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PEM fuel cells stack protection from CO-poisoning in a m-CHP system with membrane reformer

机译:具有膜重整器的m-CHP系统中的PEM燃料电池可防止CO中毒

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An innovative m-CHP system based on membrane reformer and PEM fuel cells is developed within the FluidCELL project. Hydrogen production and purification is carried out in one single reactor. Hydrogen produced by bio-ethanol auto-thermal reforming permeates across the Pd-based membranes and is obtained as a pure stream to feed the LT-PEM fuel cells stack. The system, rated at 5 kW_(el), is designed to obtain high net electric efficiency (>40%) with a limited Pd-membranes area (<0.4 m~2). In case of low selectivity or leakage of membranes, polluted hydrogen may enter the fuel cells stack. In order to prevent CO-poisoning different solutions are discussed here: (i) methanation reactor, (ii) preferential oxidation reactor (Prox) and (iii) external air bleeding. To define the best mitigation strategy many aspects must be taken into account as electric efficiency, vented gases by purge, additional components and control systems, fuel cells degradation over the time. In this particular, the main focus is on PEM behavior.
机译:在FluidCELL项目中开发了一种基于膜重整器和PEM燃料电池的创新型m-CHP系统。氢气的生产和提纯是在一个反应​​器中进行的。由生物乙醇自热重整产生的氢气会渗透到Pd基膜上,并以纯净流的形式获得,以供入LT-PEM燃料电池堆。该系统的额定功率为5 kW_(el),旨在在有限的Pd膜面积(<0.4 m〜2)内获得高净电效率(> 40%)。在选择性低或膜泄漏的情况下,污染的氢气可能会进入燃料电池堆。为了防止CO中毒,此处讨论了不同的解决方案:(i)甲烷化反应器,(ii)优先氧化反应器(Prox)和(iii)外部空气泄漏。为了定义最佳的缓解策略,必须考虑许多方面,例如电效率,通过吹扫排出的气体,附加组件和控制系统,燃料电池随时间而退化。特别是,主要重点是PEM行为。

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