Evaporation heat transfer enhancement and pressure gradient of R-513A in a horizontal smooth tube (2024)

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Volume 3086, Issue 1

17 May 2024

THE 12TH INTERNATIONAL CONFERENCE ON MECHANICAL ENGINEERING (TSME-ICoME 2022)

14–16 December 2022

phu*ket, Thailand

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Research Article| May 17 2024

Thana Arkadumnuay;

Thana Arkadumnuay

1

Fluid Mechanics, Thermal Engineering and Multiphase Flow Research Lab (FUTURE), Department of Mechanical Engineering, Faculty of Engineering, King Mongkut’s University of Technology Thonburi (KMUTT)

, Bangmod, Bangkok 10140,

Thailand

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Somchai Wongwises

Somchai Wongwises a)

1

Fluid Mechanics, Thermal Engineering and Multiphase Flow Research Lab (FUTURE), Department of Mechanical Engineering, Faculty of Engineering, King Mongkut’s University of Technology Thonburi (KMUTT)

, Bangmod, Bangkok 10140,

Thailand

2

National Science and Technology Development Agency (NSTDA)

, Pathum Thani 12120,

Thailand

a)Corresponding author: somchai.won@kmutt.ac.th

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Author & Article Information

a)Corresponding author: somchai.won@kmutt.ac.th

AIP Conf. Proc. 3086, 090006 (2024)

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Citation

Thana Arkadumnuay, Somchai Wongwises; Evaporation heat transfer enhancement and pressure gradient of R-513A in a horizontal smooth tube. AIP Conf. Proc. 17 May 2024; 3086 (1): 090006. https://doi.org/10.1063/5.0205214

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Experimental studies to determine the average heat transfer coefficient (hav) and frictional pressure gradient (ΔPF/L) of R-513A flowing through a horizontal smooth tube during evaporation are investigated. The experimental setup comprises a double-tube heat exchanger with supplied water circulating inside the annulus in the opposite direction. The average heat transfer coefficient ratio (hav,513A/hav,134a) and frictional pressure gradient ratio ((ΔPF/L)513A/((ΔPF/L)134a) of R-513A and R-134a were compared in this study. The experimental results show hav and ΔPF/L obtained from R-513A are about 0.96 and 0.95 times lower than R-134a, respectively. For R-513A, the hav is lower due to a decreased convective effect, whereas the lower ΔPF/L is due to decreased flow resistance. The Nusselt number (Nu) is higher than R-134a, whereas the two-phase friction factor (fTP) is slightly higher.

Topics

Heat transfer, Engineering thermodynamics

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