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Partial oxidation of methane with air for methanol production in a post-plasma catalytic system

机译:等离子体后催化系统中甲烷与空气的部分氧化以生产甲醇

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Partial oxidation of methane to methanol via post-plasma catalysis using a dielectric-barrier discharge was performed under mild reaction conditions. Air was used as the oxidizing co-reactant because of its economical practicality. Three catalysts impregnated with Pt, Fe2O3, CeO2 on ceramic supports located downstream of the discharge zone were examined for increased selectivity towards methanol. It was found that all three catalysts had no significant effect on the conversion of methane, but enhanced methanol selectivity, which could be explained by a two-stage reaction mechanism. The Fe2O3-based catalyst showed the best catalytic activity, and high stability in the reaction. The methanol selectivity of the Fe2O3-assisted plasma process was 36% higher than that of the non-catalytic system at a rather low catalyst temperature (150℃). In addition, the effects of input power, discharge frequency, discharge gap distance, total flow rate, and methane/air ratio on methane conversion and methanol yield were also studied.
机译:在温和的反应条件下,使用介电势垒放电通过等离子体后催化将甲烷部分氧化为甲醇。空气由于其经济实用性而被用作氧化共反应物。检查了在放电区下游的陶瓷载体上浸渍了Pt,Fe2O3,CeO2的三种催化剂对甲醇的选择性提高。发现所有三种催化剂对甲烷的转化没有显着影响,但是提高了甲醇的选择性,这可以通过两阶段反应机理来解释。 Fe2O3基催化剂显示出最佳的催化活性,并且在反应中具有很高的稳定性。在相当低的催化剂温度(150℃)下,Fe 2 O 3辅助等离子体工艺的甲醇选择性比非催化体系的甲醇选择性高36%。此外,还研究了输入功率,放电频率,放电间隙距离,总流速以及甲烷/空气比对甲烷转化率和甲醇产率的影响。

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