The catalytic properties of Mo/HSAPO-34, Mo/H-ZSM-5 and Mo/HY catalyst
s for methane conversion without using oxidants were compared. Mo/H-ZS
M-5 catalyst has the best performance in terms of catalytic activity a
nd stability. This catalyst is very selective for benzene production a
nd the benzene yield is the highest of the three catalysts studied. Th
e catalytic activity and benzene selectivity over the Mo/HSAPO-34 cata
lyst, however, decreased with increasing time on stream. As the cataly
st deactivated, the selectivity to ethene increased. The Mo/HY catalys
t is active for methane conversion but rapid deactivation of the catal
yst resulted in negligible product yield. These results are discussed
in terms of the shape-selectivity effect of the support taking into co
nsideration the high reaction temperature. Preliminary studies on alka
li metal doped Mo/HSAPO-34 catalysts showed no observed effect on cata
lyst deactivation.