The reaction network of n-butane selective oxidation
was comparatively analyzed over a novel αII-V0.8W0.2OPO4 orthophosphate and a reference
vanadyl pyrophosphate (VPP) based catalyst via parameter field studies
(T = 360–420 °C, x(n-butane) = 0.5–2.0%, x(O2) = 10–20%) as well as cofeed and pulse experiments with presumed
reaction intermediates. For VPP the selectivity to the target product
maleic anhydride (MAN) is particularly sensitive to the reaction temperature,
the n-butane concentration, and the amount of cofed
H2O, whereas the selectivity to MAN over the W-containing
catalyst is almost independent of all reaction parameters. The roles
of 1-butene, acetylene, furan, acetaldehyde, water, and 2,5-dihydrofuran
are discussed. Pulsing of possible C4 intermediates indicates that
their desorption from the catalyst surface is detrimental to MAN selectivity.
Ethylene and acetylene may be formed from MAN. The consecutive reaction
of acetylene with H2O can lead to acetic acid, whereas
all other byproducts are predominantly formed directly from n-butane. The pronounced stability of both samples was confirmed
by repeated catalyst performance test under reference conditions,
XRD, and SEM. Mass and heat transport limitations were experimentally
excluded. A formal kinetic model including n-butane,
MAN, CO, CO2, acetic acid, and acrylic acid was developed,
in which the acids were found to be less relevant on the V0.8W0.2OPO4 catalyst. However, the main reaction
pathways were found to be similar over both catalysts, which differ
mainly in product selectivities.