Effects of Experimental Parameters on Condensation Heat Transfer in Plate Fin Heat Exchanger

This study aims to provide an experimental investigation and comparison of the condensation heat transfer characteristics in a plate–fin heat exchanger (PFHE). The heat flux, mass flux, and saturation pressure were adjusted as experimental parameters to verify the effects on the condensation heat tr...

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Autores principales: Sung-Hoon Seol, Sun-Geun Lee, Chang-Hyo Son, Ji-Hoon Yoon, In-Seob Eom, Young-Min Park, Jung-In Yoon
Formato: article
Lenguaje:EN
Publicado: MDPI AG 2021
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Acceso en línea:https://doaj.org/article/851a7b06ae774b04bb9c019189b351cd
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spelling oai:doaj.org-article:851a7b06ae774b04bb9c019189b351cd2021-11-25T17:27:51ZEffects of Experimental Parameters on Condensation Heat Transfer in Plate Fin Heat Exchanger10.3390/en142276811996-1073https://doaj.org/article/851a7b06ae774b04bb9c019189b351cd2021-11-01T00:00:00Zhttps://www.mdpi.com/1996-1073/14/22/7681https://doaj.org/toc/1996-1073This study aims to provide an experimental investigation and comparison of the condensation heat transfer characteristics in a plate–fin heat exchanger (PFHE). The heat flux, mass flux, and saturation pressure were adjusted as experimental parameters to verify the effects on the condensation heat transfer. In addition, condensation heat transfer correlation of two-stream PFHEs was provided based on the experimental data for utilization as a design reference for the heat exchanger. The turbulence is the most influential in heat transfer. One of the ways to foster turbulence is to increase shear stress. The higher flow velocity results in the higher shear stress. That was why increasing mass flux or the flow with higher vapor quality showed the higher heat transfer coefficient (HTC). Refrigerant properties such as viscosity and specific volume of vapor changed according to the saturation pressure. It is expected they affect the degree of turbulence too in similar manners. The mass flux was more influential than the heat flux and saturation pressure. Thus, the equivalent mass flux of the refrigerant is dominant in the derived correlation model. The average difference between experimental and calculated HTC from correlations was about 6.5%. Multi-stream PFHE comprises an additional heat transfer surface, which implies a more active droplet formation. The average pressure drop in the multi-stream is 15% larger than that of the two-stream.Sung-Hoon SeolSun-Geun LeeChang-Hyo SonJi-Hoon YoonIn-Seob EomYoung-Min ParkJung-In YoonMDPI AGarticlecondensation heat transferheat transfer correlationWilson plot methodplate–fin heat exchanger (PFHE)multi-stream PFHETechnologyTENEnergies, Vol 14, Iss 7681, p 7681 (2021)
institution DOAJ
collection DOAJ
language EN
topic condensation heat transfer
heat transfer correlation
Wilson plot method
plate–fin heat exchanger (PFHE)
multi-stream PFHE
Technology
T
spellingShingle condensation heat transfer
heat transfer correlation
Wilson plot method
plate–fin heat exchanger (PFHE)
multi-stream PFHE
Technology
T
Sung-Hoon Seol
Sun-Geun Lee
Chang-Hyo Son
Ji-Hoon Yoon
In-Seob Eom
Young-Min Park
Jung-In Yoon
Effects of Experimental Parameters on Condensation Heat Transfer in Plate Fin Heat Exchanger
description This study aims to provide an experimental investigation and comparison of the condensation heat transfer characteristics in a plate–fin heat exchanger (PFHE). The heat flux, mass flux, and saturation pressure were adjusted as experimental parameters to verify the effects on the condensation heat transfer. In addition, condensation heat transfer correlation of two-stream PFHEs was provided based on the experimental data for utilization as a design reference for the heat exchanger. The turbulence is the most influential in heat transfer. One of the ways to foster turbulence is to increase shear stress. The higher flow velocity results in the higher shear stress. That was why increasing mass flux or the flow with higher vapor quality showed the higher heat transfer coefficient (HTC). Refrigerant properties such as viscosity and specific volume of vapor changed according to the saturation pressure. It is expected they affect the degree of turbulence too in similar manners. The mass flux was more influential than the heat flux and saturation pressure. Thus, the equivalent mass flux of the refrigerant is dominant in the derived correlation model. The average difference between experimental and calculated HTC from correlations was about 6.5%. Multi-stream PFHE comprises an additional heat transfer surface, which implies a more active droplet formation. The average pressure drop in the multi-stream is 15% larger than that of the two-stream.
format article
author Sung-Hoon Seol
Sun-Geun Lee
Chang-Hyo Son
Ji-Hoon Yoon
In-Seob Eom
Young-Min Park
Jung-In Yoon
author_facet Sung-Hoon Seol
Sun-Geun Lee
Chang-Hyo Son
Ji-Hoon Yoon
In-Seob Eom
Young-Min Park
Jung-In Yoon
author_sort Sung-Hoon Seol
title Effects of Experimental Parameters on Condensation Heat Transfer in Plate Fin Heat Exchanger
title_short Effects of Experimental Parameters on Condensation Heat Transfer in Plate Fin Heat Exchanger
title_full Effects of Experimental Parameters on Condensation Heat Transfer in Plate Fin Heat Exchanger
title_fullStr Effects of Experimental Parameters on Condensation Heat Transfer in Plate Fin Heat Exchanger
title_full_unstemmed Effects of Experimental Parameters on Condensation Heat Transfer in Plate Fin Heat Exchanger
title_sort effects of experimental parameters on condensation heat transfer in plate fin heat exchanger
publisher MDPI AG
publishDate 2021
url https://doaj.org/article/851a7b06ae774b04bb9c019189b351cd
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