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Direct methanol fuel cell: transport properties of polymer electrolyte membrane and cell performance

机译:直接甲醇燃料电池:聚合物电解质膜的运输性能和细胞性能

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Methanol and water absorption in 1100 and 1200 e.w. Nafion membranes was determined by weighing P{sub}2{sub}O5 dried and methanol solution equilibrated membranes. Both methanol and water absorption in the 1200 e.w. membrane is about 70-74 % of that in the 1100 e.w. membrane. The methanol cross-over rate corresponding to that in a direct methanol fuel cell (DMFC) at open circuit was measured using a voltammetric method in the DMFC configuration and under the same cell operating conditions (temperature, humidification and concentration of feed methanol solution). Accounting for the thickness difference between the membrane samples, the methanol cross-over rate through a 1200 e.w. membrane is 52 % of that through a 1100 e.w. membrane. To resolve the cathode and anode performances in an operating DMFC, a dynamic hydrogen electrode (DHE) was used as a reference electrode. Results show that in DMFC operation the cathode could be flooded due to the high water and methanol cross-over rates, especially through the 1100 e.w. membrane at a cell temperature below 80 °C. An increase in methanol cross-over rate as incurred by increasing the concentration of the feed methanol solution, increasing the cell operating temperature or using a membrane more permeable to methanol decreases the cathode potential of the DMFC at open circuit. As the cell current density is increased, the cathode potential of the DMFC can approach the cathode potential of a H{sub}2/air cell, thanks to the consumption of methanol at the anode and consequent decrease in methanol cross-over rate.
机译:1100和1200中的甲醇和吸水率。通过称重P {亚} 2 {Sub} O5干燥和甲醇溶液平衡膜测定Nafion膜。 1200英尺的甲醇和吸水性。膜在1100英尺中约为70-74%。膜。在DMFC构型中的伏安法和在相同的电池操作条件下(温度,甲醇溶液的温度,加湿和浓缩甲醇溶液的浓度),测量对应于在开路的直接甲醇燃料电池(DMFC)中的甲醇交叉速率。占膜样品之间的厚度差异,甲醇交叉速率通过1200英尺。膜的52%是通过1100英尺的52%。膜。为了在操作DMFC中解析阴极和阳极性能,使用动态氢电极(DHE)作为参比电极。结果表明,在DMFC操作中,阴极可能由于高水和甲醇交过速率而被淹没,尤其是通过1100。细胞温度低于80℃的膜。通过增加进料甲醇溶液的浓度,增加电池操作温度或使用更透过的甲醇的膜来增加甲醇交叉率,从而降低了DMFC在开路的阴极电位。由于电池电流密度增加,由于阳极处的甲醇的消耗,因此DMFC的阴极电位可以接近H {亚} 2 /空气电池的阴极电位,从而降低甲醇交叉率。

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