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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MDPI AG
2021
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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 |
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DOAJ |
language |
EN |
topic |
condensation heat transfer heat transfer correlation Wilson plot method plate–fin heat exchanger (PFHE) multi-stream PFHE Technology T |
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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 |
work_keys_str_mv |
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1718412359474610176 |