Cc. Chang et al., RECOMBINANT BIOPROCESS OPTIMIZATION FOR HETEROLOGOUS PROTEIN-PRODUCTION USING 2-STAGE, CYCLIC FED-BATCH CULTURE, Applied microbiology and biotechnology, 49(5), 1998, pp. 531-537
A two-stage, cyclic fed-batch bioprocess was designed, and its perform
ance evaluated to improve rice a-amylase productivity by the yeast Yar
rowia lipolytica SMY2 (MatA, ade1, ura3, xpr2), ATCC 201847, containin
g a replicative plasmid coding for a rice alpha-amlyase. Transcription
of the recombinant gene is controlled by the XPR2 promoter. The first
stage (or growth stage) was operated in the fed-batch mode, and the g
rowth medium, designed to maintain a constant high cell density (i.e.,
60 g/l), was fed according to a predetermined and preprogrammed optim
al feed rate which, in turn, maintained the specific cell growth rate
at an optimal value (i.e., 0.1 h(-1)). Typically, when the volume in t
he first stage reached a preset value, a portion of culture broth (i.e
., 55%) was transferred to the second stage (or production stage). The
remaining cells in the growth stage were then fed with fresh growth m
edium according to the bioprocess control strategy developed, while in
duction of alpha-amylase expression and its production was taking plac
e in the second stage. The second stage was also operated in the fed-b
atch mode, and the production medium designed to maintain a constant h
igh cell density and high productivity of heterologous protein was fed
at a predetermined and preprogrammed rate, which maintained the speci
fic cell growth rate at an optimal level. The volumetric alpha-amylase
productivity achieved (1835 units l(-1) h(-1)) from the two-stage, cy
clic fed-batch culture process was twofold higher than that of the fed
-batch culture process. The genetic stability of the recombinant strai
n and the design of optimal media for growth and production stages are
also critically important to a successful implementation of the two-s
tage, cyclic fed-batch process for production of heterologous protein.