Aromatization and isomerization of methylcyclohexane over Ni catalysts supported on different supports

摘要

In this work, nickel metal supported on different supports (SiOsub2/sub, Alsub2/subOsub3/sub, ZSM-5) were prepared by spraying nickel nitrate on the supports and calcined at 873?K. Then, they were characterized by XRD, XRF, Nsub2/sub adsorption–desorption, NHsub3/sub-TPD, MCH-TPD, Hsub2/sub-TPR, and pyridine-FTIR, and tested as catalysts for the dehydrogenation aromatization and isomerization of methylcyclohexane (MCH) under the conditions of S-Zorb catalytic adsorption desulfurization (T?=?673?K, P?=?1.5?MPa, WHSV?=?5?hsup?1/sup). The Hsub2/sub-TPR results showed that the interaction of NiO with support decreased in the order of NiO/ZSM-5-Fe??NiO/ZSM-5??NiO/Alsub2/subOsub3/sub??NiO/SiOsub2/sub. The decrease of the interaction appeared to facilitate the reduction of Ni and therefore to promote the dehydrogenation aromatization of MCH. It was found that a direct correlation existed between the gasoline components yields, cracking activity and the total number of different supports acid sites measured by NHsub3/sub-TPD tests. Higher total acidity of ZSM-5 resulted in gasoline loss because of higher cracking activity of MCH. The number of total acid sites of NiO/ZSM-5-Fe decreased and the medium strong Br?nsted acid sites necessary for MCH isomerization increased after the modification of ZSM-5 by iron metal. So, NiO/ZSM-5-Fe exhibited enhanced MCH conversion, aromatic and isomerization yields when compared to NiO/ZSM-5 and other Ni-based catalysts. This study shows that NiO/ZSM-5-Fe catalyst may be possible to be integrated into the S-Zorb system achieving the recovery of the octane number of gasoline.