Product yield in methanol conversion over ZSM-5 is predominantly independent of coke content
- 1 December 2012
- journal article
- Published by Elsevier BV in Microporous and Mesoporous Materials
- Vol. 164, 190-198
- https://doi.org/10.1016/j.micromeso.2012.06.020
Abstract
No abstract availableKeywords
This publication has 31 references indexed in Scilit:
- Conversion of Methanol to Hydrocarbons: How Zeolite Cavity and Pore Size Controls Product SelectivityAngewandte Chemie-International Edition, 2012
- Role of internal coke for deactivation of ZSM-5 catalysts after low temperature removal of coke with NO2Catalysis Science & Technology, 2012
- Structure–deactivation relationship for ZSM-5 catalysts governed by framework defectsJournal of Catalysis, 2011
- “Coking” of zeolites during methanol conversion: Basic reactions of the MTO-, MTP- and MTG processesCatalysis Today, 2010
- A new approach to the modeling of deactivation in the conversion of methanol on zeolite catalystsJournal of Catalysis, 2009
- Methanol Conversion to Light Olefins over SAPO-34: Reaction Network and Deactivation KineticsIndustrial & Engineering Chemistry Research, 2006
- Supramolecular Origins of Product Selectivity for Methanol-to-Olefin Catalysis on HSAPO-34Journal of the American Chemical Society, 2001
- The effect of crystal size of SAPO-34 on the selectivity and deactivation of the MTO reactionMicroporous and Mesoporous Materials, 1999
- Influence of Coke Deposition on Selectivity in Zeolite CatalysisIndustrial & Engineering Chemistry Research, 1997
- The conversion of methanol and other O-compounds to hydrocarbons over zeolite catalystsJournal of Catalysis, 1977