Abstract
A continuous fermentation process for 2-keto-gluconic acid (2KGA) production from cheap raw material corn starch hydrolysate was developed using the strain Pseudomonas fluorescens AR4. The dilution rate and feeding glucose concentration had a significant effect on the cell concentrations, glucose utilization and 2KGA production performance. The optimal operating factors were obtained as: 0.065h−1 of dilution rate, 180g/L of feeding glucose concentration, and 16h of batch fermentation time as the starting point. Under these conditions, the steady state had the 135.92g/L of produced 2KGA concentration, 8.83g/L.h of average volumetric productivity, and 0.9510g/g of yield. In conclusion, the proposed efficient and stable continuous fermentation process for 2KGA production by the strain P. fluorescens AR4 is potentially competitive for industrial production from corn starch hydrolysate in terms of 2KGA productivity and yield.
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