The unsteady dispersion of a solute in a Casson fluid flowing in a conduit
(pipe/channel) is studied using the generalized dispersion model of Gill an
d Sankarasubramanian. With this approach, the entire dispersion process is
described appropriately in terms of a simple diffusion process with the eff
ective diffusion coefficient as a function of time, in addition to its depe
ndence on the yield stress of the fluid. The results are accurate up to a f
irst approximation for small times, but verified with Sharp to be exact for
large rimes. The model brings out mainly the effect of yield stress, or eq
uivalently, the plug Row region on the overall dispersion process. It is fo
und that the rate of dispersion is reduced (i.e., the effective diffusivity
decreases) due to the yield stress of the fluid, or equivalently, the plug
flow region in the conduit. Also, the effective diffusivity increases with
time, bur eventually attains its steady state value below a critical time
[0.48(a(2)/D-m) for dispersion in a pipe and 0.55(a(2)/D-m) for dispersion
in a channel-the critical transient time for a Newtonian fluid-where ''a" i
s the radius of the pipe and D-m is the molecular diffusivity]. At steady s
tate, for dispersion in a pipe with the plug Row radius one tenth of the ra
dius of the pipe, the effective diffusivity is reduced to about 0.78 times
of the corresponding value for a Newtonian fluid at equivalent flow rates;
for dispersion in a channel, the reduction factor is about 0.73 confirming
the earlier result of Sharp. Further, the location of the center of mass of
a passive species over a cross section is found to remain unperturbed duri
ng the course of dispersion and for different values of the plug flow param
eter (i.e., the yield stress of the fluid). The study can be used as a star
ting first approximate solution for studying the dispersion in the cardiova
scular system or blood oxygenators. (C) 2000 Biomedical Engineering Society
.