Dry reforming of methane to syngas over La-promoted hydrotalcite clay-derived catalysts

被引:95
|
作者
Serrano-Lotina, A. [1 ]
Martin, A. J. [2 ]
Folgado, M. A. [2 ]
Daza, L. [1 ]
机构
[1] Inst Catalisis & Petr Quim CSIC, Madrid 28049, Spain
[2] CIEMAT, E-28040 Madrid, Spain
关键词
Biogas; Reforming; Hydrogen; Hydrotalcite; Mg/Al ratio; CARBON-DIOXIDE; AL CATALYSTS; ANIONIC CLAYS; METAL-OXIDE; NI; CO2; DEPOSITION; SUPPORT; MGAL; COKE;
D O I
10.1016/j.ijhydene.2012.06.041
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
Hydrotalcite-like compounds with general formula [M(II)(1-x)M(III)(x)(OH)(2)](x+)(A(x/n)(n-)) mH(2)O, where A(n-) is the compensation anion, were promoted with lanthanum and used as precursors for active catalysts for dry reforming of methane. Four precursors were prepared by co-precipitation and characterized by X-ray diffraction (XRD) and temperature programmed oxidation (TPO-MS). Three of them showed pure hydrotalcite structure. However, Mg/Al molar ratio of 4 provoked the formation of hydromagnesite phase. N-2 physisorption, X-ray diffraction (XRD), temperature programmed reduction (TPR-MS) and X-ray photoelectron spectroscopy (XPS) provided structural, morphological and compositional information about the catalysts. Post-reaction characterization by TPO-MS and scanning electron microscopy (SEM) was also performed in order to evaluate whether carbon actually deposited during reaction. As Mg/Al molar ratio rose, some properties changed: thermal stability increased, BET surface area, and reducibility of Mg(Ni,Al)O decreased while free or segregated NiO reducibility increased. Even though high Mg/Al molar ratios did not favour catalytic activities, it led to enhanced stability during reaction tests, as a consequence of lower deactivation and/or carbon deposition rates. The best stability was achieved at Mg/Al = 3, during a 120 h test. Reduction of Ni inside Ni(Mg,Al)O phase led to a decrease on catalysts' stability. Copyright (c) 2012, Hydrogen Energy Publications, LLC. Published by Elsevier Ltd. All rights reserved.
引用
收藏
页码:12342 / 12350
页数:9
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