New design of a cathode flow-field with a sub-channel to improve the polymer electrolyte membrane fuel cell performance

被引:61
|
作者
Wang, Yulin [1 ,2 ]
Yue, Like [1 ,2 ]
Wang, Shixue [1 ,2 ]
机构
[1] Tianjin Univ, Sch Mech Engn, 92 Weijin Rd, Tianjin, Peoples R China
[2] Tianjin Univ, Key Lab Efficient Utilizat Low & Medium Grade Ene, MOE, Tianjin, Peoples R China
关键词
PEM fuel cell; Water management; Cathode flow-field design; Sub-channel; GAS-DIFFUSION LAYER; PARALLEL; MICROGROOVES; ENHANCEMENT; SERPENTINE; REMOVAL;
D O I
10.1016/j.jpowsour.2017.01.075
中图分类号
O64 [物理化学(理论化学)、化学物理学];
学科分类号
070304 ; 081704 ;
摘要
The cathode flow-field design of polymer electrolyte membrane (PEM) fuel cells determines the distribution of reactant gases and the removal of liquid water. A suitable design can result in perfect water management and thus high cell performance. In this paper, a new design for a cathode flow-field with a sub-channel was proposed and had been experimentally analyzed in a parallel flow-field PEM fuel cell. Three sub-channel inlets were placed along the cathode channel. The main-channel inlet was fed with moist air to humidify the membrane and maintain high proton conductivity, whereas, the sub-channel inlet was fed with dry air to enhance water removal in the flow channel. The experimental results indicated that the sub-channel design can decrease the pressure drop in the flow channel, and the sub channels inlet positions (SIP, where the sub-channel inlets were placed along the cathode channel) and flow rates (SFR, percentage of air from the sub-channel inlet in the total cathode flow rate) had a considerable impact on water removal and cell performance. A proposed design that combines the SIP and SFR can effectively eliminate water from the fuel cell, increasing the maximum power density by more than 13.2% compared to the conventional design. (C) 2017 Elsevier B.V. All rights reserved.
引用
收藏
页码:32 / 38
页数:7
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