Experimental Study of Local Heat Transfer Coefficient of R113 Flow Boiling in Vertical Square Tube

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Abstract:

This article is based on the experimental investigations on flow boiling heat transfer of R113 with the equivalent diameter of the square tube 15.66mm, mass flow rate 500 ~ 2000kg / (m2•s), steam quality from 0.1 to 1, heat flux 50 ~ 90kW/m2, and pressure 100 ~ 250 kPa. The experimental results show that with the rise of heat flux and mass velocity the local convection heat transfer coefficient increases, and with the enhancement of steam quality the local convection heat transfer coefficient increases firstly and then decreases. By comparison of the experimental data and the calculation results of predecessor’s correlations, a correction coefficient applicable to this experiment was obtained.

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Periodical:

Advanced Materials Research (Volumes 374-377)

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622-625

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October 2011

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© 2012 Trans Tech Publications Ltd. All Rights Reserved

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[1] Guo Y J, Bi Q C, He Y Q, Zhou Y, Chen T K. Research on air-water flow in vertical noncircular channels. Nuclear Power Engineering 2006, 27(5): 8~53.

Google Scholar

[2] Yang Z C, Bi Q C, Yang D, Chen T K. Non-circular small channels of water in a vertical upward flow of air research .Engineering Thermo physics 2006,27(5):787-790.

Google Scholar

[3] A. Greco Convective boiling of pure and mixed refrigerants: An experimental study of the major parameters affecting heat transfer. International Journal of Heat and Mass Transfer 2008,51:896-909.

DOI: 10.1016/j.ijheatmasstransfer.2007.11.002

Google Scholar

[4] Zhang X L, Cai Z H, Li M L. HFC2134a and CFC212 experimental comparison of horizontal tube flow boiling heat transfer coefficient . Journal of East China University of technology 1996,18(3):51-55.

Google Scholar

[5] Chen J B, Cai Z H, Ding Y M, Zhang X L. R12 experimental study on flow boiling heat transfer in a horizontal tube . Journal of Shanghai Institute of machinery 1992,14(3): 1-9.

Google Scholar

[6] Chen Y M, Hu R J, Chen Y H. Heating channel vertical gas-liquid two phase flow heat transfer performance .chemical industry and engineering 9(2):1-7.

Google Scholar

[7] Bi Q C, Zhou Y, Chen T K. Researches on Two-Phase Flow Patterns in Circular and Triangular Channels. 5th International Conference on Multiphase Flow (ICMF'04), Yokohama Japan, 2004, Paper No. 167.

Google Scholar

[8] Kandlikar S.G. An improved correlation for predicting two-phase flow boiing heat transfer coefficient in horizontal and vertical tubes. ASME.HTD,1983, 27:3-10.

Google Scholar