The vapour-phase Beckmann rearrangement has been studied using a boron
-MFI zeolite. The multitude of papers concerning this reaction state t
he maximum yield of epsilon-caprolactam at a temperature of 350 degree
s C and ambient pressure. Investigation of different process parameter
s showed that decreasing the pressure in addition to reducing the temp
erature to 300 degrees C leads to an improvement in caprolactam select
ivity. This resulted in a drop in catalyst lifetime. In order to reduc
e deactivation, the addition of water to the reaction is useful. Contr
ary to former papers, it was shown that the deactivation rate decrease
d with a raising amount of added water up to 6 mol water per mol cyclo
hexanone oxime. The conversion was slightly increased with no consider
able effect on the selectivity. Due to the short catalyst service time
, a regeneration of deactivated catalysts is inevitable. Using air or
oxygen as a regenerating agent, it is possible to regain complete acti
vity and selectivity. Nitrogen can also be used as a regeneration gas,
although a slight drop in activity must be accepted. For industrial a
pplication, a continuous reaction-regeneration system should be employ
ed when using fluidized bed reactors. Therefore, the reaction was stud
ied in a fluidized bed reactor of laboratory scale. The yields achieve
d in this apparatus were in good agreement with the results obtained i
n a fixed bed reactor.