The effects of steam, fed to the riser section of a laboratory recircu
lating solids reactor, on butane oxidation over a vanadyl pyrophosphat
e catalyst are reported. Gas fed to the riser was either butane in ine
rt or butane co-fed with oxygen in inert. The catalyst regenerator-ves
sel was fluidized with air in all cases. It was observed that steam ad
ded to the riser competes for sites required for gas-phase oxygen acti
vation, while catalyst lattice oxygen utilization is not affected. The
competition for sites with oxygen causes a decrease in butane convers
ion and a corresponding increase in selectivity to maleic anhydride. T
he improvement in selectivity is more pronounced under anaerobic condi
tions, and an explanation for this result is offered. This study demon
strates the opportunity offered by a recirculating solids reactor to s
tudy various aspects of selective oxidation catalysis independent of t
he complicating effects of simultaneous catalyst reduction and oxidati
on reactions.