The state of mixing in a continuous flow vessel is shown to affect the
extent of aggregation and the extent of aggregation at which mathemat
ical gelation occurs. Three aspects of the state of mixing in vessels
where aggregation alone occurs are considered: the degree of segregati
on, the residence-time distribution (RTD) and the earliness or latenes
s of mixing. The effect of the stare of mixing is different for each k
ernel and depends primarily on the order of the moment rate law for th
e zeroth and sixth moments. For example, the sum kernel has a first-or
der decay moment rate law for its zeroth moment and is not affected ei
ther by the degree of segregation or the earliness or lateness of mixi
ng. On the other hand, the product kernel (omega = 1) has a second-ord
er growth moment rate law for its sixth moment and its gelling behavio
ur is strongly affected by the degree of segregation and the earliness
or lateness of mixing. Our results follow directly from an analogy wi
th reaction engineering based on the formal equivalence of our moment
rate law for aggregating systems and a well-known reaction rate law. W
e show the following striking progression of the dependence of the gel
ling behaviour of the sum kernel on the RTD: it is a non-gelling kerne
l in a plug flow vessel, a gelling kernel in a well-mixed vessel and a
n instantaneously gelling kernel when a vessel contains a partially st
agnant zone. We propose that these observations be used for predicting
the effects of scale-up and also of departures from ideal mixing. For
gelling kernels, any deviation from the ideal case of plug flow alway
s leads to a reduction in the extent of aggregation at which mathemati
cal gelation occurs. Finally, we recommend that batch experiments be u
sed to obtain aggregation rate data because of the difficulty of inter
preting unambiguously the data from continuous flow vessels where the
state of mixing is not well defined.