Experimental Analysis of a Small-Scale Flowing Electrolyte-Direct Methanol Fuel Cell Stack

被引:5
|
作者
Kablou, Yashar [1 ]
Cruickshank, Cynthia A. [1 ]
Matida, Edgar [1 ]
机构
[1] Carleton Univ, Dept Mech & Aerosp Engn, Ottawa, ON K1S 5B6, Canada
来源
基金
加拿大自然科学与工程研究理事会;
关键词
PERFORMANCE; MEMBRANES;
D O I
10.1115/1.4031423
中图分类号
O646 [电化学、电解、磁化学];
学科分类号
081704 ;
摘要
A small-scale five-cell flowing electrolyte-direct methanol fuel cell (FE-DMFC) stack with U-type manifold configuration and parallel serpentine flow bed design was studied experimentally. The active area of a single cell was approximately 25 cm(2). For every stack cell, diluted sulphuric acid was used as the flowing electrolyte (FE) which was circulated through a porous medium placed between two Nafion (R) 115 polymer electrolyte membranes. The stack performance was studied over a range of several operating conditions, such as temperature (50-80 degrees C), FE flow rate (0-17.5 ml/min), methanol concentration (0.5-4.0 M), and methanol solution flow rate (10-20 ml/min). In addition, the stack cell to cell voltage variations and the effects of the FE stream interruption on the output voltage were investigated at various operating loads. Experimental results showed that utilization of the FE effectively reduced methanol crossover and improved the stack power output. It was found that increasing the FE flow rate enhanced the stack capability to operate at higher inlet methanol concentrations without any degradation to the performance. The results also demonstrated that the stack power output can be directly controlled by regulating the FE stream especially at high operating currents.
引用
收藏
页数:7
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