The partial oxidation of isobutene to methacrolein and methacrylic aci
d was studied on oxidic catalysts containing mainly a mixture of bismu
th tungstate and iron-cobalt-potassium molybdate. Catalyst shaping was
done by extrusion. The kinetic measurements were performed by monitor
ing the gas-phase composition along the length of a fixed bed of catal
yst. The reactor was treated as an isothermal plug-flow system. The ne
twork of parallel and consecutive reactions taking place in this syste
m can be described by a simplified scheme. It is possible to predict t
he gas-phase composition prevailing in the reactor using five differen
t kinetic parameters. In the temperature range 380 < theta < 420 degre
es C grain selectivities as high as 85% combined with yields of methac
rolein and methacrylic acid about 72% at 92% conversion were obtained.