Search Results - "Bizkarra, K."

Renewable hydrogen production via steam reforming of simulated bio-oil over Ni-based catalysts by Italiano, C., Bizkarra, K., Barrio, V.L., Cambra, J.F., Pino, L., Vita, A.

“…The production of hydrogen via steam reforming (SR) of simulated bio-oil (glycerol, syringol, n-butanol, m-xylene, m-cresol, and furfural) was investigated…”
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Nickel based monometallic and bimetallic catalysts for synthetic and real bio-oil steam reforming by Bizkarra, K., Bermudez, J.M., Arcelus-Arrillaga, P., Barrio, V.L., Cambra, J.F., Millan, M.

“…Catalysts based on Ni supported on alumina were studied for steam reforming (SR) of a synthetic bio-oil/bio-glycerol mixture and a real bio-oil. Catalyst tests…”
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Preparation of Ni-based catalysts to produce hydrogen from glycerol by steam reforming process by Yurdakul, M., Ayas, N., Bizkarra, K., El Doukkali, M., Cambra, J.F.

“…Nickel and Nickel–Palladium-catalysts supported on Al2O3–ZrO2, Al2O3–ZrO2–La2O3 and on Olivine were synthesized using a combination of sol–gel and wet…”
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Hydrogen production from a model bio-oil/bio-glycerol mixture through steam reforming using Zeolite L supported catalysts by Bizkarra, K., Barrio, V.L., Gartzia-Rivero, L., Bañuelos, J., López-Arbeloa, I., Cambra, J.F.

“…Zeolite L featuring different size and shape (nanocrystals and discs), with and without alkaline metal exchange (Cs or Na), was used as catalyst support in…”
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Hydrogen production from n-butanol over alumina and modified alumina nickel catalysts by Bizkarra, K., Barrio, V.L., Yartu, A., Requies, J., Arias, P.L., Cambra, J.F.

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Hydrogen production by steam reforming of m-cresol, a bio-oil model compound, using catalysts supported on conventional and unconventional supports by García-García, I., Acha, E., Bizkarra, K., Martínez de Ilarduya, J., Requies, J., Cambra, J.F.

“…The steam-reforming of a bio-oil model compound, like m-cresol, was performed in order to produce renewable hydrogen. Different nickel based catalysts…”
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Sustainable hydrogen production from bio-oil model compounds (meta-xylene) and mixtures (1-butanol, meta-xylene and furfural) by Bizkarra, K., Barrio, V.L., Arias, P.L., Cambra, J.F.

“…[Display omitted] •High conversions and hydrogen yields were achieved at 800 and 700°C.•Catalysts deactivation only happened during the SR of the…”
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Ni and RhNi catalysts supported on Zeolites L for hydrogen and syngas production by biogas reforming processes by Izquierdo, U., Barrio, V.L., Bizkarra, K., Gutierrez, A.M., Arraibi, J.R., Gartzia, L., Bañuelos, J., Lopez-Arbeloa, I., Cambra, J.F.

“…•Very high conversions were reached by all tested catalysts and operation conditions.•For biogas SR at S/C=1.0 and TR, H2/CO ratios near to 2.0 were…”
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