A cracking catalyst designated SRNY was manufactured from a commercial
SRNY molecular sieve (M.S.). The support consisted of kaolin, clay an
d SiO2. The coking behaviour of the SRNY M.S., the support and the cat
alyst were examined with light diesel oil (LDO) as feedstock in a micr
oreactor. The physico-chemical properties of both fresh and aged sampl
es, subjected to or not subjected to the cracking reaction of LDO, wer
e sequentially characterized by means of pore structure determination
and thermal analysis. The pore structure included the specific surface
area and the pore volume or porosity. Thermal analysis methods used i
ncluded TG and DSC. The results indicated that all coked samples exhib
ited obvious changes in surface pore structure and acidity in comparis
on with non-coked samples. Their specific surface area and acid amount
decreased with increase in the coke content of the samples. The appar
ent activation energy data obtained from decoking samples in an air fl
ow, using the temperature-programmed oxidation (TPO) method, showed th
at the kinetic parameters of the SRNY M.S. differed from those of the
SRNY catalyst and its support.