Natural Gas to Fuels and Chemicals: Improved Methane Aromatization in an Oxygen-Permeable Membrane Reactor
Natural Gas to Fuels and Chemicals: Improved Methane Aromatization in an Oxygen-Permeable Membrane Reactor
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DOI:
10.1002/anie.201307935
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发表时间:
2013-12-16
影响因子:
16.6
通讯作者:
Caro, Juergen
中科院分区:
文献类型:
--
作者:
Cao, Zhengwen;Jiang, Heqing;Caro, Juergen
Methane dehydroaromatization (MDA) is attracting considerable interest from both academia and industry because of its potential in the conversion of methane into chemicals and liquid fuels.[1] Compared to the conventional liquid fuels production based on Fischer–Tropsch technology from syngas (CO+ 2H2), MDA provides a simple, straightforward, and economic pathway from methane to aromatic hydrocarbons without intermediate steps. Intensive efforts have been devoted to the development of suitable catalysts, such as Zn/HZSM-5,[2] Fe/HZSM-5,[3] and Ga/HZSM-5,[4] and encouraging progress has been made, especially on Mo/MCM-22,[5] Mo/HMCM-49,[6] and Mo/HZSM-5.[2, 7] Challenging problems still exist, such as the rapid catalyst deactivation by coke and the limited methane conversion, which hinder the industrialization of MDA.[8] To overcome the equilibrium limitation of Reaction (1), it is proposed that the generated hydrogen can be removed by hydrogen-permeable membranes (metal alloys, zeolite or other molecular sieves, proton/electron conducting ceramics).[9] Using a Pd-coated Nb-Ta membrane, the methane conversion could be increased from 3.8% to 9% at 6008C; however, hydrogen removal resulted in accelerated coking.[9b] Thermodynamically favorable is the substitution of the nonoxidative MDA according to Reaction (1) by the oxidative MDA according to Reaction (2).