Regeneration kinetics of a cracking catalyst was studied by temperature pro
grammed oxidation (TPO) in a microreactor system. The CO and CO2 responses
were detected as a function of time while heating the sample at a constant
rate. Different oxygen concentrations (0.5-2.0%) and heating rates (5 and 1
0 K/min) were applied. Three kinetic models were tested and the parameters
were estimated by non-linear regression. The models were capable of describ
ing the experimental data adequately and the parameters were physically acc
eptable. (C) 2001 Elsevier Science Ltd. All rights reserved.