Experimental study of the thermal performance of chaotic geometries for their use in PEM fuel cells

被引:31
作者
Castelain, Cathy [1 ]
Lasbet, Yahia [1 ]
Auvity, Bruno [1 ]
Peerhossaini, Hassan [2 ]
机构
[1] Univ Nantes, Polytech Nantes, Lab Thermocinet Nantes, CNRS,UMR 6607, BP 50609, F-44306 Nantes 3, France
[2] Univ Paris Diderot, Sorbonne Paris Cite, Lab Interdisciplinaire Energies Demain, CNRS,UMR 8236, Paris, France
关键词
PEM fuel cell; Chaotic advection; Bipolar plate; Cooling; HEAT-TRANSFER; MICROCHANNEL NETS; BIPOLAR PLATES; PRESSURE-DROP; ADVECTION; PIPE; EXCHANGER; FLOW; MANAGEMENT; DESIGNS;
D O I
10.1016/j.ijthermalsci.2015.10.033
中图分类号
O414.1 [热力学];
学科分类号
摘要
In order to improve the thermal performance of heat exchangers used in the bipolar plates of PEM fuel cells, we suggest replacing the networks of straight channels by geometries generating chaotic flows. In transport applications, high heat densities are generated because of the combined high heat fluxes and the imposed compactness of heat exchangers. Moreover, the convective regime in the cooling channels is laminar and the channel network has to be as thin as possible to limit the electrical resistance through the bipolar plates. In such extreme conditions, the generation of spatial chaos by geometrical perturbation in the heat exchanger is a relevant way to intensify heat transfer. In this paper, an experimental study is presented for two chaotic advection geometries and a straight tube. A specialized test bench was designed and built. The channels were placed in a counterflow heat exchanger with a laminar flow in the center and a turbulent flow in the annulus. Heat exchange was carefully analyzed to obtain the convective heat transfer coefficient for each channel. (C) 2015 Elsevier Masson SAS. All rights reserved.
引用
收藏
页码:181 / 192
页数:12
相关论文
共 38 条
[1]   HEAT-TRANSFER ENHANCEMENT IN COILED TUBES BY CHAOTIC MIXING [J].
ACHARYA, N ;
SEN, M ;
CHANG, HC .
INTERNATIONAL JOURNAL OF HEAT AND MASS TRANSFER, 1992, 35 (10) :2475-2489
[2]   Evaluation of heat transfer and exergy loss in a concentric double pipe exchanger equipped with helical wires [J].
Akpinar, Ebru Kavak .
ENERGY CONVERSION AND MANAGEMENT, 2006, 47 (18-19) :3473-3486
[3]  
[Anonymous], 2001, FABR FLOW EXP MECANI
[4]   STIRRING BY CHAOTIC ADVECTION [J].
AREF, H .
JOURNAL OF FLUID MECHANICS, 1984, 143 (JUN) :1-21
[5]   Design of thermal management subsystem for a 5 kW polymer electrolyte membrane fuel cell system [J].
Asghari, Saeed ;
Akhgar, Hooman ;
Imani, Bagher Faghih .
JOURNAL OF POWER SOURCES, 2011, 196 (06) :3141-3148
[6]   Identification of the heat transfer coefficient over the external area of a finned tubes heat exchanger with respect to the moisture content of the air without condensation. [J].
Benelmir, R ;
Khalfi, M ;
Feidt, M .
REVUE GENERALE DE THERMIQUE, 1997, 36 (04) :289-301
[7]  
Borel L., 2005, THERMODYNAMIQUE ENER
[8]   Experimental study of chaotic advection regime in a twisted duct flow [J].
Castelain, C ;
Mokrani, A ;
Le Guer, Y ;
Peerhossaini, H .
EUROPEAN JOURNAL OF MECHANICS B-FLUIDS, 2001, 20 (02) :205-232
[9]   Heat transfer and pressure drop in fractal tree-like microchannel nets [J].
Chen, YP ;
Cheng, P .
INTERNATIONAL JOURNAL OF HEAT AND MASS TRANSFER, 2002, 45 (13) :2643-2648
[10]  
CHOW CY, 1998, Patent No. 5804326