Nucleate Pool Boiling Heat Transfer from High-Flux Tube with Dielectric Fluid HFE-7200

In the present experimental study, nucleate pool boiling heat transfer measurements of two high-flux tubes (sample A and sample B) were conducted at atmospheric pressure with HFE-7200 as the working fluid. Both high-flux tubes were made from a sintered Cu-Ni (high-flux) tube. The porous high-flux su...

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Main Authors: Abhishek Kumar, Kuo-Shu Hung, Chi-Chuan Wang
Format: Article
Language:English
Published: MDPI AG 2020-05-01
Series:Energies
Subjects:
Online Access:https://www.mdpi.com/1996-1073/13/9/2313
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spelling doaj-013e0130cb5b4d449fd6ea5e651a47152020-11-25T04:03:24ZengMDPI AGEnergies1996-10732020-05-01132313231310.3390/en13092313Nucleate Pool Boiling Heat Transfer from High-Flux Tube with Dielectric Fluid HFE-7200Abhishek Kumar0Kuo-Shu Hung1Chi-Chuan Wang2Department of Mechanical Engineering, National Chiao Tung University, Hsinchu 300, TaiwanGreen Energy & Environment Research Laboratories, Industrial Technology Research Institute, Zhudong 310, TaiwanDepartment of Mechanical Engineering, National Chiao Tung University, Hsinchu 300, TaiwanIn the present experimental study, nucleate pool boiling heat transfer measurements of two high-flux tubes (sample A and sample B) were conducted at atmospheric pressure with HFE-7200 as the working fluid. Both high-flux tubes were made from a sintered Cu-Ni (high-flux) tube. The porous high-flux surface was coated inside the test tube with heat flux ranging from 2.6 to 86 kW/m<sup>2</sup>. The major difference between sample A and sample B was the coating thickness, where sample B (0.6 mm) was much larger than that of sample A (0.07 mm). Both tubes showed about three times enhancement in heat transfer coefficient (HTC) when compared to plain tube. Even though sample B contained a higher HTC than sample A, it also revealed a faster level-off phenomenon regarding the HTC vs. wall superheat. The major parameter which characterizes the boiling performance of high-flux tube was the ratio of coating thickness to pore diameter which also yielded different trends upon HTC vs. wall superheat amid sample A and B. It was found that the porous based Nishikawa correlation can well predict the performance of sample A but not sample B. This is because the ratio of coating thickness to pore diameter is far outside the applicable range of the Nishikawa correlation. Hence, a modified Nishikawa correlation is proposed. The predicted capability of the proposed modified Nishikawa correlation against sample A and sample for HTC was within ±28% deviation. The standard mean deviation of the Nishikawa correlation with experimental data for sample A and sample B was 0.302 (12.48%) and 5.64 (73%), respectively.https://www.mdpi.com/1996-1073/13/9/2313high-flux tubeporous surfacepool boilingheat transfer coefficient
collection DOAJ
language English
format Article
sources DOAJ
author Abhishek Kumar
Kuo-Shu Hung
Chi-Chuan Wang
spellingShingle Abhishek Kumar
Kuo-Shu Hung
Chi-Chuan Wang
Nucleate Pool Boiling Heat Transfer from High-Flux Tube with Dielectric Fluid HFE-7200
Energies
high-flux tube
porous surface
pool boiling
heat transfer coefficient
author_facet Abhishek Kumar
Kuo-Shu Hung
Chi-Chuan Wang
author_sort Abhishek Kumar
title Nucleate Pool Boiling Heat Transfer from High-Flux Tube with Dielectric Fluid HFE-7200
title_short Nucleate Pool Boiling Heat Transfer from High-Flux Tube with Dielectric Fluid HFE-7200
title_full Nucleate Pool Boiling Heat Transfer from High-Flux Tube with Dielectric Fluid HFE-7200
title_fullStr Nucleate Pool Boiling Heat Transfer from High-Flux Tube with Dielectric Fluid HFE-7200
title_full_unstemmed Nucleate Pool Boiling Heat Transfer from High-Flux Tube with Dielectric Fluid HFE-7200
title_sort nucleate pool boiling heat transfer from high-flux tube with dielectric fluid hfe-7200
publisher MDPI AG
series Energies
issn 1996-1073
publishDate 2020-05-01
description In the present experimental study, nucleate pool boiling heat transfer measurements of two high-flux tubes (sample A and sample B) were conducted at atmospheric pressure with HFE-7200 as the working fluid. Both high-flux tubes were made from a sintered Cu-Ni (high-flux) tube. The porous high-flux surface was coated inside the test tube with heat flux ranging from 2.6 to 86 kW/m<sup>2</sup>. The major difference between sample A and sample B was the coating thickness, where sample B (0.6 mm) was much larger than that of sample A (0.07 mm). Both tubes showed about three times enhancement in heat transfer coefficient (HTC) when compared to plain tube. Even though sample B contained a higher HTC than sample A, it also revealed a faster level-off phenomenon regarding the HTC vs. wall superheat. The major parameter which characterizes the boiling performance of high-flux tube was the ratio of coating thickness to pore diameter which also yielded different trends upon HTC vs. wall superheat amid sample A and B. It was found that the porous based Nishikawa correlation can well predict the performance of sample A but not sample B. This is because the ratio of coating thickness to pore diameter is far outside the applicable range of the Nishikawa correlation. Hence, a modified Nishikawa correlation is proposed. The predicted capability of the proposed modified Nishikawa correlation against sample A and sample for HTC was within ±28% deviation. The standard mean deviation of the Nishikawa correlation with experimental data for sample A and sample B was 0.302 (12.48%) and 5.64 (73%), respectively.
topic high-flux tube
porous surface
pool boiling
heat transfer coefficient
url https://www.mdpi.com/1996-1073/13/9/2313
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AT kuoshuhung nucleatepoolboilingheattransferfromhighfluxtubewithdielectricfluidhfe7200
AT chichuanwang nucleatepoolboilingheattransferfromhighfluxtubewithdielectricfluidhfe7200
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