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Subcooled flow boiling heat transfer of R-407C and associated bubble characteristics in a narrow annular duct
Authors:CA Chen  WR Chang  KW Li  YM Lie  TF Lin
Affiliation:1. State Key Laboratory of Multiphase Flow in Power Engineering, Xi’an Jiaotong University, No. 28 Xianning West Road, Xi’an 710049, China;2. Southwestern Institute of Physics, P.O. Box 432, Chengdu 610041, China;1. Department of Chemistry, Aristotle University of Thessaloniki, University Box 116, 54124 Thessaloniki, Greece;2. Mechanical Engineering Department, Technical University of Serres, 62124 Serres, Greece;1. School of Energy and Power Engineering, Huazhong University of Science and Technology, Wuhan 430074, China;2. Dongfeng Commercial Vehicle Technical Center, Wuhan, China;1. Department of Nuclear, Plasma, and Radiological Engineering, University of Illinois, Urbana, IL 61801, USA;2. School of Nuclear Engineering, Purdue University, West Lafayette, IN 47907-1290, USA
Abstract:An experiment is conducted here to investigate how the channel size affects the subcooled flow boiling heat transfer and the associated bubble characteristics of refrigerant R-407C in a horizontal narrow annular duct with the gap of the duct fixed at 1.0 and 2.0 mm. The measured boiling curves indicate that the temperature overshoot at ONB is relatively significant for the subcooled flow boiling of R-407C in the duct. Besides, the subcooled flow boiling heat transfer coefficient increases with a reduction in the duct gap, but decreases with an increase in the inlet liquid subcooling. Moreover, raising the heat flux imposed on the duct can cause a significant increase in the boiling heat transfer coefficients. However, the effects of the refrigerant mass flux and saturated temperature on the boiling heat transfer coefficient are slighter. Visualization of the subcooled flow boiling processes in the duct reveals that the bubbles are suppressed to become smaller and less dense by raising the refrigerant mass flux and inlet subcooling. Raising the imposed heat flux, however, produces positive effects on the bubble population, coalescence and departure frequency. Meanwhile, the present heat transfer data for R-407C are compared with the R-134a data measured in the same duct and with some existing correlations. We also propose empirical correlations for the present data for the R-407C subcooled flow boiling heat transfer and some quantitative bubble characteristics such as the mean bubble departure diameter and frequency and the active nucleation site density.
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