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Dehydrogenation Catalyst for Organic Chemical Hydrides and ApplicationScheme to the Various Hydrogen Sources

机译:有机化学氢化物的脱氢催化剂及其在各种氢源中的应用方案

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Utilization of organic chemical hydride method for the hydrogen storage and transportationby using hydrogenation and dehydrogenation of aromatic compound has been investigatedfrom 1980's. This method has both of high gravimetric and volumetric hydrogen density, andit has little potential risk due to storage and transportation under ambient pressure. It has alsoan advantage that the hydrogen storage and transportation is carried out as a conventionalpetrochemical product. However, this method has not been established technically becausedehydrogenation catalyst does not have the enough stability and the sufficient performance.Chiyoda Corporation has been developed the proprietary dehydrogenation catalyst working inthe simple fixed bed reactor with the high stability and the sufficient performance. Thiscatalyst can generate hydrogen with methylcyclohexane (MCH) conversion: >95%, Tolueneselectivity: >99.9%, hydrogen generation rate: >1000 Ncc/h/cc-cat under the reasonablecondition of 593K (320 ℃), ambient pressure, LHSV:2.0h -1 and co-feed hydrogen:5 ~20mol% in feed. The estimated production cost at hydrogen station for FCV is around64.7¥/Nm 3 -H2 (59 ¢/Nm 3 -H2). The application scheme of the method is also investigated toutilize various hydrogen sources including the refinery, iron manufacture plant andpetrochemical plant, which produce hydrogen as by-product containing high impurity.
机译:从1980年代开始研究利用有机化学氢化物法通过芳香族化合物的加氢和脱氢来储氢和运输氢。该方法具有高的重量氢密度和体积氢密度,并且由于在环境压力下的存储和运输而具有很小的潜在风险。还有一个优点是,氢气的存储和运输是作为常规的石油化学产品进行的。但是,由于脱氢催化剂不具有足够的稳定性和足够的性能,因此该方法在技术上还没有建立。千代田公司开发了在简单的固定床反应器中具有高稳定性和足够的性能的专有脱氢催化剂。该催化剂在593K(320℃),环境压力,LHSV:2.0的合理条件下,可以通过甲基环己烷(MCH)转化率> 95%,甲苯选择性> 99.9%,产氢率> 1000 Ncc / h / cc-cat生成氢气。 h -1与氢共同进料:进料中氢5%〜20mol%。 FCV氢站的估计生产成本约为64.7元/ Nm 3 -H2(59 ¢ / Nm 3 -H2)。还研究了该方法的应用方案,以利用包括精炼厂,炼铁厂和石化厂在内的各种氢源,这些氢源产生的氢为副产物,杂质含量高。

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