Origin of the Improved Performance in Lanthanum-doped Silica-supported Ni Catalysts

被引:16
作者
Baudouin, David [1 ,2 ]
Margossian, Tigran [2 ]
Rodemerck, Uwe [3 ]
Webb, Paul B. [4 ]
Veyre, Laurent [1 ]
Krumeich, Frank [2 ]
Candy, Jean-Pierre [1 ]
Thieuleux, Chloe [1 ]
Coperet, Christophe [2 ]
机构
[1] Univ Lyon, Inst Chim Lyon, UMR 5265, CNRS,UCBL,CPE Lyon,LC2P2, 43 Bd 11 Novembre 1918, F-69616 Villeurbanne, France
[2] Swiss Fed Inst Technol, Dept Chem & Appl Biosci, 2 Vladimir Prelog Web,1-ETH Zurich, CH-8093 Zurich, Switzerland
[3] Univ Rostock, Leibniz Inst Catalysis, Albert Einstein Str 29a, D-18059 Rostock, Germany
[4] Sasol Technol UK Ltd, Purdie Bldg, St Andrews KY16 9ST, Fife, Scotland
关键词
carbon dioxide fixation; doping; lanthanum; nickel; supported catalysts; CARBON-DIOXIDE; SYNTHESIS GAS; METHANE ACTIVATION; METGAS CO-2H(2); PARTICLE-SIZE; HYDROGEN; CO2; STEAM; OXIDE; ADSORPTION;
D O I
10.1002/cctc.201600582
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
Dry-reforming catalysts were prepared by supporting Ni nanoparticles (2-3nm) on La-doped silica. These materials display higher activity and stability in low-temperature dry reforming (773K) than Ni/SiO2 or Ni/La2O3. The La-doped silica-supported catalysts were found to have exclusively lanthanum silicate at their surface rather than La2O3 and/or SiO2. While an increasing amount of La was found to favor both CO2 adsorption capacity and strength, it also influenced the hydrogen adsorption strength on nickel particles significantly, as evidenced by H-2 temperature-programmed desorption analysis. Finally, CH4 temperature-programmed reduction analysis revealed that the CH4 cracking threshold temperature varies in the order: Ni-bulk<Ni/La-34@SiO2<Ni/La-2.1@SiO2<<Ni/SiO2<Ni/La2O3, which parallels the catalytic performance. Balancing the adsorption of CH4, H-2, and CO2 on supported Ni nanoparticles (2-3nm) on La-doped silica improves the catalytic performance of this low-temperature dry-reforming catalyst.
引用
收藏
页码:586 / 596
页数:11
相关论文
共 62 条
[1]   Local and bulk 13C hyperpolarization in nitrogen-vacancy-centred diamonds at variable fields and orientations [J].
Alvarez, Gonzalo A. ;
Bretschneider, Christian O. ;
Fischer, Ran ;
London, Paz ;
Kanda, Hisao ;
Onoda, Shinobu ;
Isoya, Junichi ;
Gershoni, David ;
Frydman, Lucio .
NATURE COMMUNICATIONS, 2015, 6
[2]   The multiple roles for catalysis in the production of H2 [J].
Armor, JN .
APPLIED CATALYSIS A-GENERAL, 1999, 176 (02) :159-176
[3]   Carbonatation and Decarbonatation Kinetics in the La2O3-La2O2CO3 System under CO2 Gas Flows [J].
Bakiz, Bahcine ;
Guinneton, Frederic ;
Arab, Madjid ;
Benlhachemi, Abdeljalil ;
Villain, Sylvie ;
Satre, Pierre ;
Gavarri, Jean-Raymond .
ADVANCES IN MATERIALS SCIENCE AND ENGINEERING, 2010, 2010
[4]   THE STOICHIOMETRY OF HYDROGEN AND CARBON-MONOXIDE CHEMISORPTION ON ALUMINA-SUPPORTED AND SILICA-SUPPORTED NICKEL [J].
BARTHOLOMEW, CH ;
PANNELL, RB .
JOURNAL OF CATALYSIS, 1980, 65 (02) :390-401
[5]  
Baudouin D., 2011, THESIS
[6]   Particle size effect in the low temperature reforming of methane by carbon dioxide on silica-supported Ni nanoparticles [J].
Baudouin, David ;
Rodemerck, Uwe ;
Krumeich, Frank ;
de Mallmann, Aimery ;
Szeto, Kai C. ;
Menard, Herve ;
Veyre, Laurent ;
Candy, Jean-Pierre ;
Webb, Paul B. ;
Thieuleux, Chloe ;
Coperet, Christophe .
JOURNAL OF CATALYSIS, 2013, 297 :27-34
[7]   Steam reforming and graphite formation on Ni catalysts [J].
Bengaard, HS ;
Norskov, JK ;
Sehested, J ;
Clausen, BS ;
Nielsen, LP ;
Molenbroek, AM ;
Rostrup-Nielsen, JR .
JOURNAL OF CATALYSIS, 2002, 209 (02) :365-384
[8]   The state of zirconia supported platinum catalysts for CO2/CH4 reforming [J].
Bitter, JH ;
Seshan, K ;
Lercher, JA .
JOURNAL OF CATALYSIS, 1997, 171 (01) :279-286
[9]   CARBON-DIOXIDE REFORMING OF METHANE OVER LANTHANUM-MODIFIED CATALYSTS IN A FLUIDIZED-BED REACTOR [J].
BLOM, R ;
DAHL, IM ;
SLAGTERN, A ;
SORTLAND, B ;
SPJELKAVIK, A ;
TANGSTAD, E .
CATALYSIS TODAY, 1994, 21 (2-3) :535-543
[10]   Effect of MgO additive on catalytic properties of Co/SiO2 in the dry reforming of methane [J].
Bouarab, R ;
Akdim, O ;
Auroux, A ;
Cherifi, O ;
Mirodatos, C .
APPLIED CATALYSIS A-GENERAL, 2004, 264 (02) :161-168