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Carlo Resini

Researcher at University of Genoa

Publications -  6
Citations -  374

Carlo Resini is an academic researcher from University of Genoa. The author has contributed to research in topics: Catalysis & Steam reforming. The author has an hindex of 6, co-authored 6 publications receiving 345 citations. Previous affiliations of Carlo Resini include Chartered Institute of Management Accountants.

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Journal ArticleDOI

Characterization of cubic ceria–zirconia powders by X-ray diffraction and vibrational and electronic spectroscopy

Vicente Sanchez Escribano, +5 more
- 01 Oct 2003 - 
TL;DR: In this paper, the X-ray diffraction (XRD) patterns and the Infrared, Raman and UV-visible spectra of CeO 2 ZrO 2 powders prepared by co-precipitation are presented.
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Hydrogen production by ethanol steam reforming over Ni catalysts derived from hydrotalcite-like precursors: Catalyst characterization, catalytic activity and reaction path

Carlo Resini, +15 more
- 28 Feb 2009 - 
TL;DR: In this paper, the urea hydrolysis method has been applied to prepare Ni−Zn−Al and Ni−Mg−Al layered double hydroxides (LDHs) to be used as precursors of mixed oxide catalysts for the ethanol steam reforming (ESR) reaction.
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Production of hydrogen by steam reforming of C3 organics over Pd–Cu/γ-Al2O3 catalyst

Carlo Resini, +11 more
- 01 Jan 2006 - 
TL;DR: In this article, the C3 organics propane, propene, isopropanol and acetone were investigated over a Pd-Cu/Al2O3 catalyst in a flow reactor.
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Propene versus propane steam reforming for hydrogen production over Pd-based and Ni-based catalysts

Carlo Resini, +7 more
- 01 Jul 2005 - 
TL;DR: Experiments of propane and propene steam reforming have been performed over a Pd-Cu/c-Al 2O3 catalyst and over a Ni/NiAl2O4 catalyst.
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Catalytic wet oxidation of phenol over lanthanum strontium manganite

Carlo Resini, +8 more
- 01 Dec 2008 - 
TL;DR: In this article, the effect of temperature, catalyst loading, phenol concentration and stirrer speed on phenol conversion was evaluated under milder conditions of temperature (398 −498 K) and pressure (P o 2 = 4 bar ), in a batch reactor.