Different Sn/H-zeolite (β, MOR, SSZ-13, FER, and
Y zeolite)
catalysts are prepared with the improved impregnation method. The
effects of reaction temperature and the composition of the reaction
gas (ammonia, oxygen, and ethane) on the catalytic reaction are investigated.
Adjusting the fraction of ammonia and/or ethane in the reaction gas
can effectively strengthen the ethane dehydrogenation (ED) route and
ethylamine dehydrogenation (EA) route and inhibit the ethylene peroxidation
(EO) route, whereas the adjustment of oxygen cannot effectively promote
acetonitrile formation because it cannot avoid enhancing the EO route.
By comparing the acetonitrile yields on different Sn/H-zeolite catalysts
at 600 °C, it is revealed that the ammonia pool effect, the residual
Brönsted acid in the zeolite, and the Sn-Lewis acid synergistically
catalyze ethane ammoxidation. Moreover, a higher L/B ratio of the
Sn/H zeolite is beneficial to the improvement of acetonitrile yield.
With a certain application potential, the Sn/H-FER-zeolite catalyst
shows an ethane conversion of 35.2% and an acetonitrile yield of 22.9%
at 600 °C; although a similar catalytic performance was observed
on the best Co-zeolite catalyst in literature, the Sn/H-FER-zeolite
catalyst is more selective to ethene and CO than the Co catalyst.
In addition, the selectivity to CO2 is less than 2% of
that on the Sn-zeolite catalyst. This may be attributed to the special
2D topology and pore/channel system of the FER zeolite, which guarantee
an ideal synergistic effect of the ammonia pool, the residual Brönsted
acid in the zeolite, and the Sn-Lewis acid for the Sn/H-FER-catalyzed
ethane ammoxidation reaction.