Experimental analysis of ammonia condensation on smooth and integral-fin titanium tubes

被引:16
作者
Fernandez-Seara, Jose [1 ]
Uhia, Francisco J. [1 ]
Diz, Ruben [1 ]
机构
[1] Univ Vigo, Area Maquinas & Motores Term, ETS Ingenieros Ind, Vigo 36310, Spain
来源
INTERNATIONAL JOURNAL OF REFRIGERATION-REVUE INTERNATIONALE DU FROID | 2009年 / 32卷 / 06期
关键词
Heat exchanger; Condenser; Ammonia; Experiment; Condensation; Smooth tube; Finned tube; Material; Titanium; Heat transfer coefficient; HEAT-TRANSFER; REFRIGERATION; COEFFICIENT; SYSTEMS; VAPOR;
D O I
10.1016/j.ijrefrig.2009.01.026
中图分类号
O414.1 [热力学];
学科分类号
摘要
This paper reports on the experimental research conducted to study the condensation of ammonia on smooth and integral-fin (32 fpi) titanium tubes of 19.05 mm outer diameter. Experiments were carried out at saturation temperatures of 30, 35, 40 and 45 degrees C and wall subcoolings from 1 to 8 degrees C. The results show that the condensation coefficients on the smooth tubes are well predicted by the Nusselt theory with an average error of +0.66% and within a deviation between -6.6% and +8.3%. The enhancement factors provided by the integral-fin tubes range from 0.77 to 1.22. The low enhancement factors are due to the high condensate retention between fins, which brings about flooded fractions of the tube perimeter from 62.9% to 73.2%, and the low thermal conductivity of titanium. The Briggs and Rose [1994. Effect of fin efficiency on a model for condensation heat transfer on a horizontal, integral-fin tube. Int. J. Heat Mass Transfer 37,457-463.] model, which accounts for the conduction in the fins, predicts the experimental data with a mean overestimation of 20%. The analysis of the partial thermal resistances in the overall heat transfer process points out the convenience of enhancing the outside ammonia condensation when high water velocities are considered inside the tubes. (C) 2009 Elsevier Ltd and IIR. All rights reserved.
引用
收藏
页码:1140 / 1148
页数:9
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