The dependence of ZSM-5 additive performance on the hydrogen-transfer activity of the REUSY base catalyst in fluid catalytic cracking
- 1 June 2001
- journal article
- Published by Elsevier in Applied Catalysis A: General
- Vol. 214 (1) , 11-29
- https://doi.org/10.1016/s0926-860x(01)00482-3
Abstract
No abstract availableThis publication has 14 references indexed in Scilit:
- Influence of coke deactivation and vanadium and nickel contamination on the performance of low ZSM-5 levels in FCC catalystsApplied Catalysis A: General, 2000
- ZSM-5 Additive in Fluid Catalytic Cracking. 2. Effect of Hydrogen Transfer Characteristics of the Base Cracking Catalysts and FeedstocksIndustrial & Engineering Chemistry Research, 1999
- Performance of ZSM-5 as a Fluid Catalytic Cracking Catalyst Additive: Effect of the Total Number of Acid Sites and Particle SizeIndustrial & Engineering Chemistry Research, 1999
- Gasoline selective ZSM-5 FCC additives: Model reactions of C6–C10 olefins over steamed 55:1 and 450:1 ZSM-5Applied Catalysis A: General, 1998
- Compositional changes in FCC gasoline products resulting from high-level additions of ZSM-5 zeolite to RE-USY catalystApplied Catalysis A: General, 1997
- Effects of high temperature and high ZSM-5 additive level on FCC olefins yields and gasoline compositionApplied Catalysis A: General, 1996
- Effects of high-level additions of ZSM-5 to a fluid catalytic cracking (FCC) RE-USY catalystApplied Catalysis A: General, 1995
- Role of ZSM-5 and ultrastable Y zeolites for increasing gasoline octane numberJournal of Catalysis, 1991
- Octane Enhancement in Catalytic Cracking by Using High-Silica ZeolitesPublished by American Chemical Society (ACS) ,1991
- Prediction of cracking catalyst behavior by a zeolite unit cell size modelJournal of Catalysis, 1984