Wj. Choi et al., ENHANCED PRODUCTION OF CIS,CIS-MUCONATE IN A CELL-RECYCLE BIOREACTOR, Journal of fermentation and bioengineering, 84(1), 1997, pp. 70-76
For enhanced production of cis,cis-muconate via biocatalytic conversio
n from benzoate, a high cell density culture of a mutant Pseudomonas p
utida strain, BM014 in a cell-recycle bioreactor has been investigated
, The volumetric productivity in a continuous bioconversion process wa
s dependent on the biomass concentration, specific growth rate, and en
vironmental conditions including dissolved oxygen tension (DOT) and ci
s,cis-muconate concentration, Biotransformation was started ire a cell
-recycle continuous culture mode far obtaining a high cell density of
40 g/l and then carried out in a fed-batch mode for accumulation of ci
s,cis-muconate to up to 12 g/l at which induction of catechol 1,2-diox
ygenase, a key enzyme catalyzing the rate-determining step in the bios
ynthetic pathway, was maximized. Since in the biosynthesis of cis,cis-
muconate growing cells mere utilized as catalysts, cell growth should
be continued, but a low specific growth rate achieved under phosphate-
limited conditions was indispensable for higher productivity. When the
concentration of phosphate in the feed was lowered from 150 to 10 mM,
the productivity could be enhanced three fold, It was also found that
cobalt ions markedly increased the specific productivity and that DOT
should be kept at above 20% of the saturation level for achieving opt
imum rates of cell growth and product formation. After a period of fed
-batch operation continuous production with cell recycling was attempt
ed with phosphate-limited minimal medium supplemented with cobalt ions
, and benzoate medium. Enhanced productivity of 5.5 g/(l.h) and a cis,
cis-muconate concentration of 13.5 g/l in the culture broth were obtai
ned and continuous production in a cell-recycle bioreactor mas maintai
ned fur more than 7 d.