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Hydrogen by Steam Reforming of Ethanol over Co-Mg Incorporated Novel Mesoporous Alumina Catalysts in Tubular and Microwave Reactors

机译:钴和镁结合新型介孔氧化铝催化剂在管状和微波反应器中通过乙醇蒸汽重整制氢

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Bio-ethanol is an excellent hydrogen carrier with a good potential to be used as a resource for on-board hydrogen production. In this work, a set of new Co incorporated mesoporous alumina (MA) catalysts modified with Mg were synthesized and the effects of synthesis procedure on their catalytic performances were investigated in steam reforming of ethanol. Activity tests of the synthesized catalysts were performed in a reactor with conductive heating and also in a focused-microwave system, in which better energy utilization and temperature uniformity were achieved. Product distributions obtained with Co incorporated Mg promoted mesoporous alumina catalysts synthesized by following impregnation and one-pot routes (Co@Mg-MA and Co-Mg-MA, respectively) gave very high and stable hydrogen yields, over 5.2 moles per mole of ethanol reacted. However, in the case of Co based catalyst synthesized using unmodified mesoporous alumina, hydrogen yield value was quite low and the main product was ethylene.
机译:生物乙醇是一种极好的氢载体,具有良好的潜力,可以用作船上制氢的资源。在这项工作中,合成了一组新型的掺有Mg的掺Co介孔氧化铝(MA)催化剂,并研究了合成工艺对其在乙醇蒸汽重整中的催化性能的影响。在具有传导加热的反应器中以及在聚焦微波系统中进行了合成催化剂的活性测试,其中获得了更好的能量利用率和温度均匀性。通过以下浸渍和一锅法(分别为Co @ Mg-MA和Co-Mg-MA)合成的,掺有Co的Mg促进的介孔氧化铝催化剂获得的产品分布产生了非常高且稳定的氢产率,每摩尔乙醇超过5.2摩尔。反应了。然而,在使用未改性的中孔氧化铝合成的Co基催化剂的情况下,氢产率值非常低,并且主要产物是乙烯。

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