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Metal-catalysed steam reforming of ethanol in the production of hydrogen for fuel cell applications

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TLDR
In this article, a range of oxide-supported metal catalysts have been investigated for the steam reforming of ethanol/water mixtures for the production of hydrogen, and it was concluded that the support plays a significant role in the steam reformulation of ethanol.
Abstract
A range of oxide-supported metal catalysts have been investigated for the steam reforming of ethanol/water mixtures for the production of hydrogen. Alumina-supported catalysts are very active at lower temperatures for the dehydration of ethanol to ethene which, at higher temperatures, is converted into H2, CO, and CO2 as the major products and CH4 as a minor product. The order of activity of the metals is Rh>Pd>Ni=Pt. With ceria/zirconia-supported catalysts, the formation of ethene is not observed and the order of activity at higher temperatures is Pt≥Rh>Pd. By using combinations of a ceria/zirconia-supported metal catalyst with the alumina support it is shown that the formation of ethene does not inhibit the steam reforming reaction at higher temperatures. It is concluded that the support plays a significant role in the steam reforming of ethanol.

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Journal ArticleDOI

Current status of hydrogen production techniques by steam reforming of ethanol : A review

TL;DR: In this paper, the current state of the steam reforming process of ethanol, examines different catalysts, and makes a comparative analysis, and concludes that Co/ZnO, ZnO+Al2O3, Co/CeO2, Ni/La 2O3−Ni/La2O2−Al2E3, and Ni/E3−E2E2−E3 performed the best in terms of steam reforming of ethanol.
Journal ArticleDOI

2D Transition‐Metal‐Dichalcogenide‐Nanosheet‐Based Composites for Photocatalytic and Electrocatalytic Hydrogen Evolution Reactions

TL;DR: Recent progress in photocatalytic and electrocatalytic HERs using 2D TMD-based composites as catalysts is discussed.
Journal ArticleDOI

Production of hydrogen for fuel cells by steam reforming of ethanol over supported noble metal catalysts

TL;DR: In this article, the performance of supported noble metal catalysts for the steam reforming (SR) of ethanol has been investigated in the temperature range of 600-850°C with respect to the nature of the active metallic phase (Rh, Ru, Pt, Pd, Al2O3, MgO, TiO2).
Journal ArticleDOI

Production of Hydrogen from Ethanol: Review of Reaction Mechanism and Catalyst Deactivation

TL;DR: Mechanism and Catalyst Deactivation Lisiane V. Mattos,† Gary Jacobs,‡ Burtron H. Davis,† and Fab́io B. Noronha.
References
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Journal ArticleDOI

NOx storage-reduction catalyst for automotive exhaust with improved tolerance against sulfur poisoning

TL;DR: In this article, a hexagonal cell monolithic substrate was developed to make a uniform catalytic wash-coat thickness on the substrate, and hydrogen generation on catalyst was enhanced by adding Rh/ZrO 2 with high steam reforming reactivity.
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Hydrogen from steam reforming of ethanol. characterization and performance of copper-nickel supported catalysts

TL;DR: In this article, the effect of the copper loading and calcination temperature on the structure and performance of Cu/Ni|K|γ-Al2O3 catalysts was examined. But the results were limited to the case of ethanol.
Journal ArticleDOI

Ethanol steam reforming on Rh/Al2O3 catalysts

S. Cavallaro
- 16 Sep 2000 - 
TL;DR: In this paper, a high water content (H2O/C2H5OH = 8.4 mol/mol) was used to simulate the composition of the ecological fuel product from vegetable biomass fermentation.
Journal ArticleDOI

Ethanol steam reforming in a molten carbonate fuel cell. A preliminary kinetic investigation

TL;DR: In this article, the decomposition of ethanol to COx and H2 was investigated under a wide range of operating conditions, including high pressure, high temperature, and high humidity, where high pressure reduces H2, CO and CO2 production, while high temperature produces the opposite effect.
Journal ArticleDOI

Synthesis gas production by steam reforming of ethanol

TL;DR: In this paper, a two-layer fixed-bed catalytic reactor for syngas production by steam reforming of ethanol has been proposed, where ethanol is first converted to a mixture of methane, carbon oxides and hydrogen over a Pd-based catalyst.
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