Simulation of foam separation has been reported usually for two-component s
ystems. In this paper, a mathematical model is developed to describe the pr
ocess of foam separation of tributyl phosphate (TBP) from aqueous solutions
using sodium dodecyl sulphate (SDS) as surfactant. The model assumed that
the bubbles are uniform in size and have regular dodecahedral structure. Th
e solution in the liquid pool has uniform concentration and the enrichment
is completed in the course of film drainage. The model is calculated under
different operating parameters. The calculated results show that by decreas
ing the bubble size and equilibrium height or by increasing the foam height
and equilibrium coefficient will improve the foam separation efficiency. I
f the operating parameters can be controlled by just increase the gas how r
ate, the recovery concentration of TBP will not be influenced. (C) 2000 Els
evier Science B.V. All rights reserved.