R410A flow condensation inside two dimensional micro-fin tubes and three dimensional dimple tubes

被引:23
作者
Li, Wei [1 ,2 ]
Wang, Jiacheng [1 ]
Guo, Yu [1 ]
Shi, Qiyun [1 ]
He, Yan [1 ]
Kukulka, David J. [3 ]
Luo, Xing [4 ]
Kabelac, Stephan [4 ]
机构
[1] Qingdao Univ Sci & Technol, Dept Mech & Elect Engn, 99 Songling Rd, Qingdao 266061, Peoples R China
[2] Zhejiang Univ, Dept Energy Engn, 38 Zheda Rd, Hangzhou 310027, Peoples R China
[3] State Univ New York Coll Buffalo, 1300 Elmwood Ave, Buffalo, NY 14222 USA
[4] Leibniz Univ Hannover, Inst Thermodynam, Univ 1, D-30823 Hannover, Germany
基金
美国国家科学基金会;
关键词
Tube side condensation; Heat transfer coefficient; R410A; Helix micro fin tube; Dimple tube; HEAT-TRANSFER CHARACTERISTICS; HORIZONTAL SMOOTH; THERMAL-CONDUCTIVITY; 5; MM; R134A; REFRIGERANT; MODEL;
D O I
10.1016/j.ijheatmasstransfer.2021.121910
中图分类号
O414.1 [热力学];
学科分类号
摘要
Condensation heat transfer characteristics were experimentally investigated inside two dimensional helix micro fin (HX) tubes, three-dimensional dimple (1EHT) tubes and smooth (ST) tubes; while using R410A, for a variety of operating conditions and tube parameters. Tubes evaluated had a length of 2 m, with outer diameters of 9.52 and 12.7 mm; tube materials included copper and stainless steel. Experimental procedure was verified using a single-phase heat balance; with a comparison of results (enhanced tubes to smooth tube) being performed. The condensation experiments were performed at a saturated temperature of 35-45 degrees C; for the vapor quality range from 0.1 to 0.9; with mass fluxes that ranged from 70 to 450 kg m(-2) s(-1). Additionally, the effect of various parameters (mass flux, mean vapor quality, saturation temperature, tube thermal conductivity, tube diameter, and surface structure) on the tube side condensation heat transfer was evaluated. For the test conditions considered here the HTC enhancement ratio is in the range from 1.15 to 2.05 for the 1EHT tube and for the HX tube it ranged from 1.18 to 1.69; while the performance factor (PF takes into account the pressure drop) is 1.02-1.57 (1EHT) and 1.23-1.78 (HX). Heat transfer performance of the smooth tube was determined to be slightly affected by the thermal conductivity of the tube; however, for enhanced tubes there is a more dramatic increase in the HTC for an increase of thermal conductivity. Additionally, better heat transfer performance is demonstrated for smaller diameter tubes. Finally, the enhancement effect of the experimental parameters on the enhanced tubes was quantified through the use of a newly introduced evaluation factor. (c) 2021 Elsevier Ltd. All rights reserved.
引用
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页数:14
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