The effect of multipass arrangement on membrane extraction through a cross-
flow rectangular module has been investigated both theoretically and experi
mentally. In contrast to a single-pass device, improvement in mass transfer
is obtained if cross-flow membrane extraction is operated in a multipass d
evice of same configuration. It is concluded that multipass effect which pr
ovides the increase of fluid velocity, can enhance mass transfer, especiall
y for concentrated solution with high distribution coefficient where the li
quid-phase mass-transfer resistances are more extremely predominant. (C) 20
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