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A substrate feeding strategy using an oxystat was first successfully applied to a fed-batch phenylalanine fermentation. The control method allowed the fermentation to be under low dissolved oxygen tension, which was favourable phenylalanine formation, and to be from substrate inhibition during the course of fed-batch operation. The final product concentration was 3 times higher than in a batch culture.

By screening 15,000 mutants, tyrosine auxotrophs T6, T7, and tryptophan auxotrophs P6, P8, were obtained. After primary production test, mutant P6 was chosen for further investigation. Fractional factorial design(FFD) and steepest ascent method(SAM) were used to optimize the medium component Mutant P6 had 17.1 g/l L-phenylalanine production when 0.44 g/l tryptophan was added. When Corynebacterium glutamicum P6 was cultivated in the optimum medium, L-phenylaianine production increased 22% as compared with the parent strain CCRC 18335, and the interference of tryptophan during the purification process was removed.

ThelysC gene encoding aspartokinase of a lysine-hyperproducing mutantBrevibacterium flavum CCRC 18271 was cloned by polymerase chain reaction and its expression in CCRC 18271 was studied. Enzyme assays showed thatB. flavum cells harbouring thelysC gene exhibited 4- to 11-fold higher specific activities of aspartokinase as compared to respective hosts. Introduction of thelysC gene intoB. flavum CCRC 18271 resulted in increased lysine production up to 33% in flask fermentations.

The aro gene of Corynebacterium glutamucum CCRC 18310 encoding 3-deoxy- D -arabinoheptulosonate-7-phosphate (DAHP) synthase was isolated by complementation of a DAHP synthase-deficient mutant of Escherichia coli AB3257. The specific activity of DAHP synthase was increased four-fold in a C. glutamicum strain harboring the cloned aro gene. The complete nucleotide sequence of the aro gene and 5′ and 3′ flanking regions has been determined. The sequence contained an open reading frame of 368 codons, from which a protein with a molecular mass of 39 340 Da could be predicted. The deduced amino acid sequence shows high identity with the aro gene products of E. coli and Salmonella typhimurium .

Production feedback inhibition both on cell growth and on product formation of phenylalanine fermentation might be alleviated by elevated oxygen supply. Batch fermentations by a high phenylalanine producing strain Corynebacterium glutamicum CCRC 18335 at various initial phenylalanine concentrations (P(0)) ranging from 0 to 20 g/L and different oxygen transfer rate coefficients (K(L)a) ranging from 23 to 76 h(-1) were studied. The fermentation parameters with respect to P(0) were strongly dependent on K(L)a. Cell yield favored higher K(L)a and lower P(0). Product yield with respect to varying phenylalanine concentration was evaluated by the relative oxygen availability (ROA). The optimal ROA for phenylalanine formation was strongly dependent on the product concentration. While P(0) was low, the product inhibition was less significant and the maximum product yield occurred while ROA was at 0.5-0.6. While P(0) was high, the product inhibition was significant and the maximum product yield occurred while ROA was at 0.8-0.9. These results suggest that the product feedback inhibition of phenylalanine fermentation processes can be alleviated by a gradual increase in oxygen supply rate while the increasing product concentration is taken into account. The strategy is demonstrated in a fed-batch culture with elevated oxygen supply. The final phenylalanine concentration was 23.2 g/L, which was 45% better than that of the fed-batch fermentation without elevated oxygen supply. Likewise, the maximum productivity was improved by 42% at 0.37 g/(L x h).