Details
Original language | English |
---|---|
Article number | 121910 |
Journal | International Journal of Heat and Mass Transfer |
Volume | 182 |
Early online date | 21 Sept 2021 |
Publication status | Published - 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
- Physics and Astronomy(all)
- Condensed Matter Physics
- Engineering(all)
- Mechanical Engineering
- Chemical Engineering(all)
- Fluid Flow and Transfer Processes
Cite this
- Standard
- Harvard
- Apa
- Vancouver
- BibTeX
- RIS
In: International Journal of Heat and Mass Transfer, Vol. 182, 121910, 01.2022.
Research output: Contribution to journal › Article › Research › peer review
}
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
UR - http://www.scopus.com/inward/record.url?scp=85115167880&partnerID=8YFLogxK
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 -