Cl. Zhang et al., Aromatization of methane in the absence of oxygen over Mo-based catalysts supported on different types of zeolites, CATAL LETT, 56(4), 1998, pp. 207-213
The catalytic performance of Mo-based catalysts supported on various zeolit
es has been studied for methane aromatization in the absence of oxygen in a
fixed-bed continuous-flow quartz reactor, and their catalytic properties a
re correlated with features of zeolite structure. It was found that H-type
silica-alumina zeolites, such as ZSM-5, ZSM-8, ZSM-11 and beta possessing t
wo-dimensional structure and pore diameter equaling the dynamic diameter of
a benzene molecule (about 6 Angstrom) simultaneously, are fine supports fo
r methane activation and aromatization catalysts. Among them, MoO3/H-ZSM-11
has the best activity and stability; for instance, a methane conversion of
8.0% and selectivity higher than 90% was obtained at 973 K. The catalytic
performance of MoO3/H-ZSM-8 is somewhat lower than that of MoO3/H-ZSM-5, wh
ile activity of MoO3/H-beta is lower than that of MoO3/H-ZSM-8. Catalysts s
upported on H-MCM-41 and H-SAPO-34 exhibit low activity for methane aromati
zation and those supported on H-MOR, H-X and H-Y give only a little amount
of ethylene. Over MoO3/H-SAPO-5 and MoO3/H-SAPO-11 no hydrocarbons were det
ected.