FCC cracking operations that process resid-type feedstocks are often faced
with the dilemma of managing significant levels of contaminant metals on th
eir FCC catalyst inventory. Ni and V are of primary concern because of the
ability of these metals to impair catalyst activity and to negatively impac
t catalyst yields. Typical practices for higher metals operations have incl
uded the use of equilibrium catalyst to "flush" contaminant metals from the
unit, while adding minimal fresh catalyst just to maintain activity. This
approach forces the unit to operate at a metal level that is often lower th
an the optimum, to counteract the contaminant metals brought in with the eq
uilibrium catalyst and the potential negative yields associated with them.
Modem catalysts, which incorporate metal tolerant technologies that minimiz
e the effects of Ni and V, can be used to improve the overall selectivity o
f a particular unit's inventory. Fresh catalyst addition rates of these new
technologies can often be much lower than the combined addition of "flushi
ng" catalyst and fresh catalyst, with improvements in yields. This paper wi
ll examine the differences between these methods of catalyst management.