The reactive extraction of Cephalosporin C ester directly from the fer
mentation broth of Cephalosporin C was studied in Liquid-Liquid two ph
ase system using ethyl acetate. When the volumetric fraction rate of e
thyl acetate phase was 0.33 or more, the effect of agitation was not o
bserved on the reaction rate. On the other hand, the effectiveness of
agitation appeared at the ratio 0.17 or less. It was clarified that th
e rate determining step of this reactive extraction was mass transfer
to reaction interface by a series of experimental results. An excellen
t correlation was also obtained between the scale-up factor(Z), showin
g power consumption ratio of agitation, and the over all mass transfer
coefficient at the volumetric fraction ratio oi 0.17.