Axial dispersion coefficients were measured in an aqueous phase flowin
g downward through a 5.08-cm-dia. Karr-type reciprocating plate column
. The steady tracer injection method was used, in which the concentrat
ion profile was measured upstream of tracer injection. The tracer solu
tion was a strong (150-170 g/L) solution of sodium chloride, whereby a
significant stable density gradient (density decreasing with height)
was created in the upstream section. The operating variables included
frequency (0 to 7.1 Hz), amplitude (0.7 to 1.4 cm), and plate spacing
(2.65 to 7.65 cm). Some data were also obtained under two-phase condit
ions with a refined kerosene (Isopar M) dispersed in the aqueous phase
as droplets. Some control experiments were done using a neutrally buo
yant tracer solution containing sodium chloride and methanol. There wa
s no evidence that the stable density gradient had any effect in reduc
ing the values of the axial dispersion coefficient although earlier pu
blished work had shown that an unstable density gradient did increase
axial mixing.