In order to study the difference between catalytic and non-catalytic oxidat
ive cracking of n-butane, the oxidative cracking over various silica was in
vestigated in the temperature range of 600-700 degrees C. The reactions wer
e conducted with molecular oxygen, nitrogen, and n-butane using a fixed bed
reactor loaded with various silica packings. Homogeneous radical reaction
in the gas phase proceeded farther in an empty silica tube reactor and the
highest conversion of n-butane was attained. With the loading of various si
lica packings, the conversion of n-butane was lowered; however, the convers
ion obtained using amorphous silica was quite different from that obtained
using crystalline silica such as quartz sand or silicalite. The radical rea
ction was not suppressed so much by amorphous silica packing as by crystall
ine silica packing, and the n-butane conversion was as high as that in the
empty tube reactor without silica packing. It was considered that the surfa
ce OH groups on the amorphous silica are involved in the radical chain reac
tions of the oxidative cracking. Ethylene, propylene, and butenes were obta
ined as major products and the selectivity of light olefins was high (700 d
egrees C, about 75% at 45% conversion) compared with that obtained using ot
her oxides.