How do the products in methane ...
Type de document :
Compte-rendu et recension critique d'ouvrage
Titre :
How do the products in methane dehydroaromatization impact the distinct stages of the reaction?
Auteur(s) :
Beuque, Antoine [Auteur]
Institut de Chimie des Milieux et Matériaux de Poitiers [IC2MP]
Hao, Hu [Auteur]
Unité de Catalyse et Chimie du Solide - UMR 8181 [UCCS]
Berrier, Elise [Auteur]
Laboratoire de Physique des Lasers, Atomes et Molécules - UMR 8523 [PhLAM]
Batalha, Nuno [Auteur]
Institut de Chimie des Milieux et Matériaux de Poitiers [IC2MP]
Sachse, Alexander [Auteur]
Institut de Chimie des Milieux et Matériaux de Poitiers [IC2MP]
Paul, Jean-François [Auteur]
Unité de Catalyse et Chimie du Solide - UMR 8181 [UCCS]
Pinard, Ludovic [Auteur]
Institut de Chimie des Milieux et Matériaux de Poitiers [IC2MP]
Institut de Chimie des Milieux et Matériaux de Poitiers [IC2MP]
Hao, Hu [Auteur]
Unité de Catalyse et Chimie du Solide - UMR 8181 [UCCS]
Berrier, Elise [Auteur]
Laboratoire de Physique des Lasers, Atomes et Molécules - UMR 8523 [PhLAM]
Batalha, Nuno [Auteur]
Institut de Chimie des Milieux et Matériaux de Poitiers [IC2MP]
Sachse, Alexander [Auteur]
Institut de Chimie des Milieux et Matériaux de Poitiers [IC2MP]
Paul, Jean-François [Auteur]
Unité de Catalyse et Chimie du Solide - UMR 8181 [UCCS]
Pinard, Ludovic [Auteur]
Institut de Chimie des Milieux et Matériaux de Poitiers [IC2MP]
Titre de la revue :
Applied Catalysis B: Environmental
Pagination :
121274
Éditeur :
Elsevier
Date de publication :
2022
ISSN :
0926-3373
Mot(s)-clé(s) en anglais :
Zeolite
Methane dehydroaromatization
Molybdenum species
Brønsted acidity
Catalytic activity
Deactivation
methane dehydroaromatization
deactivation molybdenum
carbides
hydrogen
Methane dehydroaromatization
Molybdenum species
Brønsted acidity
Catalytic activity
Deactivation
methane dehydroaromatization
deactivation molybdenum
carbides
hydrogen
Discipline(s) HAL :
Chimie/Chimie organique
Chimie/Catalyse
Chimie/Catalyse
Résumé en anglais : [en]
Among all the proposed catalytic systems (new supports, synthesis post-treatment, new metal transition, multi-metallic catalysts, etc.) for the methane dehydroaromatization, the initial Mo/ZSM-5 has remained one of the ...
Lire la suite >Among all the proposed catalytic systems (new supports, synthesis post-treatment, new metal transition, multi-metallic catalysts, etc.) for the methane dehydroaromatization, the initial Mo/ZSM-5 has remained one of the best suitable catalysts, despite its lack of deep understanding. The catalyst evolves throughout four successive stages: calcination, activation, induction, and deactivation. By studying the balance influence between the acid and metal functions throughout its lifetime, the molybdenum and carbon species could be localized, quantified, and identified as well as their roles. An optimal compromise was then established where the catalyst is composed of 4 wt.% Mo with the highest possible acidity. Below these targets, the catalysts with minimal Mo content and low Brønsted acidity display no significant performances. Once this Mo loading is exceeded, zeolite amorphization occurs independently of the zeolite acidity. Actually, in molybdenum excess, a high amount of water is produced during the activation step. The low space velocity of the water flow, its hightemperature initiate reaction on both metallic and acid catalyst functions leading to molybdenum change of morphology and zeolite dealumination, respectively.Lire moins >
Lire la suite >Among all the proposed catalytic systems (new supports, synthesis post-treatment, new metal transition, multi-metallic catalysts, etc.) for the methane dehydroaromatization, the initial Mo/ZSM-5 has remained one of the best suitable catalysts, despite its lack of deep understanding. The catalyst evolves throughout four successive stages: calcination, activation, induction, and deactivation. By studying the balance influence between the acid and metal functions throughout its lifetime, the molybdenum and carbon species could be localized, quantified, and identified as well as their roles. An optimal compromise was then established where the catalyst is composed of 4 wt.% Mo with the highest possible acidity. Below these targets, the catalysts with minimal Mo content and low Brønsted acidity display no significant performances. Once this Mo loading is exceeded, zeolite amorphization occurs independently of the zeolite acidity. Actually, in molybdenum excess, a high amount of water is produced during the activation step. The low space velocity of the water flow, its hightemperature initiate reaction on both metallic and acid catalyst functions leading to molybdenum change of morphology and zeolite dealumination, respectively.Lire moins >
Langue :
Anglais
Vulgarisation :
Non
Source :
Fichiers
- https://hal.archives-ouvertes.fr/hal-03647187/document
- Accès libre
- Accéder au document
- https://hal.archives-ouvertes.fr/hal-03647187/document
- Accès libre
- Accéder au document
- document
- Accès libre
- Accéder au document
- j.apcatb.2022.121274
- Accès libre
- Accéder au document
- draft%20final%20publi%20Tc-1.pdf
- Accès libre
- Accéder au document