Reliable estimates of catalyst deactivation parameters are difficult t
o get from conventional experiments at constant space velocity where c
onversion declines with time on stream, or when temperature is adjuste
d to compensate for the loss of catalyst activity. An alternate techni
que, where space velocity is adjusted to maintain constant conversion,
is shown here to give reliable rate information for both the catalyst
deactivation and the primary catalytic reactions. This technique, at
constant temperature, provides kinetics data on a deactivating catalys
t in which the catalyst is exposed to reactant and product concentrati
ons that are relatively constant. In principle, the kinetics of deacti
vation are obtained directly as the kinetic regime remains unchanged.
This technique is used quite successfully for many catalytic processes
of industrial significance. In this paper, the variable-space-velocit
y experimental technique is demonstrated for the methanol to hydro car
bons process on a ZSM-5 catalyst. The deactivation kinetic parameters
were determined at several temperatures in a fixed-bed reactor. This r
ate information was then used to determine the temperature-time policy
for maintaining constant reactor outlet conversion at a fixed space-v
elocity. The predicted temperature-time policies are in good agreement
with experimental data on fixed-bed and fluid-bed reactors. Mathemati
cal analysis of interpreting experimental data. as well as predicted t
emperature-time policies for practical applications, is illustrated. (
C) 1997 Elsevier Science Ltd.