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Catalytic reactor, methane / steam reforming process, and methane processing plant to produce longer chain hydrocarbons

机译:催化反应器,甲烷/蒸汽重整工艺和甲烷加工厂生产更长链的碳氢化合物

摘要

"CATALYTIC REACTOR, PROCESS TO PERFORM METHAN / STEAM REFORM, AND PLAN FOR PROCESSING METHANE TO MAKE LONGER CHAIN HYDROCARBONS". A catalytic reactor (40) comprises a plurality of sheets (42) defining flow channels (44) between them. Within each flow channel (44) is a sheet (46) of corrugated material whose surfaces are coated with catalytic material away from where they contact the sheets (44). At each end of the reactor (40) are manifolds for feeding gas mixtures to the flow channels (44), the manifolds communicating with adjacent channels being separated. Reactor (40) allows different gas mixtures to be fed to adjacent channels (44), which may be at different pressures, with corresponding chemical reactions also being different. When one of the reactions is endothermic, while the other reaction is exothermic, heat is transferred through the leaves (42) separating adjacent channels (44) from the exothermic reaction to the endothermic reaction. The reactor (40) can be used in a compact plant to perform steam / methane reforming, obtaining the necessary heat from catalytic methane combustion, and also for Fischer-Tropsch synthesis, so that the overall process involves methane conversion. in long chain hydrocarbons.
机译:“催化反应器,进行甲烷/蒸汽重整的过程,以及用于处理甲烷以制造更长链烃的计划”。催化反应器(40)包括在它们之间限定流动通道(44)的多个板(42)。在每个流动通道(44)内是波纹材料片(46),其表面在远离它们接触片(44)的位置上涂覆有催化材料。在反应器(40)的每一端是用于将气体混合物进料到流动通道(44)的歧管,与相邻通道连通的歧管是分开的。反应器(40)允许将不同的气体混合物进料至可能处于不同压力的相邻通道(44),相应的化学反应也不同。当一个反应是吸热反应,而另一个反应是放热反应时,热量通过叶片(42)传递,将相邻的通道(44)从放热反应转移到吸热反应。该反应器(40)可用于紧凑型工厂中以进行蒸汽/甲烷重整,从催化甲烷燃烧中获得必要的热量,并且还用于费-托合成,因此整个过程涉及甲烷转化。在长链烃中。

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