On falling film evaporator - A review of mechanisms and critical assessment of correlation on a horizontal tube bundle with updated development

被引:9
作者
Lin, Hao-Yu [1 ]
Muneeshwaran, M. [2 ]
Yang, Cheng-Min [2 ]
Nawaz, Kashif [2 ]
Wang, Chi-Chuan [1 ]
机构
[1] Natl Yang Ming Chiao Tung Univ, Dept Mech Engn, Hsinchu 300, Taiwan
[2] Oak Ridge Natl Lab, Bldg Technol Res & Integrat Ctr BTRIC, Multifunct Equipment Integrat Grp, Oak Ridge, TN 37831 USA
关键词
Falling film evaporation; Nucleate boiling; Mist flow heat transfer; Bundle effect; Dry-out; Enhanced tube; BOILING HEAT-TRANSFER; ENHANCED TUBES; LIQUID-FILMS; PART II; PREDICTION; PLAIN; FLUX; DRYOUT; COEFFICIENTS; BREAKDOWN;
D O I
10.1016/j.icheatmasstransfer.2023.107165
中图分类号
O414.1 [热力学];
学科分类号
摘要
Optimization of the energy efficiency and reduction of the greenhouse gas emission for the heat pump system is imperative to meet the net-zero goals at 2050. Chillers with falling film evaporator design not only possess better system performance but also contain less refrigerant inventory. Hence, accurate prediction of the evaporator performance is pivotal especially when charged with low-GWP refrigerant. The present study reviews the correlations for falling film evaporator with a horizontal tube bundle configuration. The major efforts of this study include four tasks: (a) literature review of the experimental studies and available empirical correlations; (b) comprehensive discussion of the falling film evaporation heat transfer mechanism; (c) development of a new rationally based correlation based on available literature; and (d) comparison of different correlations based on the existing data. The collected data includes 4114 data points from 8 sources, 6 refrigerants (R-600a, R-290, R245fa, R-134a, R-1234ze(E), R-123), 5 types of the tubes (Plain, Turbo-GII-HP, GEWA-B, Low-fin, High-Flux), liquid Weber number from 2.2 x 10-6 to 0.7, imposed vapor Weber number from 0 to 37.2, heat flux from 2.5 to 151.5 kW/m2, and film Reynolds number from 1 to 3159.8. The new correlation gives a MAD of 28.3%, and an R2 of 0.86. Yet, the developed correlation considers various heat transfer mechanisms, including the transition point from falling film evaporation to the nucleate boiling, local evaporation, dry-out, mist flow, imposed flow, and enhanced tube effects.
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页数:28
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