Liquid-Metal Indium Catalysis for Direct Dehydrogenative Conversion of Methane to Higher Hydrocarbons

被引:42
作者
Nishikawa, Yuta [1 ]
Ogihara, Hitoshi [2 ]
Yamanaka, Ichiro [2 ]
机构
[1] Tokyo Inst Technol, Dept Chem & Mat Sci, Meguro Ku, 2-12-1 Ookayama, Tokyo, Japan
[2] Tokyo Inst Technol, Dept Chem Sci & Engn, Meguro Ku, 2-12-1 Ookayama, Tokyo, Japan
关键词
methane; direct methane conversion; methane dehydrogenation; indium catalyst; liquid metal catalysis; PARTIAL OXIDATION; MEMBRANE REACTOR; NITROUS-OXIDE; HYDROGEN; AROMATIZATION; DECOMPOSITION; AROMATICS; ETHYLENE; BENZENE; CARBON;
D O I
10.1002/slct.201700734
中图分类号
O6 [化学];
学科分类号
0703 ;
摘要
Catalysts for dehydrogenative conversion of methane (DCM) to higher hydrocarbons are worthy of attention. Indium supported on silica (In/SiO2) was found for effective catalyst for the DCM reaction above 1023 K. Products were ethane, ethylene, acetylene, propylene, benzene, toluene, naphthalene and hydrogen. A highest selectivity of sum of products was 96% at 1098 K and a steady-state sum yield was 2.1% with 63% selectivity at 1173 K. Characterization studies using temperature-programed X-ray diffraction (TP-XRD) and scanning electron microscopy (SEM) indicated that the working state of indium catalyst was liquid metal. Effects of reaction temperature on the product distribution and studies of temperature-programed-reaction (TPR) indicated that liquid-metal indium activated methane and selectively converted to ethane. Higher hydrocarbons were produced from ethane in the gas phase without catalyst.
引用
收藏
页码:4572 / 4576
页数:5
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