Using asymptotic expansion and numerical analysis, we demonstrate how
the step-response ignition time of an automobile catalytic converter d
epends on the ratio of the reaction rate to the interphase heat-transf
er rate, as measured by a key Damkohler parameter chi and the degree o
f monolith subcooling eta. In the region of low reaction rate at small
chi, the normalized ignition time t(ig) scaled by the homogeneous ign
ition time t(ig)(infinity) from the inlet gas temperature is (t(ig)/t(
ig)(infinity)) = 1 + 2 chi(1/2)\ln(chi(1/2)/2 eta)\(1/2), and the igni
tion takes place at a thermal front deep in the monolith. At large chi
when the reaction rate is high, ignition occurs at the leading edge o
f the monolith with (t(ig)/t(ig)(infinity))= 2.50 + chi(ln eta - 0.34)
. The delay in ignition time with increasing chi is due to a Taylor-Ar
is dispersion mechanism induced by interphase heat transfer. Although
the small-chi ignition mechanism is faster, its downstream ignition lo
cation leads to a very slow upstream propagation of the thermal front
that follows ignition. An optimal converter system that ignites in 13
s, 25% of the current value in a. standard step-response test, is then
designed by placing a small igniter, which ignites by the small-chi m
echanism, upstream to preheat the current converter which then ignites
by the large-chi mechanism. The length of the igniter is kept small b
y bypassing 2/3 of the exhaust since, from our theory, t(ig)(infinity)
is independent of the gas velocity.