In order to obtain casein peptides at higher productivity, a filtratio
n membrane automatic bioreactor has been developed. Total solid concen
tration of reaction solution in a reaction vessel was controlled autom
atically by adding substrate and deionized water to it. As the results
, it was possible to operate for 24 hours with a constant permeate Bur
. However, when operated during 80 hours under the concentration ratio
of substrate to enzyme : 5.0%/1.0% at an operation pressure of 150 kP
a, the lowering of 8.1% of permeate flux was finally Pound. In general
, permeate flux decreased with an increase in substrate concentration
and increased with an increase in operation pressure. Total membrane r
esistance, R (m(-1)) was represented by the following equation, R=4.47
+0.15 C, where 4.47 was membrane resistance of itself and C was total
solid concentration (%) of the reaction solution at 45 degrees C, Thes
e results suggested that the decrease in enzyme activity and the accum
ulation of peptide which could not be further hydrolyzed and the incre
ase in membrane resistance reduced the permeate flux after long operat
ion period of up to 80 hours.