Institute Investigaciones en Tecnologia Quimica Chacabuco y Pedernera

San Luis del Palmar, Argentina

Institute Investigaciones en Tecnologia Quimica Chacabuco y Pedernera

San Luis del Palmar, Argentina

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Galetti A.E.,Institute Investigaciones en Tecnologia Quimica Chacabuco y Pedernera | Barroso M.N.,Institute Investigaciones en Tecnologia Quimica Chacabuco y Pedernera | Gomez M.F.,Institute Investigaciones en Tecnologia Quimica Chacabuco y Pedernera | Arrua L.A.,Institute Investigaciones en Tecnologia Quimica Chacabuco y Pedernera | And 2 more authors.
Catalysis Letters | Year: 2012

Hydrogen production by ethanol steam reforming was studied using Ni catalysts supported over MgAl2O4 doped with Ce or Pr. Ni/MgAl2O4-CeO2 catalyst obtained from nickel nitrate impregnation was selected as the best one (final steady conversion = 95.8 %, carbon formation = 0.4 wt% and activity decay = 6.6 %) under the experimental conditions used in this work. Graphical Abstract: Product distribution and ethanol conversion in ethanol steam reforming over a MAP-Ac; b MAP-Nt; c MAC-Ac and d MAC-Nt catalysts.[Figure not available: see fulltext.] © 2012 Springer Science+Business Media New York.

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