Abstract
Catalytic hydroisomerization of n-heptane was carried out following the reduction by hydrogen of bulk MoO 3, MoO 3/TiO 2, as well as MoO 3 were present on the surface of commercial bulk MoO 2. A conversion of 55% and a selectivity of more than 90% in isomerization products, mainly 2- and 3-methyl hexanes, were obtained at 573 K using the supported system. The major hydrocracking products obtained are C3 and C4 with a ratio C3/C4=1.2. Modifications of the reactant flow rate as well as the catalyst mass, enabled us to increase the conversion to 74% with a selectivity of 82% in isomerization products at 573 K reaction temperature. The catalytic active phase is attributed to the bifunctional MoO 2(H x ) ac. single phase. The metallic function is assured by MoO 2 delocalized π electrons as identified by XPS–UPS in terms of density of state (DOS) at the Fermi-level. The Brönsted acidic functional group(s), (H x ) ac. were deduced from the adsorption of ammonia, the isomerization of olefins at relatively low reaction temperatures in comparison to alkanes and the dehydration of 2-propanol.
Talk to us
Join us for a 30 min session where you can share your feedback and ask us any queries you have
Disclaimer: All third-party content on this website/platform is and will remain the property of their respective owners and is provided on "as is" basis without any warranties, express or implied. Use of third-party content does not indicate any affiliation, sponsorship with or endorsement by them. Any references to third-party content is to identify the corresponding services and shall be considered fair use under The CopyrightLaw.