Hydrogen production by ethanol steam reforming on nickel catalysts: Effect of support modification by CeO2 and La2O3. (1st May 2015)

• Record Type: Journal Article
• Authors: Dan, Monica; Mihet, Maria; Tasnadi-Asztalos, Zsolt; Imre-Lucaci, Arpad; Katona, Gabriel; Lazar, Mihaela D.
• Is Part Of: Fuel. Volume 147(2015)
• Page Start: 260
• Page End: 268
• Publication Date: 2015-05-01
• Subjects: Hydrogen -- Ethanol steam reforming -- CeO2 promoted catalysts -- La2O3 promoted catalyst -- Thermodynamic evaluation of ethanol steam reforming; Fuel -- Periodicals; Coal -- Periodicals; Coal; Fuel; Periodicals; 662.6
• DOI: 10.1016/j.fuel.2015.01.050
• Languages: English
• ISSNs: 0016-2361

Abstract

Highlights: Ethanol steam reforming on Ni/Al2 O3 and Ni/ZrO2 promoted with ceria and lanthana. The addition of CeO2 and La2 O3 lead to better Ni dispersion on both supports. Improved ethanol conversion at low temperatures for La2 O3 promoted catalysts. The best hydrogen yield at 350 °C was obtained for Ni/La2 O3 –ZrO2 . Abstract: Ethanol steam reforming at low temperatures and high water:ethanol ratios was studied on Ni (8 wt.%) catalysts deposited on CeO2 (6 wt.%) or La2 O3 (6 wt.%) promoted alumina and zirconia supports. The catalysts were prepared by successive impregnation: first the rare earth oxide and then the Ni, and characterized by XRD, H2 chemisorption, TPR and H2 -TPD. Promotion of both alumina and zirconia with CeO2 and La2 O3 leads to changes in the Ni – support interaction resulting in much better dispersion and stabilization of the Ni nanoparticles on the catalyst surface. For La2 O3 promoted catalysts 100% ethanol conversion was obtained in the experimental conditions used in this work, at temperatures as low as 300 °C. The ethanol conversion was improved by the addition of CeO2 to zirconia supported catalyst, but was not significantly influenced by the addition of CeO2 to alumina supported one. A thermodynamic study of ethanol steam reforming was performed (CHEMCAD process simulator and Gibbs reactor with calculations based on free energy minimization), in order to find the thermodynamic equilibrium composition of reaction products in the particular experimental reaction conditions used in this work. The reaction products mixture at 350 °C contains higher proportion of hydrogen and lower proportion of methane than the equilibrium concentration predicted by thermodynamic analysis. The best hydrogen yield was obtained for Ni/La2 O3 –ZrO2 catalyst. All catalysts except Ni/ZrO2 are stable in 24 h time on stream experiments.