Dry Reforming of Methane over a Ruthenium/Carbon Nanotube Catalyst

被引:9
|
作者
Zhu, Yuan [1 ]
Chen, Kun [2 ]
Barat, Robert [1 ]
Mitra, Somenath [2 ]
机构
[1] New Jersey Inst Technol, Otto H York Dept Chem & Mat Engn, Newark, NJ 07102 USA
[2] New Jersey Inst Technol, Dept Chem & Environm Sci, Newark, NJ 07102 USA
关键词
catalysis; ruthenium; reforming; carbon nanotubes; methane; carbon dioxide; PROCESS PARAMETERS; CARBON NANOTUBES; PERFORMANCE; CONVERSION;
D O I
10.3390/chemengineering4010016
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
In this study, CH4 dry reforming was demonstrated on a novel microwave-synthesized ruthenium (Ru)/carbon nanotube (CNT) catalyst. The catalyst was tested in an isothermal laboratory-packed bed reactor, with gas analysis by gas chromatography/thermal conductivity detection. The catalyst demonstrated excellent dry-reforming activity at modest temperatures (773-973 K) and pressure (3.03 x 10(5) Pa). Higher reaction temperatures favored increased conversion of CH4 and CO2, and increased H-2/CO product ratios. Slight coke deposition, estimated by carbon balance, was observed at higher temperatures and higher feed CH4/CO2. A robust global kinetic model composed of three reversible reactions-dry reforming, reverse water gas shift, and CH4 decomposition-simulates observed outlet species concentrations and reactant conversions using this Ru/CNT catalyst over the temperature range of this study. This engineering kinetic model for the Ru/CNT catalyst predicts a somewhat higher selectivity and yield for H-2, and less for CO, in comparison to previously published results for a similarly prepared Pt_Pd/CNT catalyst from our group.
引用
收藏
页码:1 / 14
页数:14
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