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Electrochemical reaction engineering of polymer electrolyte fuel cell

机译:高分子电解质燃料电池的电化学反应工程

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摘要

Although fuel cells can be considered as a type of reactor, methods of kinetic analysis and reactor modeling from the viewpoint of chemical reaction engineering have not yet been established. The rate of an electrochemical reaction is a function of concentration, temperature, and interfacial potential difference (or electromotive force). This study examined the cathode reaction in a polymer electrolyte fuel cell, in which oxygen and protons react over platinum in the catalyst layer (CL). The effects of the oxygen partial pressure and the cathode electromotive force on the reaction rate were assessed. Resistance to proton transport increases the electromotive force and reducing the reaction rate. It was established that the effectiveness factor of the cathode CL is determined by competition between the reaction and mass transport of oxygen and protons. Two dimensionless moduli that govern the cathode behavior are proposed as a means of depicting the processes in the cell.
机译:尽管可以将燃料电池视为反应堆的一种,但是从化学反应工程学的观点来看,动力学分析和反应堆建模的方法尚未建立。电化学反应的速率是浓度,温度和界面电势差(或电动势)的函数。这项研究检查了聚合物电解质燃料电池中的阴极反应,其中氧气和质子在催化剂层(CL)中的铂上反应。评估了氧分压和阴极电动势对反应速率的影响。质子传输的阻力增加了电动势并降低了反应速率。已经确定,阴极CL的效率因子是由反应与氧气和质子的质量传输之间的竞争决定的。提出了两种控制阴极行为的无量纲模量,作为描绘电池中过程的一种手段。

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