Experimental data from Hydrowax cracking using the microriser equipment hav
e been used to develop a kinetic model that adequately describes the experi
mental data from 0.05 to 5 s residence time. To account for different time
scales of the reactions, different activity functions were used for coke fo
rmation and for conversion to the other products. The activity for coke for
mation was described by an exponentially decreasing function of the residen
ce time with a very short characteristic time of 0.02 s. The activity for f
ormation of the other products was also described by an exponentially decre
asing function, in this case of the coke content of the catalyst.
The model was used to predict the residual activity of the catalyst in a se
cond experiment with fresh Hydrowax feedstock. Using the assumption that in
the second run no further deactivation of the catalyst took place, the mod
el predictions agreed well with the experimental data.
The applicability of the model to data from other feedstocks, a hydrotreate
d flashed distillate and a vacuum gas oil, was successfully demonstrated.