Selective hydrogenation of CO2 into CO on a highly dispersed nickel catalyst obtained by magnetron sputtering deposition: A step towards liquid fuels

被引:80
作者
Goncalves, Renato V. [1 ]
Vono, Lucas L. R. [2 ]
Wojcieszak, Robert [3 ]
Dias, Carlos S. B. [4 ]
Wender, Heberton [5 ]
Teixeira-Neto, Erico [6 ]
Rossi, Liane M. [2 ]
机构
[1] Univ Sao Paulo, Sao Carlos Inst Phys, POB 369, BR-13560970 Sao Carlos, SP, Brazil
[2] Univ Sao Paulo, Inst Quim, Dept Quim Fundamental, Av Prof Lineu Prestes 748, BR-05508000 Sao Paulo, SP, Brazil
[3] Univ Artois, UMR 8181, UCCS, Univ Lille,CNRS,Cent Lille,ENSCL, F-59000 Lille, France
[4] Brazilian Synchrotron Light Lab LNLS, Campinas, SP, Brazil
[5] LNNano, Campinas, SP, Brazil
[6] LNNano CNPEM, Electron Microscopy Lab, POB 6192, BR-13083970 Campinas, SP, Brazil
基金
巴西圣保罗研究基金会;
关键词
Reverse water gas shift; CO2; hydrogenation; Magnetron sputtering deposition; Nickel catalyst; WATER-GAS SHIFT; MONODISPERSED NIO PARTICLES; VALUE-ADDED PRODUCTS; CARBON-DIOXIDE; CU/SIO2; CATALYST; ENHANCED SELECTIVITY; GOLD NANOPARTICLES; NI-CEO2; CATALYSTS; CONVERSION; SPECTROSCOPY;
D O I
10.1016/j.apcatb.2017.02.081
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
The transformation of CO2 into CO through the reverse water gas shift (RWGS) reaction is very sensitive to the metal particle size and metal-support interactions. Indeed, large metallic particles or aggregates tend to produce more methane than CO. In this context, magnetron sputtering deposition was explored here for the preparation of highly dispersed nickel catalyst supported on silica. The Ni catalyst prepared for 30 min of sputtering time contains 2.4 wt% of Ni, small metal particles size (2.3 nm) and controlled composition (77% Ni, 23% Ni oxides). In-situ XANES under RWGS reaction conditions indicates reduction of nickel in the temperature range from 250 to 500 C. The conversion of CO2 into CO through the RWGS reaction was close to the thermodynamic equilibrium values for 1:1 and 1:4 (CO2:H-2) gas composition at temperature as high as 800 degrees C. CO was produced continuously for 40 h at 660 degrees C without significant drop of activity. The overall catalytic performance was superior to that of a classical catalyst prepared by incipient wetness impregnation, as evidenced by the higher activity at T> 600 C and stability for a long time on stream. (C) 2017 Elsevier B.V. All rights reserved.
引用
收藏
页码:240 / 246
页数:7
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