Abstract
The paper is concerned with the dispersion of a solute in a Bingham plastic fluid flowing in a pipe or a parallel plate channel. For pipe flow, the dispersion coefficient K 2 first increases with ξ0 (the dimensionless radius of the plug flow region), reaches a maximum and then decreases. But in a channel flow, K 2 decreases monotonically with increasing ξ0. Further K 2 for channel flow is found to be larger than that for pipe flow for all values of ξ0 except 0.8≤ξ0≤1.