4.8 Article

Hydrogen from biogas: Catalytic tri-reforming process with Ni/La-Ce-O mixed oxides

Journal

APPLIED CATALYSIS B-ENVIRONMENTAL
Volume 148, Issue -, Pages 91-105

Publisher

ELSEVIER
DOI: 10.1016/j.apcatb.2013.10.043

Keywords

Biogas; Tri-reforming; Hydrogen production; Syngas; Ni/La2O3-CeO2 catalysts

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A series of Ni catalysts supported on La-Ce-O mixed oxides with different Ni content (Ce1-xLa2xNixO2-delta, x= 0.10; 0.20 and 0.25) prepared by combustion synthesis, was tested in tri-reforming reaction of simulated biogas. The influence of O-2/CH4, CH4/CO2 molar ratios in the reaction stream has been evaluated caring out the reaction at 800 degrees C, under a fixed gas hourly space velocity (GHSV = 31,000 h(-1)). The highest catalytic activity was obtained with the Ce0.70La0.20Ni0.10O2-delta sample that showed high stability (CH4, CO2 conversion rates and the H-2/CO molar ratio in the reformed gas were 1.56 mmol/s gN 0.56 mmol/s gN, and 1.57, respectively) under an average biogas composition (CH4/CO2 = 1.5). No carbon deposition was detected after 150 h of reaction. The characterizations of the samples have highlighted that Ni and La ions were partially incorporated into CeO2 framework, cubic fluorite structure of CeO2 support was retained also at high level of doping. Ni metal phase in close contact with La2O3-CeO2 matrix coupled with Ni2+ with high cationic character appeared to be responsible of the catalytic activity and stability of the catalysts. (C) 2013 Elsevier B.V. All rights reserved.

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