The dehydrogenation of butene-1 over a chromia-alumina catalyst has be
en used to study the distribution and concentration of the coke deposi
ted along a fixed bed reactor using different feed concentrations of b
utene-1. Axial temperature measurements showed a steep initial tempera
ture minimum followed by a subsequent shallower minimum. Corresponding
coke profiles were determined using a microbalance and confirmed by t
he non-invasive neutron attenuation technique. These together with det
erminations of exit gas concentrations suggest that coke is formed pri
marily from the reaction product butadiene, and that this coke deposit
limits further formation of this product and thus decreases further c
oke formation.