R410A flow condensation inside two dimensional micro-fin tubes and three dimensional dimple tubes

Research output: Contribution to journalArticleResearchpeer review

Authors

  • Wei Li
  • Jiacheng Wang
  • Yu Guo
  • Qiyun Shi
  • Yan He
  • David J. Kukulka
  • Xing Luo
  • Stephan Kabelac

External Research Organisations

  • Qingdao University of Science and Technology
  • SUNY Albany
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Details

Original languageEnglish
Article number121910
JournalInternational Journal of Heat and Mass Transfer
Volume182
Early online date21 Sept 2021
Publication statusPublished - Jan 2022

Abstract

Condensation heat transfer characteristics were experimentally investigated inside two dimensional helix micro fin (HX) tubes, three-dimensional dimple (1EHT) tubes and smooth (ST) tubes; while using R410A, for a variety of operating conditions and tube parameters. Tubes evaluated had a length of 2 m, with outer diameters of 9.52 and 12.7 mm; tube materials included copper and stainless steel. Experimental procedure was verified using a single-phase heat balance; with a comparison of results (enhanced tubes to smooth tube) being performed. The condensation experiments were performed at a saturated temperature of 35–45 °C; for the vapor quality range from 0.1 to 0.9; with mass fluxes that ranged from 70 to 450 kg m−2 s−1. Additionally, the effect of various parameters (mass flux, mean vapor quality, saturation temperature, tube thermal conductivity, tube diameter, and surface structure) on the tube side condensation heat transfer was evaluated. For the test conditions considered here the HTC enhancement ratio is in the range from 1.15 to 2.05 for the 1EHT tube and for the HX tube it ranged from 1.18 to 1.69; while the performance factor (PF takes into account the pressure drop) is 1.02–1.57 (1EHT) and 1.23–1.78 (HX). Heat transfer performance of the smooth tube was determined to be slightly affected by the thermal conductivity of the tube; however, for enhanced tubes there is a more dramatic increase in the HTC for an increase of thermal conductivity. Additionally, better heat transfer performance is demonstrated for smaller diameter tubes. Finally, the enhancement effect of the experimental parameters on the enhanced tubes was quantified through the use of a newly introduced evaluation factor.

Keywords

    Dimple tube, Heat transfer coefficient, Helix micro fin tube, R410A, Tube side condensation

ASJC Scopus subject areas

Cite this

R410A flow condensation inside two dimensional micro-fin tubes and three dimensional dimple tubes. / Li, Wei; Wang, Jiacheng; Guo, Yu et al.
In: International Journal of Heat and Mass Transfer, Vol. 182, 121910, 01.2022.

Research output: Contribution to journalArticleResearchpeer review

Li W, Wang J, Guo Y, Shi Q, He Y, Kukulka DJ et al. R410A flow condensation inside two dimensional micro-fin tubes and three dimensional dimple tubes. International Journal of Heat and Mass Transfer. 2022 Jan;182:121910. Epub 2021 Sept 21. doi: 10.1016/j.ijheatmasstransfer.2021.121910
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title = "R410A flow condensation inside two dimensional micro-fin tubes and three dimensional dimple tubes",
abstract = "Condensation heat transfer characteristics were experimentally investigated inside two dimensional helix micro fin (HX) tubes, three-dimensional dimple (1EHT) tubes and smooth (ST) tubes; while using R410A, for a variety of operating conditions and tube parameters. Tubes evaluated had a length of 2 m, with outer diameters of 9.52 and 12.7 mm; tube materials included copper and stainless steel. Experimental procedure was verified using a single-phase heat balance; with a comparison of results (enhanced tubes to smooth tube) being performed. The condensation experiments were performed at a saturated temperature of 35–45 °C; for the vapor quality range from 0.1 to 0.9; with mass fluxes that ranged from 70 to 450 kg m−2 s−1. Additionally, the effect of various parameters (mass flux, mean vapor quality, saturation temperature, tube thermal conductivity, tube diameter, and surface structure) on the tube side condensation heat transfer was evaluated. For the test conditions considered here the HTC enhancement ratio is in the range from 1.15 to 2.05 for the 1EHT tube and for the HX tube it ranged from 1.18 to 1.69; while the performance factor (PF takes into account the pressure drop) is 1.02–1.57 (1EHT) and 1.23–1.78 (HX). Heat transfer performance of the smooth tube was determined to be slightly affected by the thermal conductivity of the tube; however, for enhanced tubes there is a more dramatic increase in the HTC for an increase of thermal conductivity. Additionally, better heat transfer performance is demonstrated for smaller diameter tubes. Finally, the enhancement effect of the experimental parameters on the enhanced tubes was quantified through the use of a newly introduced evaluation factor.",
keywords = "Dimple tube, Heat transfer coefficient, Helix micro fin tube, R410A, Tube side condensation",
author = "Wei Li and Jiacheng Wang and Yu Guo and Qiyun Shi and Yan He and Kukulka, {David J.} and Xing Luo and Stephan Kabelac",
note = "Funding Information: This work is supported by the National Science Foundation of China ( 52076187 ).",
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TY - JOUR

