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dc.contributor.authorVera Romero, Iván-
dc.contributor.authorHeard Wade, Christopher Lionel-
dc.date.accessioned2018-09-10T16:04:34Z-
dc.date.available2018-09-10T16:04:34Z-
dc.date.issued2018-01-01-
dc.identifier.citationVera Romero, I. & Heard Wade, C. L. (2018). Evaluation of irreversibility in an ammonia-water absorption refrigeration system using three different mathematical models to calculate the thermodynamic properties. Revista Facultad de Ingeniería, 27(47), 9-19. https://doi.org/10.19053/01211129.v27.n47.2018.7746.spa
dc.identifier.issn2357-5328-
dc.identifier.urihttp://repositorio.uptc.edu.co/handle/001/2169-
dc.description1 recurso en línea (páginas 9-19).spa
dc.description.abstractLos 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.spa
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dc.language.isoengspa
dc.publisherUniversidad Pedagógica y Tecnológica de Colombiaspa
dc.relation.ispartofseriesRevista Facultad de Ingeniería;Volumen 27, número 47 (Enero-Abril 2018)-
dc.rightsCopyright (c) 2018 Universidad Pedagógica y Tecnológica de Colombiaspa
dc.rights.urihttps://creativecommons.org/licenses/by-nc/4.0/spa
dc.sourcehttps://revistas.uptc.edu.co/index.php/ingenieria/article/view/7746/6136spa
dc.titleEvaluation of irreversibility in an ammonia-water absorption refrigeration system using three different mathematical models to calculate the thermodynamic propertiesspa
dc.title.alternativeEvaluación de irreversibilidades en un sistema de refrigeración por absorción amoniaco-agua empleando tres modelos matemáticos diferentes para calcular las propiedades termodinámicasspa
dc.title.alternativeAvaliação de irreversibilidades em um sistema de refrigeração por absorção amoníaco-água empregando três modelos matemáticos diferentes para calcular as propriedades termodinâmicasspa
dc.typeArtículo de revistaspa
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dc.description.notesBibliografía: páginas 17-19.spa
dc.rights.accessrightsinfo:eu-repo/semantics/openAccessspa
dc.type.dcmi-type-vocabularyTextspa
dc.type.driverinfo:eu-repo/semantics/articlespa
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dc.description.abstractenglishSecond 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.spa
dc.description.abstractportuguesAs análises por Segunda Lei, ou de Exergia, nos Sistemas de Refrigeração por Absorção (SRA) são muito importantes, já que permitem realizar análises de optimização de acordo com o trabalho disponível, os quais se estabelecem a partir das condições de operação e do cálculo de suas propriedades. Para a modelagem destes sistemas existem diversas metodologias de cálculo para as propriedades termodinâmicas. Neste trabalho realizase um estudo termodinâmico sobre um SRA com a mistura amoníaco-água proposta (Caso Base), com a finalidade de avaliar a sensibilidade nas irreversibilidades globais e por equipamento. Para tal propósito, empregaram-se três metodologias existentes: (M1) o modelo de Ibrahim e Klein (1993), através do software comercial Engineering Equation Solver (EES); (M2) o modelo proposto por Tillner-Roth e Friend (1998), através do software REFPROP v.8.0, desenvolvido pelo National Institute of Standars and Technology (NIST), e (M3) a metodologia proposta por Xu e Goswami (1999), programada para esta análise. As diferenças entre as propriedades obtidas e o funcionamento do SRA por Primeira Lei não são significativas na avaliação do COP, obtendo variações mínimas (Caso Base: 0.595, M1: 0.596, M2: 0.594, M3: 0.599). Para a análise por Segunda Lei, a irreversibilidade total do sistema para os três modelos resultou ser a mesma (Irr Global: 123.339 kW), apesar de que na irreversibilidade por equipamento sobressaem as diferenças entre o Intercambiador da Solução (M1: 5.783kW, M2: 6.122kW, M3: 8.701kW), o Dessorbedor (M1: 51.302kW, M2: 45.713kW, M3: 49.098kW) e o Retificador (M1: 0.766kW, M2: 3.565kW, M3: 0.427kW). Os equipamentos que mais destroem exergia são o Dessorbedor, o Absorvedor e o Condensador, respectivamente.spa
dc.identifier.doihttps://doi.org/10.19053/01211129.v27.n47.2018.7746-
dc.rights.creativecommonsAtribución-NoComercialspa
dc.subject.armarcHeat -Radiation and absortion-
dc.subject.armarcProcess control-
dc.subject.proposalAmmonia-water propertiesspa
dc.subject.proposalAbsorption refrigerationspa
dc.subject.proposalCoefficient of performancespa
dc.subject.proposalIrreversibilityspa
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