Confined jet array impingement boiling of subcooled aqueous ethylene glycol solution

被引:31
作者
Hong, F. J. [1 ]
Zhang, C. Y. [1 ]
He, W. [1 ]
Cheng, P. [1 ]
Chen, G. [2 ]
机构
[1] Shanghai Jiao Tong Univ, Sch Mech Engn, Shanghai 200240, Peoples R China
[2] Shanghai Inst Satellite Engn, Shanghai 200240, Peoples R China
基金
中国国家自然科学基金;
关键词
Aqueous ethylene glycol solution; Confined; Jet impingement; Boiling; Critical heat flux; HEAT-TRANSFER; MIXTURES;
D O I
10.1016/j.icheatmasstransfer.2014.06.013
中图分类号
O414.1 [热力学];
学科分类号
摘要
A closed-loop experimental setup was built to study the confined jet array impingement boiling of 43% mass concentration aqueous ethylene glycol solution at low jet velocities and large degree of subcoolings. A 20 mm x 40 mm rectangular thin metal film with thickness of 0.03 mm was used as the heating surface. The in-line jet array had an orifice diameter d = 1 mm, a dimensionless jet-to-jet spacing S/d = 5 or 4, and a dimensionless jet-to-target spacing H/d = 1, 15 or 3. Experiments were performed at atmospheric pressure with the saturation temperature of 106 degrees C, jet velocities of 02 m/s, 031 m/s and 0.5 m/s, and liquid subcoolings of 36 degrees C, 46 degrees C and 56 degrees C. It is found that the heat transfer coefficient in the nucleate boiling regime at first increases with the increase of heat flux and then starts to decrease before the critical heat flux (CHF). Jet velocity and jet-to-target spacing have little effects on heat transfer coefficient in the nucleate boiling dominant regime, while subcooling and jet-to-jet spacing play important roles. Not only the jet velocity but also the liquid subcooling has great influences on the boiling inception and CHF. There exists an optimal jet-to-target spacing to achieve the maximum CHF because of the tradeoff between the breakup and confinement (or expel) of vapor bubbles. For the same flow rate, S/d = 5 has a higher heat transfer coefficient and CHF than S/d = 4. (C) 2014 Elsevier Ltd. All rights reserved.
引用
收藏
页码:165 / 173
页数:9
相关论文
共 16 条
[1]   State of the art of high heat flux cooling technologies [J].
Agostini, Bruno ;
Fabbri, Matteo ;
Park, Jung E. ;
Wojtan, Leszek ;
Thome, John R. ;
Michel, Bruno .
HEAT TRANSFER ENGINEERING, 2007, 28 (04) :258-281
[2]  
Cardenas R., 2012, J HEAT TRANSF T ASME, V134
[3]   Heat transfer characteristics of submerged jet impingement boiling of saturated FC-72 [J].
Cardenas, Ruander ;
Narayanan, Vinod .
INTERNATIONAL JOURNAL OF HEAT AND MASS TRANSFER, 2012, 55 (15-16) :4217-4231
[4]   Evaluation of jet impingement, spray and microchannel chip cooling options for high heat flux removal [J].
Kandlikar, Satish G. ;
Bapat, Akhilesh V. .
HEAT TRANSFER ENGINEERING, 2007, 28 (11) :911-923
[5]   An experimental investigation on flow boiling of ethylene-glycol/water mixtures [J].
Kandlikar, SG ;
Bulut, M .
JOURNAL OF HEAT TRANSFER-TRANSACTIONS OF THE ASME, 2003, 125 (02) :317-325
[6]   Boiling heat transfer with binary mixtures: Part II - Flow boiling in plain tubes [J].
Kandlikar, SG .
JOURNAL OF HEAT TRANSFER-TRANSACTIONS OF THE ASME, 1998, 120 (02) :388-394
[7]   JET IMPINGEMENT NUCLEATE BOILING [J].
MA, CF ;
BERGLES, AE .
INTERNATIONAL JOURNAL OF HEAT AND MASS TRANSFER, 1986, 29 (08) :1095-1101
[8]   Single-phase and two-phase cooling with an array of rectangular jets [J].
Meyer, MT ;
Mudawar, I ;
Boyack, CE ;
Hale, CA .
INTERNATIONAL JOURNAL OF HEAT AND MASS TRANSFER, 2006, 49 (1-2) :17-29
[9]   BURNOUT IN A HIGH HEAT-FLUX BOILING SYSTEM WITH AN IMPINGING JET [J].
MONDE, M ;
KATTO, Y .
INTERNATIONAL JOURNAL OF HEAT AND MASS TRANSFER, 1978, 21 (03) :295-305
[10]   An experimental investigation of free and submerged miniature liquid jet array impingement heat transfer [J].
Robinson, A. J. ;
Schnitzler, E. .
EXPERIMENTAL THERMAL AND FLUID SCIENCE, 2007, 32 (01) :1-13