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首页> 外文期刊>International journal of hydrogen energy >Development of dehydrogenation catalyst for hydrogen generation in organic chemical hydride method
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Development of dehydrogenation catalyst for hydrogen generation in organic chemical hydride method

机译:有机化学氢化物法制氢脱氢催化剂的研制

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摘要

The utilization of the organic chemical hydride method (OCH method) for hydrogen storage and transportation using hydro-genation and dehydrogenation chemical reactions with aromatic compounds has been investigated since the 1980s. This method provides for both high gravimetric and volumetric hydrogen densities, and the potential risk is very small due to the storage and transportation in the liquid state under ambient pressure. It also has the advantage that hydrogen storage and transportation is carried out as a conventional petrochemical product. However, this method has not been technically established because the dehydrogenation catalyst does not have a sufficient stability and performance. We have developed a dehydrogenation catalyst using a simple fixed-bed reactor that has a high stability and sufficient performance. This catalyst can generate hydrogen from methyl-cyclohexane (MCH: 99.9%) with a conversion > 95%, toluene selectivity > 99.9%, hydrogen generation rate > 1000 Nm~3/h/m~3 cat under the reasonable conditions of 593 K, ambient pressure, LHSV:2.0/h and co-feed hydrogen 5-20 mol% in the feed. The estimated production cost at a hydrogen station for fuel cell vehicle (FCV) is around 64.7¥/Nm~3 H_2(59¢/Nm~3 H_2). Two possible applications of this method are introduced. One is the utilization of low-grade hydrogen including impurities. The other is a future vision of the global hydrogen energy chain.
机译:自1980年代以来,已经研究了利用有机化学氢化物法(OCH法)通过与芳香族化合物的氢化和脱氢化学反应进行氢存储和运输。该方法提供了高的重量氢密度和体积氢密度,并且由于在环境压力下以液态储存和运输,潜在风险非常小。它还具有作为常规石油化学产品进行氢存储和运输的优点。然而,由于脱氢催化剂不具有足够的稳定性和性能,因此该方法在技术上尚未建立。我们已经开发了使用具有高稳定性和足够性能的简单固定床反应器的脱氢催化剂。该催化剂在593 K的合理条件下,可从甲基环己烷(MCH:99.9%)生成氢,转化率> 95%,甲苯选择性> 99.9%,产氢率> 1000 Nm〜3 / h / m〜3 cat ,环境压力,LHSV:2.0 / h和进料中氢气的进料为5-20 mol%。燃料电池汽车加氢站的估计生产成本约为64.7元/ Nm〜3 H_2(59 ¢ / Nm〜3 H_2)。介绍了该方法的两个可能的应用。一种是利用包括杂质的低级氢。另一个是全球氢能源链的未来愿景。

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