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CO_2 reforming of methane combined with steam reforming or partial oxidation of methane to syngas over NdCoO_3 perovskite-type mixed metal-oxide catalyst

机译:NdCoO_3钙钛矿型混合金属氧化物催化剂上甲烷的CO_2重整结合蒸汽重整或甲烷部分氧化为合成气

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摘要

CO_2 reforming with simultaneous steam reforming or partial oxidation of methane to syngas over NdCoO_3 perovskite-type mixed metal oxide catalyst (prereduced by H_2) at different process conditions has been investigated. In the simultaneous CO_2 and steam reforming, the conversion of methane and H_2O and also the H_2/CO product ratio are strongly influenced by the CO_2/H_2O feed-ratio. In the simultaneous CO_2 reforming and partial oxidation of methane, the conversion of methane and CO_2, H_2 selectivity and the net heat of reaction are strongly influenced by the process parameters (viz. temperature, space velocity and relative concentration of O_2 in the feed). In both cases, no carbon deposition on the catalyst was observed. The reduced NdCoO_3 perovskite-type mixed-oxide catalyst (Co dispersed on Nd_2O_3) is a highly promising catalyst for carbon-free CO_2 reforming combined with steam reforming or partial oxidation of methane to syngas.
机译:研究了在不同工艺条件下,在NdCoO_3钙钛矿型混合金属氧化物催化剂(H_2还原)下,同时进行蒸汽重整或甲烷部分氧化为合成气的CO_2重整。在同时进行的CO_2和蒸汽重整中,甲烷和H_2O的转化率以及H_2 / CO产物比受CO_2 / H_2O进料比的影响很大。在同时进行CO_2重整和甲烷部分氧化的过程中,甲烷和CO_2的转化率,H_2的选择性和反应的净热受工艺参数(即温度,空速和进料中O_2的相对浓度)的影响很大。在两种情况下,均未观察到碳沉积在催化剂上。还原的NdCoO_3钙钛矿型混合氧化物催化剂(Co分散在Nd_2O_3上)是用于无碳CO_2重整与蒸汽重整或甲烷部分氧化为合成气的极有希望的催化剂。

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