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Synthesis Gas Production by Partial Oxidation of Methane and Dry Reforming of Methane in the Presence of Novel Ni-Co/MFI Catalysts

机译:通过在新型Ni-Co / MFI催化剂存在下,通过部分氧化甲烷的甲烷和干重改性的合成气产量

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Catalysts based on Ni, Co, and NiCo supported on MFI zeolites for the partial oxidation of methane and dry reforming of methane to synthesis gas have been synthesized and studied. The total metal content in the catalysts is 2 wt %. A commercial zeolite with a binder (alumina) and a binder-free zeolite synthesized by an accelerated microwave-assisted hydrothermal method are used as supports. The synthesis gas yield is 97% in the presence of Ni and NiCo catalysts supported on the MFI zeolite synthesized by the microwaveassisted hydrothermal method. The simultaneous presence of Ni and Co in the catalyst makes the sample resistant to coking during dry reforming of methane, whereas the Ni catalyst is characterized by the formation of a significant amount of carbon fibers.
机译:基于Ni,Co和Nico的催化剂支持在MFI沸石上用于部分氧化甲烷和干燥重整甲烷与合成气体的合成气体。 催化剂中的总金属含量为2wt%。 用粘合剂(氧化铝)的商业沸石和通过加速微波辅助水热法合成的无粘合剂沸石用作载体。 在通过微针率吸氢方法合成的MFI沸石上负载的Ni和Nico催化剂存在下,合成气产率为97%。 催化剂中Ni和Co的同时存在使得在甲烷的干燥重整过程中对焦化的样品进行抗焦化,而Ni催化剂的特征在于形成大量碳纤维。

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