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E. Acha

Researcher at University of the Basque Country

Publications -  28
Citations -  265

E. Acha is an academic researcher from University of the Basque Country. The author has contributed to research in topics: Catalysis & Pyrolysis. The author has an hindex of 8, co-authored 24 publications receiving 177 citations.

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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

TL;DR: In this paper, a steam-reforming of a bio-oil model compound, like m-cresol, was performed in order to produce renewable hydrogen using nickel-based catalysts supported on both conventional and unconventional supports.
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Hydrogen rich reducing gases generation in the production of charcoal from woody biomass carbonization

TL;DR: In this paper, the authors studied the carbonization process of woody biomass with the aim of producing a metallurgical grade charcoal and at the same time, a gas reducing agent with a high proportion of H 2 ǫ+ǫ through the thermo-catalytic treatment of the pyrolysis vapors.
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Thermo-Catalytic Treatment of Vapors in the Recycling Process of Carbon Fiber-Poly (Benzoxazine) Composite Waste by Pyrolysis

TL;DR: In this article, the authors presented the possibility of recovering chemical compounds through the thermo-catalytic treatment of the gases and vapors produced from the decomposition of the polymeric resin that takes place in the recycling of carbon fiber reinforced plastics by pyrolysis.
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Reclamation of carbon fibers and added-value gases in a pyrolysis-based composites recycling process

TL;DR: In this article, the possibility of obtaining high-value gaseous fractions by treating the vapors generated in the decomposition of a poly(benzoxazine) containing carbon fiber waste composite has been studied.
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PdCu membrane applied to hydrogen production from methane

TL;DR: In this paper, a PdCu membrane was characterized and then tested in complex hydrogen containing streams from methane oxidation and reforming processes, where 60% of the hydrogen produced in the catalytic reactor was separated in the membrane module, operating at 673 K, 3.5 bar(g) feed pressure and 550 NmL/min of sweep gas.