T1 - R410A flow condensation inside two dimensional micro-fin tubes and three dimensional dimple tubes

AU - Li, Wei

AU - Wang, Jiacheng

AU - Guo, Yu

AU - Shi, Qiyun

AU - He, Yan

AU - Kukulka, David J.

AU - Luo, Xing

AU - Kabelac, Stephan

N1 - Funding Information: This work is supported by the National Science Foundation of China ( 52076187 ).

PY - 2022/1

Y1 - 2022/1

N2 - Condensation heat transfer characteristics were experimentally investigated inside two dimensional helix micro fin (HX) tubes, three-dimensional dimple (1EHT) tubes and smooth (ST) tubes; while using R410A, for a variety of operating conditions and tube parameters. Tubes evaluated had a length of 2 m, with outer diameters of 9.52 and 12.7 mm; tube materials included copper and stainless steel. Experimental procedure was verified using a single-phase heat balance; with a comparison of results (enhanced tubes to smooth tube) being performed. The condensation experiments were performed at a saturated temperature of 35–45 °C; for the vapor quality range from 0.1 to 0.9; with mass fluxes that ranged from 70 to 450 kg m−2 s−1. Additionally, the effect of various parameters (mass flux, mean vapor quality, saturation temperature, tube thermal conductivity, tube diameter, and surface structure) on the tube side condensation heat transfer was evaluated. For the test conditions considered here the HTC enhancement ratio is in the range from 1.15 to 2.05 for the 1EHT tube and for the HX tube it ranged from 1.18 to 1.69; while the performance factor (PF takes into account the pressure drop) is 1.02–1.57 (1EHT) and 1.23–1.78 (HX). Heat transfer performance of the smooth tube was determined to be slightly affected by the thermal conductivity of the tube; however, for enhanced tubes there is a more dramatic increase in the HTC for an increase of thermal conductivity. Additionally, better heat transfer performance is demonstrated for smaller diameter tubes. Finally, the enhancement effect of the experimental parameters on the enhanced tubes was quantified through the use of a newly introduced evaluation factor.

AB - Condensation heat transfer characteristics were experimentally investigated inside two dimensional helix micro fin (HX) tubes, three-dimensional dimple (1EHT) tubes and smooth (ST) tubes; while using R410A, for a variety of operating conditions and tube parameters. Tubes evaluated had a length of 2 m, with outer diameters of 9.52 and 12.7 mm; tube materials included copper and stainless steel. Experimental procedure was verified using a single-phase heat balance; with a comparison of results (enhanced tubes to smooth tube) being performed. The condensation experiments were performed at a saturated temperature of 35–45 °C; for the vapor quality range from 0.1 to 0.9; with mass fluxes that ranged from 70 to 450 kg m−2 s−1. Additionally, the effect of various parameters (mass flux, mean vapor quality, saturation temperature, tube thermal conductivity, tube diameter, and surface structure) on the tube side condensation heat transfer was evaluated. For the test conditions considered here the HTC enhancement ratio is in the range from 1.15 to 2.05 for the 1EHT tube and for the HX tube it ranged from 1.18 to 1.69; while the performance factor (PF takes into account the pressure drop) is 1.02–1.57 (1EHT) and 1.23–1.78 (HX). Heat transfer performance of the smooth tube was determined to be slightly affected by the thermal conductivity of the tube; however, for enhanced tubes there is a more dramatic increase in the HTC for an increase of thermal conductivity. Additionally, better heat transfer performance is demonstrated for smaller diameter tubes. Finally, the enhancement effect of the experimental parameters on the enhanced tubes was quantified through the use of a newly introduced evaluation factor.

KW - Dimple tube

KW - Heat transfer coefficient

KW - Helix micro fin tube

KW - R410A

KW - Tube side condensation

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U2 - 10.1016/j.ijheatmasstransfer.2021.121910

DO - 10.1016/j.ijheatmasstransfer.2021.121910

M3 - Article

AN - SCOPUS:85115167880

VL - 182

JO - International Journal of Heat and Mass Transfer

JF - International Journal of Heat and Mass Transfer

SN - 0017-9310

M1 - 121910

ER -