Reaction kinetics of the gas-phase
Beckmann rearrangement of cyclohexanone
oxime to ε-caprolactam was studied over a NbO
x
/SiO2 catalyst in a fixed-bed reactor. Kinetic measurements
were carried out by variation of cyclohexanone oxime partial pressure
and reactor temperature in the range of 5 to 80 hPa and 360 to 420
°C, respectively. It was found that ethanol, used as solvent
in addition to toluene, is essential for high catalytic performance.
Reaction rates as a function of cyclohexanone oxime partial pressure
display Langmuir-type behavior, but the results could not be interpreted
satisfactorily on the basis of a Langmuir–Hinshelwood mechanism.
Another kinetic scheme is proposed, involving a kinetic adsorption
step for cyclohexanone oxime instead of an adsorption equilibrium.
Activation energies for the adsorption step and for the Beckmann rearrangement
reaction were found to be 154 and 68 kJ·mol–1, respectively. Substitution of ethanol by alcohols with longer chain
length (e.g., n-hexanol) resulted in significantly
higher ε-caprolactam selectivities.