Previous and present studies demonstrate that the new thin-film extractor w
ith the gravity settler have superior performance over other conventional d
evices. This is because the volume of the extractor and the settler are sig
nificantly reduced, on the average, by factors of 100 and 10, respectively,
for a similar power input. Correlations for a water-iodine-kerosene liquid
system developed in the past (Berman and Tamir, 2000) for the mass transfe
r and pressure drop were modified by incorporating the ratio R/R, This rati
o takes into account the impact of the liquids on the walls of the reactor
where R is the radius of the free film and R,is the radius of the reactor.
In addition, an equation was proposed, which demonstrates the dependence of
the extraction efficiency on the operating parameters. The gravity settler
combined with the thin-film extractor was tested thoroughly yielding two c
orrelations for estimating its height, i.e. the fluidized-bed and dense-pac
ked zones. In the present case the sedimentation zone is absent. A scale up
procedure based on the model developed is proposed as well as a principle
scheme of a pilot plant based on the new effective combination.