Effect of low loading of yttrium on Ni-based layered double hydroxides in CO2 reforming of CH4

被引:12
作者
Swirk, Katarzyna [1 ,2 ]
Motak, Monika [2 ]
Grzybek, Teresa [2 ]
Ronning, Magnus [3 ]
Da Costa, Patrick [1 ]
机构
[1] Sorbonne Univ, CNRS, Inst Jean le Rond dAlembert, F-78210 St Cyr Lecole, France
[2] AGH Univ Sci & Technol, Dept Fuel Technol, PL-30059 Krakow, Poland
[3] Norwegian Univ Sci & Technol, Dept Chem Engn, N-7491 Trondheim, Norway
关键词
Dry reforming of methane; Nickel; Yttrium; Layered double hydroxides; HYDROTALCITE-DERIVED CATALYSTS; BIMETALLIC CATALYSTS; CARBON-DIOXIDE; NI/SBA-15; CATALYSTS; SUPPORT COMPOSITION; CRYSTALLITE SIZE; LOW-TEMPERATURE; MIXED OXIDES; METHANE; PERFORMANCE;
D O I
10.1007/s11144-018-1515-9
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/Al/Mg layered double hydroxides (LDHs) modified with low loading of yttrium (0.2 and 0.4wt%) were used in dry reforming of methane at 700 degrees C. Physicochemical characterization, such as: X-ray fluorescence, N-2 sorption, X-ray diffraction, temperature programmed reduction in H-2, temperature programmed desorption of CO2, H-2 chemisorption, thermogravimetry analysis coupled by mass spectrometry and Raman spectroscopy, showed that the introduction of low loadings of yttrium lead to a smaller Ni degrees crystallite size, a decrease in reducibility of the nickel, and a decreased number of basic sites in the modified Ni/LDHs catalysts. The doping with 0.4wt% of Y improves catalytic activity resulting in higher CH4 and CO2 conversions at 700 degrees C, i.e., ca. 84% and ca. 87%, respectively with no clear deactivation observed after 5h run. The increase in CO2 conversion and a decrease of H-2/CO ratio indicates that side reactions occurs during DRM.
引用
收藏
页码:611 / 628
页数:18
相关论文
共 62 条
[1]  
Alper Erdogan, 2017, Petroleum, V3, P109, DOI 10.1016/j.petlm.2016.11.003
[2]  
[Anonymous], [No title captured]
[3]  
[Anonymous], 2018, CHEM ENG J
[4]   Catalyst design for dry reforming of methane: Analysis review [J].
Aramouni, Nicolas Abdel Karim ;
Touma, Jad G. ;
Abu Tarboush, Belal ;
Zeaiter, Joseph ;
Ahmad, Mohammad N. .
RENEWABLE & SUSTAINABLE ENERGY REVIEWS, 2018, 82 :2570-2585
[5]   Oxidative reforming of model biogas over NiO-Y2O3-ZrO2 catalysts [J].
Asencios, Yvan J. O. ;
Rodella, Cristiane B. ;
Assaf, Elisabete M. .
APPLIED CATALYSIS B-ENVIRONMENTAL, 2013, 132 :1-12
[6]   Stable Ni/Al2O3 catalysts for methane dry reforming -: Effects of pretreatment [J].
Becerra, A ;
Dimitrijewits, M ;
Arciprete, C ;
Luna, AC .
GRANULAR MATTER, 2001, 3 (1-2) :79-81
[7]   Effect of the Y2O3-ZrO2 support composition on nickel catalyst evaluated in dry reforming of methane [J].
Bellido, Jorge D. A. ;
Assaf, Elisabete M. .
APPLIED CATALYSIS A-GENERAL, 2009, 352 (1-2) :179-187
[8]   CO2 reforming of methane to syngas I:: evaluation of hydrotalcite clay-derived catalysts [J].
Bhattacharyya, A ;
Chang, VW ;
Schumacher, DJ .
APPLIED CLAY SCIENCE, 1998, 13 (5-6) :317-328
[9]   PREPARATION OF PD/SIO2 CATALYSTS FOR METHANOL SYNTHESIS .3. EXPOSED METAL FRACTION AND HYDROGEN SOLUBILITY [J].
BONIVARDI, AL ;
BALTANAS, MA .
JOURNAL OF CATALYSIS, 1992, 138 (02) :500-517
[10]   Sorbent-Enhanced Methane Reforming over a Ni-Ca-Based, Bifunctional Catalyst Sorbent [J].
Broda, Marcin ;
Kierzkowska, Agnieszka M. ;
Baudouin, David ;
Imtiaz, Qasim ;
Coperet, Christophe ;
Mueller, Christoph R. .
ACS CATALYSIS, 2012, 2 (08) :1635-1646