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Hydrogen by thermocatalytic decomposition of methane.

机译:氢通过甲烷的热催化分解。

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The production of hydrogen by the thermocatalytic decomposition of methane was investigated. Iron-based catalyst was synthesized using a fixed-bed flow reactor under atmospheric pressure and at temperatures range from 800 to 900°C. Two reacting gases were used to prepare the catalyst and methane was chosen due to the shortest catalyst preparation time equals to 2 h at 900°C and elimination of the need for a separate source of hydrogen at the plant site. The material characterization of the iron-based catalyst was performed by SEM, TEM, BET, XRD and particle size analysis. The mechanism of methane decomposition for the catalysts was determined and kinetic parameters were estimated using topochemical model postulated by Avrami-Erofeyev. Over 98% conversion of methane was obtained after 5 h of work of prepared catalyst and neither catalyst deactivation nor blockage of the packing was observed for over 75 h.
机译:研究了通过甲烷的热催化分解生产氢气。使用固定床流动反应器在大气压下和在800至900°C的温度范围内合成铁基催化剂。使用两种反应气体来制备催化剂,并选择甲烷是因为最短的催化剂制备时间等于900℃下2小时,并且消除了工厂现场需要单独的氢气源。通过SEM,TEM,BET,XRD和粒度分析进行铁基催化剂的材料表征。确定了甲烷分解催化剂的机理,并使用Avrami-Erofeyev提出的拓扑化学模型估算了动力学参数。制备的催化剂工作5小时后,甲烷的转化率超过98%,超过75小时未观察到催化剂失活或填料堵塞。

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