CO2 reforming of methane to syngas over highly-stable Ni/SBA-15 catalysts prepared by P123-assisted method

被引:63
作者
Yang, Weiwei [1 ]
Liu, Huimin [1 ]
Li, Yuming [1 ]
Wu, Hao [1 ]
He, Dehua [1 ]
机构
[1] Tsinghua Univ, Dept Chem, Key Lab Organ Optoelect & Mol Engn, Innovat Catalysis Program,Minist Educ, Beijing 100084, Peoples R China
基金
中国国家自然科学基金;
关键词
Ni/SBA15; P123; Ni dispersion; Carbon dioxide reforming; Confinement effect; BIMETALLIC CATALYSTS; MESOPOROUS SILICA; SYNTHESIS GAS; CARBON; NI; MECHANISM; COPOLYMER; TRIBLOCK; SBA-15; CH4;
D O I
10.1016/j.ijhydene.2015.11.044
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
Ni/SBA15-P123 (1/X) catalysts were prepared via a simple and novel P123 (PEG-PPG-PEG triblock copolymer)-assisted wet impregnation method, in which 1/X indicates the molar ratio of P123 to Ni. Various techniques including N-2 physisorption, ICP, XRD, TEM, XPS, TGA-DSC and Raman were employed to characterize the physicochemical properties of the catalysts. The catalytic performances of Ni/SBA15-P123 (1/X) catalysts in carbon dioxide reforming of methane to syngas were evaluated with a vertical fixed-bed quartz tube reactor. XRD and TEM characterization results of as-prepared samples revealed that the Ni dispersions of Ni/SBA15-P123 (1/X) catalysts were dramatically improved with n(P123)/n(Ni) ratios in the range of 1/500- 1/50. Significant improvement of the catalytic performances for the above optimum catalysts can be clearly explicated by comparing with those catalysts prepared with no P123, insufficient P123 (1/X = 1/750) or superabundant P123 (1/X = 1/5). That is, Ni/SBA15-P123 (1/500), Ni/SBA15-P123 (1/100) and Ni/SBA15-P123 (1/50) catalysts exhibited better stability, higher activity and less carbon deposition during the 50 h CRM reaction. Copyright (c) 2015, Hydrogen Energy Publications, LLC. Published by Elsevier Ltd. All rights reserved.
引用
收藏
页码:1513 / 1523
页数:11
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