Olefin production by cofeeding methanol and n-butane: Kinetic modeling considering the deactivation of HZSM-5 zeolite

Catalyst discrimination for olefin production by coupled methanol/n-butane cracking

(2010) Diana Mier et al.   APPLIED CATALYSIS A-GENERAL

Synergies in the production of olefins by combined cracking of n-butane and methanol on a HZSM-5 zeolite catalyst

(2010) Diana Mier et al.   CHEMICAL ENGINEERING JOURNAL

Kinetic Modeling ofn-Butane Cracking on HZSM-5 Zeolite Catalyst

(2010) Diana Mier et al.   INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH

Tailoring the mesopore structure of HZSM-5 to control product distribution in the conversion of propanal

(2010) Xinli Zhu et al.   JOURNAL OF CATALYSIS

Product shape selectivity dominates the Methanol-to-Olefins (MTO) reaction over H-SAPO-34 catalysts

(2009) Bart P.C. Hereijgers et al.   JOURNAL OF CATALYSIS

Effect of mesoporosity against the deactivation of MFI zeolite catalyst during the methanol-to-hydrocarbon conversion process

(2009) Jeongnam Kim et al.   JOURNAL OF CATALYSIS

Comparison of the Transport of Aromatic Compounds in Small and Large MFI Particles

(2009) O. C. Gobin et al.   Journal of Physical Chemistry C

Effect of the support acidity on the aromatic ring-opening of pyrolysis gasoline over Pt/HZSM-5 catalysts

(2008) Pedro Castaño et al.   CATALYSIS TODAY

Kinetic Modeling for Assessing the Product Distribution in Toluene Hydrocracking on a Pt/HZSM-5 Catalyst

(2008) Pedro Castaño et al.   INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH

Prevention of zeolite deactivation by coking

(2008) Michel Guisnet et al.   JOURNAL OF MOLECULAR CATALYSIS A-CHEMICAL