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首页> 外文期刊>Topics in Catalysis >Autothermal Reforming of Methane with Integrated CO2 Capture in a Novel Fluidized Bed Membrane Reactor.Part 1:Experimental Demonstration
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Autothermal Reforming of Methane with Integrated CO2 Capture in a Novel Fluidized Bed Membrane Reactor.Part 1:Experimental Demonstration

机译:新型流化床膜反应器中集成CO2捕集的甲烷自热重整。第1部分:实验论证

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摘要

Two fluidized bed membrane reactor concepts for hydrogen production via autothermal reforming of methane with integrated CO2 capture are proposed.Ultra-pure hydrogen is obtained via hydrogen perm-selective Pd-based membranes,while the required reaction energy is supplied by oxidizing part of the CH4 in situ in the methane combustion configuration or by combusting part of the permeated H2 in the hydrogen combustion configuration(oxidative sweeping).In this first part,the technical feasibility of the two concepts has been studied experimentally,investigating the reactor performance(CH4 conversion,CO selectivity,H2 production and H2 yield)at different operating conditions.A more detailed comparison of the performance of the two proposed reactor concepts is carried out with a simulation study and is presented in the second part of this work.
机译:提出了两种流化床膜反应器概念,用于通过甲烷的自热重整和集成的CO2捕集生产氢气。通过氢选择性渗透的Pd基膜获得超纯氢,而所需的反应能量则通过氧化CH4的一部分来提供在甲烷燃烧构型中原位反应或在氢气燃烧构型中通过燃烧一部分渗透的H2(氧化吹扫)。在第一部分中,通过实验研究了这两个概念的技术可行性,研究了反应堆的性能(CH4转化率,在不同的操作条件下,CO选择性,H2生成量和H2收率)。通过模拟研究对这两种拟议的反应器概念的性能进行了更详细的比较,并将在第二部分中进行介绍。

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