Catalytic activity and aromatic selectivity of n-butane transformation were
studied over various MFI type zeolites. From the data obtained, a reaction
mechanism is suggested for different catalyst systems. It is visualized th
at in gallium doped catalysts, Ga3+ directly takes part both in cracking an
d dehydrogenation. The [Ga CH3](2+) and [GaH](2+) species formed during cra
cking and dehydrogenation require protonic sites for regeneration of Ga3+ s
pecies. An alternative mechanism was suggested for dehydrogenation and crac
king by Ga3+ without the involvement of protonic sites. However a protonic
site would be required for aromatization. In case of gallosilicates a one s
tep mechanism is suggested for cracking and dehydrogenation reaction which
does not require the presence of protonic sites in the catalyst system.