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dc.contributor.advisorBarrantes Peña, Enrique José
dc.contributor.authorCárdenas Cabezas, Jian Eduardo
dc.date.accessioned2023-06-20T15:11:16Z
dc.date.available2023-06-20T15:11:16Z
dc.date.created2023
dc.date.issued2023-06-20
dc.identifier.urihttp://hdl.handle.net/20.500.12404/25231
dc.description.abstractThis work presents the dynamic modeling of a refrigeration machine evaporator that uses CO2 (R744) as refrigerant fluid, for the cooling down of a liquid water stream, as required for instance by buildings air handling units. The main goal of such a work is to accurately model the transient evolution of the evaporator outlet superheat, which is one of the main parameters to control, due to its importance in refrigeration systems. A high value of superheat temperature reduces the performance of the system, while a low or null value can generate the suction of liquid which damages the compressor. The theory of moving boundaries [19] with grouped parameters has been used for so. This method allows a precise resolution with a low numerical weight. In this method, the evaporator is divided into only two regions: the two phase region and superheated steam region, in which the energy conservation and mass conservation equations are solved. By using only two control volumes, the number of equations to be solved is smaller, thus reducing the calculation time. The ultimate aim of this work is to serve as a mathematical model usable for the design of efficient refrigeration system controllers, which are one of the most practical ways to improve the performance of these machines. The results of a numerical analysis and of a sensitivity analysis, regarding to the influence of the heat convection coefficient of the two phase region, are also presented. For this sensitivity analysis, the maximum and minimum values available in the literature, see reference [7], have been used. According to this study, the convective coefficient ofCO2 varies from 8000 to 12000 W ·m−2 ·K−1. From this sensitivity analysis, it is observed that, despite the previously mentioned uncertainty about the convective coefficient value, the latter is not influential on the rest of the calculations and on parameters such as internal pressure, length of the two-phase lengths or superheat value. This is due to the fact that the thermal resistance of the liquid hot fluid is much higher than the cold fluid in the phase change region, the global heat transfer coefficient is thus more influenced by the hot fluid thermal resistance. A maximum error of 3 percent is finally estimated in the determination of the transient superheat temperature.es_ES
dc.language.isoenges_ES
dc.publisherPontificia Universidad Católica del Perúes_ES
dc.rightsinfo:eu-repo/semantics/openAccesses_ES
dc.rightsAtribución-NoComercial-CompartirIgual 2.5 Perú*
dc.rights.urihttp://creativecommons.org/licenses/by-nc-sa/2.5/pe/*
dc.subjectRefrigeraciónes_ES
dc.subjectControl de la temperaturaes_ES
dc.subjectControladores programables--Diseño y construcciónes_ES
dc.titleNumerical modeling of a transient state evaporator using object-oriented programminges_ES
dc.typeinfo:eu-repo/semantics/masterThesises_ES
thesis.degree.nameMagíster en Energíaes_ES
thesis.degree.levelMaestríaes_ES
thesis.degree.grantorPontificia Universidad Católica del Perú. Escuela de Posgradoes_ES
thesis.degree.disciplineEnergíaes_ES
dc.type.otherTesis de maestría
dc.subject.ocdehttps://purl.org/pe-repo/ocde/ford#2.07.03es_ES
dc.publisher.countryPEes_ES
renati.advisor.dni07913376
renati.advisor.orcidhttps://orcid.org/0000-0002-9037-3358es_ES
renati.author.dni77025959
renati.discipline711117es_ES
renati.jurorJimenez Ugarte, Fernando Octavioes_ES
renati.jurorBarrantes Peña, Enrique Josees_ES
renati.jurorRojas Chavez, Freddy Jesuses_ES
renati.levelhttps://purl.org/pe-repo/renati/level#maestroes_ES
renati.typehttps://purl.org/pe-repo/renati/type#tesises_ES


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