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Coupling Experiment of Compact Integrated Fuel Processors with 75 kW PEM Fuel Cells

机译:具有75 kW PEM燃料电池的紧凑型燃料加压器的耦合试验

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A compact autothermal reformer suitable for liquid fuel for instance methanol et al. was developed. The fuel reformer was combined with polymer electrolyte membrane fuel cells (PEM FC) and a system test of the process chain was successfully performed. The fuel processor consists of a fuel evaporating step, two-stage reformer and a two-stage reactor of water gas shift (WGS, one for high temperature water gas shift and the other for low temperature water gas shifter) and a four-stage preferential oxidation (PROX) reactor and some internal heat exchanger in order to achieve optimized heat integration. The fuel processor is designed to provide enough hydrogen for 75 kWel fuel cells. After the initial step of methanol ATR, CO WGS and CO PROX steps are used for 'clean-up' CO. The exhaust gas from FC anode feedback to the fuel processor to vaporizes the feedstock of methanol and water by a catalytic combusting-evaporator. The hydrogen source system can produce hydrogen 70.5 m~3/hr and its specific gravity power and specific volume power reach 255 W/kg and 450 W/L respectively. During three hours' coupling experiment, the fuel processing system and the fuel cells all has been running smoothly. The volume concentration of H_2 and CO in product gas (dry basis) was kept in 53% and 20 ppm respectively, completely meeting the requirements of PEM fuel cells. The conversion efficiency of the hydrogen producing system based on LHV of fuel and hydrogen can exceed 95.85%. The fuel cells stacks put up strong resistance to CO and its maximum electronic load to the fuel cells reaches 75.5 kW. It indicates that it is feasible technically for supplying hydrogen for Proton Exchange Membrane Fuel Cells by catalytic reforming of hydrogen-rich liquid fuel on-board or on-site.
机译:适用于液体燃料的紧凑型自热重整器,例如甲醇等。已开发。燃料重整器与聚合物电解质膜燃料电池(PEM FC)组合,并成功进行了工艺链的系统试验。燃料处理器由燃料蒸发步骤,两级重整器和水煤气变换的两级反应器(WGS,用于高温水气体转移,另一个用于低温水气体换热器)和四级优先级氧化(Prox)反应器和一些内部热交换器,以实现优化的热集成。燃料处理器旨在为75 kwel燃料电池提供足够的氢。在甲醇ATR的初始步骤之后,CO WGS和CO PROX步骤用于“清理”CO。从FC阳极反馈到燃料处理器的废气通过催化燃烧蒸发器蒸发甲醇和水的原料。氢气源系统可以分别产生70.5M〜3 / HR及其比重分别达到255W / kg和450 w / l的特定重力功率和特定的重力功率。在三个小时的耦合实验中,燃料加工系统和燃料电池都已经平稳地运行。产品气体(干基)的H_2和CO的体积浓度分别保持在53%和20ppm,完全满足PEM燃料电池的要求。基于LHV的燃料和氢气的氢气生产系统的转化效率超过95.85%。燃料电池堆叠对燃料电池达到75.5千瓦的强抵抗力,其最大电子负荷达到45.5千瓦。它表明,通过催化重整氢气燃料的载燃料或现场,可以在技术上提供用于质子交换膜燃料电池的氢气。

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