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Saturated flow boiling heat transfer of R-407C and associated bubble characteristics in a narrow annular duct
Authors:FC Hsieh  KW Li  YM Lie  CA Chen  TF Lin
Affiliation:1. Institute of Thermofluids, School of Mechanical Engineering, University of Leeds, UK;2. Refrigeration Department, Eng. Division, South Oil Company, Ministry of Oil, Basra, Iraq;3. Department of Thermofluids, Faculty of Mechanical Engineering, Universiti Teknologi Malaysia, 81310 Skudai, Johor Bahru, Malaysia;4. Department of Energy Engineering, Technical College of Engineering, Duhok Polytechnic University (DPU), 61 Zakho Road, 1006 Mazi Qr, Duhok-Kurdistan Region, Iraq;5. Department of Mechanical Engineering, KBU International College, 47800 Petaling Jaya, Selangor, Malaysia;6. Department of oil and gas Engineering, International university of technology twintech, Haddeh street, Sana''a, Yemen;1. Faculty of Physics, LMFTA, USTHB, Algiers 16111, Algeria;2. Faculty of Mechanical Engineering and Process Engineering, LTPMP, USTHB, Algiers 16111, Algeria;3. Department of Mechanical Engineering, The University of Vermont, Burlington, VT 05405, USA
Abstract:Experiments are conducted here to investigate how the channel size affects the R-407C saturated flow boiling heat transfer and associated bubble characteristics in a horizontal narrow annular duct. The gap of the duct is fixed at 1.0 and 2.0 mm in this study. The measured data indicate that the saturated flow boiling heat transfer coefficient increases with a decrease in the duct gap. Besides, raising the imposed heat flux 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 milder. The results from the flow visualization show that the mean diameter of the bubbles departing from the heating surface decreases noticeably at increasing R-407C mass flux. Moreover, the bubble departure frequency increases at reducing duct size and at a high imposed heat flux many bubbles generated from the cavities in the heating surface tend to merge together to form big bubbles. Meanwhile comparison of the present heat transfer data for R-407C with R-134a in the same duct and with some existing correlations is conducted. Furthermore, correlation for the present R-407C saturated flow boiling heat transfer data is proposed. Additionally, the present data for some quantitative bubble characteristics such as the mean bubble departure diameter and frequency and the active nucleation site density are also correlated.
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