2021
DOI: 10.1016/j.csite.2021.100927
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An approximate model of a multilayer wire-on-tube condenser operating with R134a and R600a: Experimental validation and parametric analysis

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Cited by 5 publications
(5 citation statements)
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“…In Figure 2, the scheme of the model used as a reference for the optimization analysis is presented and was validated with stationary experimental data obtained with a real refrigerator. This model was developed in a previous study [25], in which the ε-NTU thermal analysis method and empirical correlations were used, considered as input variables the geometric parameters (Table 1) and the operating conditions of the condenser, as shown in Table 2. The thermal capacity, the air outlet temperature, and the refrigerant outlet temperature were obtained as outputs.…”
Section: Multilayer Wire-on-tube Condensermentioning
confidence: 99%
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“…In Figure 2, the scheme of the model used as a reference for the optimization analysis is presented and was validated with stationary experimental data obtained with a real refrigerator. This model was developed in a previous study [25], in which the ε-NTU thermal analysis method and empirical correlations were used, considered as input variables the geometric parameters (Table 1) and the operating conditions of the condenser, as shown in Table 2. The thermal capacity, the air outlet temperature, and the refrigerant outlet temperature were obtained as outputs.…”
Section: Multilayer Wire-on-tube Condensermentioning
confidence: 99%
“…Considering the maximization of the heat transfer and the minimization of the exchanger area, a multiple set of optimal solutions, known as Pareto optimal solutions, are obtained. According to the model developed for the wire-on-tube condenser [25], the two objective functions that were defined in this work are shown in Equations ( 2) and (3). The total heat transfer of the condenser, .…”
Section: Proposed Objective Functionsmentioning
confidence: 99%
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“…Por otro lado, el condensador se suele modelar con balances energéticos (Purohit et al, 2017), incluyendo el proceso de transferencia de calor con un modelo de tres zonas (Belman-Flores et al, 2021;Cuevas et al, 2009), un modelo de cuatro zonas (Ge and Cropper, 2005), y un modelo con zonas discretizadas (Ge and Cropper, 2009). En el caso del gas cooler, algunos lo modelan empleando balances de energía (Sooben et al, 2019), otros utilizan un modelo de una zona , y otros usan un modelo de zonas discretizadas Martínez-Ballester et al, 2013).…”
Section: Aproximaciones Empleadasunclassified