The conversion of C-3-C-9 paraffins to small olefins over ZSM-5 zeolit
e is investigated. The small olefins are primary products and are usua
lly converted into other more stable secondary products such as aromat
ics on the ZSM-5 zeolites. Thermally treated HZSM-5, K/HZSM-5 and Ba/H
ZSM-5 catalysts were developed and favourable oxidative conditions wer
e introduced for the conversion process to maximize selective conversi
on of light paraffins to small olefins at the relatively low temperatu
re of 873 K. The role of K and Pa is to minimize bimolecular hydrogen
transfer reactions and enhance the dehydrogenation activity of the cat
alysts. Meanwhile, the oxygen in the gas phase is effective to improve
the olefin selectivity and yield. C-2-C-4 olefin selectivities of 70.
4 and 66.8% have been obtained for propane and n-hexane feedstocks, re
spectively, at a temperature of 873 K.