Flow boiling heat transfer of R134a and low GWP refrigerants in a horizontal micro-scale channel

被引:69
|
作者
Sempertegui-Tapia, Daniel Felipe [1 ]
Ribatski, Gherhardt [2 ]
机构
[1] Brunel Univ London, Coll Engn Design & Phys Sci, London, England
[2] Univ Sao Paulo, EESC, Heat Transfer Res Grp, Sao Carlos, SP, Brazil
基金
巴西圣保罗研究基金会;
关键词
Two-phase flow; Heat transfer coefficient; Micro-scale channels; R1234ze(E); R1234yf; R600a; Low GWP; PRESSURE-DROP; GENERAL CORRELATION; TRANSFER MODEL; 2-PHASE FLOW; MICROCHANNELS; R1234YF; TUBE; MINICHANNELS; PERFORMANCE; EVAPORATION;
D O I
10.1016/j.ijheatmasstransfer.2017.01.036
中图分类号
O414.1 [热力学];
学科分类号
摘要
The present paper presents an investigation of the effects of the refrigerant type on the heat transfer coefficient during flow boiling inside micro-scale channels. Experimental results for R134a, R1234ze(E), R1234yf and R600a for flow boiling in a circular channel with internal diameter of 1.1 mm are presented. The experimental database comprises 3409 data points covering mass velocities ranging from 200 to 800 kg/m(2) s, heat fluxes from 15 to 145 kW/m(2), saturation temperatures of 31 and 41 degrees C, and vapor qualities from 0.05 to 0.95. The experimental data were parametrically analysed and the effects of the experimental parameters (heat flux, mass velocity, saturation temperature and working fluid) identified. Subsequently, the experimental data were compared against the most quoted predictive methods from literature, including macro and micro-scale methods. Based on the broad database obtained in the present study, an updated version of the predictive method of Kanizawa et al. (2016) was proposed. The updated version provided accurate predictions of the present experimental database, predicting more than 97% and 86% of the results within error bands of 30 and 20%, respectively. (C) 2017 Elsevier Ltd. All rights reserved.
引用
收藏
页码:2417 / 2432
页数:16
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