Two-phase heat transfer of R410A in annuli outside enhanced tubes with micro-fin and dimple

被引:18
|
作者
Li, Wei [1 ,2 ]
Wang, Jiacheng [1 ]
Guo, Yu [1 ]
Gu, Zongbao [1 ]
Wang, Xiaobo [1 ]
Sun, Zhichuan [3 ,4 ]
Tang, Weiyu [2 ]
Kukulka, David J. [5 ]
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] AVIC Nanjing Engn Inst Aircraft Syst, Nanjing 211106, Peoples R China
[4] Aviat Key Lab Sci & Technol Aero Electromech Syst, Nanjing 211106, Peoples R China
[5] Estate Univ New York Coll Buffalo, 1300 Elmwood Ave, Buffalo, NY 14222 USA
基金
美国国家科学基金会;
关键词
T-phase flow; Annuli; R410A; Composite surface; Heat transfer characteristics; PRESSURE-DROP CHARACTERISTICS; TRANSFER COEFFICIENTS; GENERAL CORRELATION; FILM CONDENSATION; HORIZONTAL TUBES; FLOW; PREDICTION; REFRIGERANTS; EVAPORATION; SURFACE;
D O I
10.1016/j.ijheatmasstransfer.2021.121370
中图分类号
O414.1 [热力学];
学科分类号
摘要
An experimental study evaluating the two-phase heat transfer using refrigerant R410A in the annuli outside the smooth tube and the enhanced tubes was investigated. Four tubes made of stainless steel including the smooth tube(ST), herringbone tube(HB), dimple tube(DIM), and dimple/herringbone tube(DIM/HB) were studied; with varying surface modification; with an inner diameter of 11.5 mm and an outer diameter of 12.7 mm; with a test length of 2 m. The condensation/evaporation experiments were performed at a saturated temperature of 45/6 degrees C; for the inlet and outlet vapor quality fixed at 0.8/0.2 and 0.2/0.8; with mass fluxes range from 75 to 225 kg m(-2) s(-1). The results indicated that: herringbone structure is more effective in condensation, especially at low flow rates, and the dimple structure is more effective in evaporation. The composite surface of the herringbone and dimple exhibited a substantial enhancement of thermal-hydraulic performance in two-phase flow. DIM/HB tube shows the highest performance factor in two-phase heat transfer. Besides, a new improved Nusselt equation for condensation outside the smooth tube is proposed with a prediction error within 5 %. Correlations for predicting the heat transfer coefficient of evaporation outside the smooth tube were also compared and analyzed. (C) 2021 Elsevier Ltd. All rights reserved.
引用
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页数:11
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