diferentes para calcular las propiedades termodinámicasresearchinvestigacióninfo:eu-repo/semantics/articlehttp://purl.org/coar/resource_type/c_2df8fbb1info:eu-repo/semantics/publishedVersionhttp://purl.org/coar/version/c_970fb48d4fbd8a359http://purl.org/coar/version/c_970fb48d4fbd8a85Vera-Romero, IvánHeard-Wade, Christopher Lionel001/14202oai:repositorio.uptc.edu.co:001/142022025-07-18 11:53:44.28metadata.onlyhttps://repositorio.uptc.edu.coRepositorio Institucional UPTCrepositorio.uptc@uptc.edu.co