Protein extraction using reversed micelles is carried out in a packed colum
n. The extracted fraction of lysozyme and the overall capacity coefficient,
K(c)a, are measured for various flow rates and different packing materials
. The same column without packings is also used as a spray column, By using
a flat interface stirred cell, mass transfer coefficients for the aqueous
and the organic phases are measured as well as the protein transfer rate, T
he results indicate that the resistance of protein solubilization at the in
terface controls protein transfer from the aqueous into the organic phase.
The extracted fraction in the packed column is about three times larger tha
n that for the spray column due to the larger holdup of dispersed phase in
the packed column. Since the drops hardly break or coalesce in the packed b
ed and the protein transfer coefficient is constant, the overall capacity c
oefficient is controlled by the holdup of dispersed phase. On the assumptio
n that the drop size and the transfer coefficient are constant, the correla
tion between holdup and now rates is obtained. Values of K(c)a and the extr
acted fraction are calculated from the holdup correlation. Effects of packi
ng materials on the values of K(c)a are small. A high protein activity is r
etained in the packed column operation, which indicates that the packed col
umn does little harm to proteins due to moderate mixing.