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Hydrogen production system by methanol reforming with microreactor

机译:微反应器甲醇重整制氢系统

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摘要

The microreactor system with a hydrogen production unit by methanol reforming and a CO removal unit by selective oxidation for small PEMFC was developed. First, the preparation of Cu/ZnO/Al_2O_3 catalyst for methanol reforming was examined. By the appropriate selection of temperature and pH in precipitation formation and Al_2O_3 support, it was possible to obtain the Cu/ZnO/Al_2O_3 catalyst with superior catalytic activity than a commercial catalyst. It was indicated that the optimization of preparation condition brings about the catalyst with large Cu surface area and small ZnO crystallite. Further, by use of the microreactor, which fabricated a Si substrate, with the superior Cu/ZnO/Al_2O_3 catalyst deposited on a microchannel, the sufficient hydrogen production rate, which corresponds to an electric power enough to drive a portable telephone that consumes about 1 W, was obtained under the practical operating condition. Finally, the developed small PEMFC, which consists of the methanol reformer and the CO remover having a Pt/Al_2O_3 catalyst, generated a maximum output almost equal to pure H_2 gas.
机译:开发了一种小型反应器系统,该系统具有通过甲醇重整制氢装置和通过选择性氧化除去CO装置的小型PEMFC。首先,研究了用于甲醇重整的Cu / ZnO / Al_2O_3催化剂的制备。通过适当选择沉淀形成中的温度和pH以及Al_2O_3载体,可以获得具有比商业催化剂优异的催化活性的Cu / ZnO / Al_2O_3催化剂。结果表明,制备条件的优化使催化剂具有较大的Cu表面积和较小的ZnO晶粒。此外,通过使用制造硅衬底的微反应器,在微通道上沉积了优异的Cu / ZnO / Al_2O_3催化剂,足够的氢气产生速率,相当于足以驱动大约消耗1的便携式电话的电能。 W是在实际操作条件下获得的。最后,由甲醇重整器和具有Pt / Al_2O_3催化剂的CO去除器组成的小型PEMFC产生的最大产量几乎等于纯H_2气体。

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