Selective Carbon Deposition on γ-Alumina Acid Sites: toward the Design of Catalyst Supports with Improved Hydrothermal Stability in Aqueous Media.

adsorption carbon hydrothermal decomposition pyrolysis sorbitol γ-alumina boehmite transformation

Journal

ACS applied materials & interfaces
ISSN: 1944-8252
Titre abrégé: ACS Appl Mater Interfaces
Pays: United States
ID NLM: 101504991

Informations de publication

Date de publication:
18 Mar 2020
Historique:
pubmed: 23 2 2020
medline: 23 2 2020
entrez: 21 2 2020
Statut: ppublish

Résumé

γ-Alumina, a widely used industrial catalyst support, undergoes irreversible transformation into various aluminum hydroxides under hydrothermal (HT) conditions, resulting in strong modification of its intrinsic properties. Most of the strategies that have been proposed to prevent or at least minimize its transformation into oxy-hydroxides consist in covering the alumina surface with a hydrophobic carbon layer, making it less sensitive to modifications induced by water. However, such methods necessitate high carbon contents, which significantly modifies structural and chemical properties of alumina. Here, we propose a new method based on a series of adsorption/pyrolysis cycles using sorbitol molecules previously adsorbed on specific hydration sites of the (110) faces of γ-alumina crystals. These sites, which are responsible for the dissolution of γ-alumina crystals in water, are thus selectively protected by carbon clusters, with the rest of the surface being totally exposed and accessible to adsorbates. Under HT conditions (10 h in water at 200 °C), the formation of hydroxides is almost totally suppressed by covering less than 25% of the surface with only 7 wt % carbon, which is far below the amount necessary to achieve similar results with more conventional carbon deposition methods.

Identifiants

pubmed: 32077273
doi: 10.1021/acsami.0c01646
doi:

Types de publication

Journal Article

Langues

eng

Sous-ensembles de citation

IM

Pagination

13558-13567

Auteurs

Etienne Girel (E)

Direction Catalyse et Séparation, IFP Energies Nouvelles, Rond-Point de l'échangeur de Solaize, BP 3, 69360 Solaize, France.
Université de Lyon, Université Claude Bernard Lyon 1, CNRS, IRCELYON-UMR 5256, 2 Avenue Albert Einstein, 69626 Villeurbanne Cedex, France.

Amandine Cabiac (A)

Direction Catalyse et Séparation, IFP Energies Nouvelles, Rond-Point de l'échangeur de Solaize, BP 3, 69360 Solaize, France.

Alexandra Chaumonnot (A)

Direction Catalyse et Séparation, IFP Energies Nouvelles, Rond-Point de l'échangeur de Solaize, BP 3, 69360 Solaize, France.

Michèle Besson (M)

Université de Lyon, Université Claude Bernard Lyon 1, CNRS, IRCELYON-UMR 5256, 2 Avenue Albert Einstein, 69626 Villeurbanne Cedex, France.

Alain Tuel (A)

Université de Lyon, Université Claude Bernard Lyon 1, CNRS, IRCELYON-UMR 5256, 2 Avenue Albert Einstein, 69626 Villeurbanne Cedex, France.

Classifications MeSH