Acid−Metal Balance of a Hydrocracking Catalyst: Ideal versus Nonideal Behavior
- 24 December 2004
- journal article
- research article
- Published by American Chemical Society (ACS) in Industrial & Engineering Chemistry Research
- Vol. 44 (14) , 5159-5169
- https://doi.org/10.1021/ie049375+
Abstract
No abstract availableKeywords
This publication has 18 references indexed in Scilit:
- Kinetic modeling of pore mouth catalysis in the hydroconversion of n-octane on Pt-H-ZSM-22Journal of Catalysis, 2003
- Alkene Protonation Enthalpy Determination from Fundamental Kinetic Modeling of Alkane Hydroconversion on Pt/H–(US)Y-ZeoliteJournal of Catalysis, 2001
- Evidence for Alkylcarbenium Ion Reaction Intermediates from Intrinsic Reaction Kinetics of C6–C9n-Alkane Hydroisomerization and Hydrocracking on Pt/H–Y and Pt/USY ZeolitesJournal of Catalysis, 2000
- Hydrocracking of n-Alkane Mixtures on Pt/H−Y Zeolite: Chain Length Dependence of the Adsorption and the Kinetic ConstantsIndustrial & Engineering Chemistry Research, 1997
- Hydroisomerization and Hydrocracking of AlkanesJournal of Catalysis, 1996
- Catalytic Hydroprocessing of Simulated Heavy Coal Liquids. 2.Reaction Networks of Aromatic Hydrocarbons and Sulfur and Oxygen Heterocyclic CompoundsIndustrial & Engineering Chemistry Research, 1994
- Impact of catalyst acid/metal balance in hydroisomerization of normal paraffinsAIChE Journal, 1993
- Hydroisomerization and hydrocracking of n-alkanes. 1. Ideal hydroisomerization PtHY catalystsIndustrial & Engineering Chemistry Product Research and Development, 1986
- Dehydrogenation of 1-Butene into Butadiene. Kinetics, Catalyst Coking, and Reactor DesignIndustrial & Engineering Chemistry Process Design and Development, 1976
- Settling of Flocculated Suspensions of Titanium Dioxide and Alum Mud in WaterIndustrial & Engineering Chemistry Process Design and Development, 1972