The Characteristics of Flow Boiling Heat Transfer and Pressure Drop in Small Tube with the Pipe Sections Having Increased Diameters

Article Preview

Abstract:

This study presents an experimental investigation of the characteristics of the flow boiling heat transfer and pressure drop for refrigerant of R134a flowing in a small - diameter evaporative tube with the pipe sections having increased diameters. The experiments were performed at the saturation temperature of 5°C , heat flux of 5.12 ~ 10.96 ( KW/m2), mass flux of 200~600 ( kg/m2s), different length-to-diameter ratios of the test tubes and refrigerant quality of 0.07~0.78, and based on the same surface area of heat transfer. The enhancement performance ratios, θa/s for the tubes with the pipe sections having increased diameters relative to the smooth tube are higher than 1 (about 1.01~1.10). It means that the augmented tubes show the better overall performance than the smooth tube under study.

You might also be interested in these eBooks

Info:

Periodical:

Pages:

525-529

Citation:

Online since:

January 2013

Export:

Price:

Permissions CCC:

Permissions PLS:

Сopyright:

© 2013 Trans Tech Publications Ltd. All Rights Reserved

Share:

Citation:

[1] S. Lin, P.A. Kew, K. Cornwell, Two-phase flow regimes and heat transfer in small tubes and channels, Proceedings of 11th Int. Heat Transfer Conference, Kyongju, Korea, August, 1998, pp.23-28.

Google Scholar

[2] M. -Y. Wen, C. -Y. Ho, J. -K. Jang, Boiling heat transfer of refrigerant R-600a/R-290-oil mixtures in the serpentine small-diameter U-tubes, Appl. Therm. Eng. 27 (2007) 2353-2362.

DOI: 10.1016/j.applthermaleng.2007.03.017

Google Scholar

[3] S. Wongwises, S. Laohalertdecha, J. Kaew-On, W. Duangthongsuk, K. Aroonrat, K. Sakamatapan, Evaporation heat transfer and flow characteristics of R-134a flowing through internally grooved tubes, Int. J. Heat Mass Transfer 47 (2008) 3741-3757.

DOI: 10.1007/s00231-010-0748-6

Google Scholar

[4] R. Bassi, P. K. Bansal, In-tube condensation of mixture of R134a and ester oil: empirical correlations, Int. J. Refrig. 26 (2003) 402–409.

DOI: 10.1016/s0140-7007(02)00152-4

Google Scholar

[5] T. Naulboonrueng, J. Kaew-On, S. Wongwises, Two-phase condensation heat transfer coefficients of HFC-134a at high mass flux in smooth and micro-fin tubes, " Int. Commun. Heat Mass Transfer 30 (2003) 577–590.

DOI: 10.1016/s0735-1933(03)00086-1

Google Scholar

[6] S. Laohalertdecha, S. Wongwises, An Experimental Study into the Evaporation Heat Transfer and Flow Characteristics of R-134a Refrigerant Flowing Through Corrugated Tubes, Int. J. Refrig. 34 (2011) 280-291.

DOI: 10.1016/j.ijrefrig.2010.07.012

Google Scholar

[7] N. Z. Azer, S. T. Lin, L. T. Fan, Augmentation of forced flow boiling heat transfer with Kenics motionless mixers, Industrial and Engineering Chemistry Process Design and Development 19 (1980) 246-250.

DOI: 10.1021/i260074a008

Google Scholar