Issue 21, 2012

Ni supported high surface area CeO2–ZrO2 catalysts for hydrogen production from ethanol steam reforming

Abstract

The catalytic activity of nano-sized x%Ni/Ce0.74Zr0.26O2 (x = 0, 2, 10 and 20wt%) catalysts have been investigated to develop highly active catalysts for ethanol steam reforming (ESR) into hydrogen. The structure and surface properties of the catalysts were tested by XRD, TPR, HRTEM and BET surface areas. The effect of reaction temperature from 200 °C to 600 °C was studied in a flow system at atmospheric pressure with an ethanol/water molar ratio of 1 : 8. Selectivity was calculated for the catalytic products H2, CO, CO2 and CH4, as well as the intermediates C2H6, C2H4, C3H8, CH3CHO and CH3COCH3, at different reaction temperatures. It was found that complete conversion of ethanol with considerable amounts of H2 was obtained at 400 °C over all catalysts. H2 was produced at a very low temperature (200 °C) over 10% and 20% Ni loadings, while a maximum H2 selectivity (75%) is reached at 600 °C over the 2%Ni/Ce0.74Zr0.26O2 catalyst; this is most likely due to the small nickel particle size (2–4 nm) in 2%Ni, which results in enhancement of the metal–support interactions. Thermal decomposition of ethanol in an ethanol/water mixture under the same reaction conditions, but in the absence of catalyst, was also studied. HRTEM of the spent catalyst (8 h ESR) shows the deposition of carbon in the form of carbon nanotubes (CNTs).

Graphical abstract: Ni supported high surface area CeO2–ZrO2 catalysts for hydrogen production from ethanol steam reforming

Article information

Article type
Paper
Submitted
14 Feb 2012
Accepted
05 Jul 2012
First published
03 Aug 2012

RSC Adv., 2012,2, 8145-8156

Ni supported high surface area CeO2–ZrO2 catalysts for hydrogen production from ethanol steam reforming

M. A. Ebiad, D. R. Abd El-Hafiz, R. A. Elsalamony and Lamia. S. Mohamed, RSC Adv., 2012, 2, 8145 DOI: 10.1039/C2RA20258A

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