CO2 reforming of methane over highly active La-promoted Ni supported on SBA-15 catalysts: mechanism and kinetic modelling

被引:141
作者
Oemar, U. [1 ]
Kathiraser, Y. [1 ]
Mo, L. [2 ]
Ho, X. K. [1 ]
Kawi, S. [1 ]
机构
[1] Natl Univ Singapore, Dept Chem & Biomol Engn, Singapore 119260, Singapore
[2] Zhejiang Univ, Inst Catalysis, Dept Chem, Hangzhou 310028, Zhejiang, Peoples R China
关键词
ONE-POT SYNTHESIS; CARBON-DIOXIDE; NICKEL-CATALYSTS; SYNTHESIS GAS; SYNGAS PRODUCTION; HYDROGEN-PRODUCTION; NI/SBA-15; CATALYST; MESOPOROUS SILICA; HIGH-PERFORMANCE; TRANSIENT;
D O I
10.1039/c5cy00906e
中图分类号
O64 [物理化学(理论化学)、化学物理学];
学科分类号
070304 ; 081704 ;
摘要
Various Ni catalysts were synthesized by combining a high surface area SBA-15 support, a novel preparation method using an oleic acid precursor to obtain highly dispersed and small Ni particles, and the basic property of La. The activity test shows that the La-promoted Ni/SBA-15 catalyst has much higher catalytic activity and stability than unpromoted Ni/SBA-15 catalysts in the CO2 (dry) reforming of methane (DRM) reaction due to the crucial role of La to simultaneously adsorb CO2 and remove deposited carbon from the Ni metal surface. The optimization of La content shows that only a small amount of La around 1 wt% is necessary to achieve the best catalytic performance. The reaction mechanism was then proposed and kinetic modeling (for pilot scale) was performed to find the rate-determining step (RDS) in the DRM reaction for this 1% La-promoted Ni/SBA-15 catalyst. The obtained fitting result shows that CH4 decomposition is the RDS for this catalyst with an apparent activation energy of around 40.8 kJ mol(-1) which is similar to the activation energies reported for common Ni-based supported catalysts.
引用
收藏
页码:1173 / 1186
页数:14
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