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Continuous succinic acid fermentation by Actinobacillus succinogenes
Affiliation:1. Research Centre for Sustainable Process Technology (CESPRO), Faculty of Engineering and Built Environment, Universiti Kebangsaan Malaysia, 43600 UKM Bangi, Selangor, Malaysia;2. Faculty of Chemical Engineering, Universiti Teknologi MARA, 40450 Shah Alam, Selangor, Malaysia;3. Chemical Engineering Discipline, School of Engineering, Monash University, 47500 Bandar Sunway, Selangor, Malaysia;1. DSM Biotechnology Center, Alexander Fleminglaan 1, 2613 AX Delft, The Netherlands;2. Department of Biotechnology, Delft University of Technology, Julianalaan 67, 2628 BC Delft, The Netherlands
Abstract:Fermentations were performed in an external recycle bioreactor using CO2 and d-glucose at feed concentrations of 20 and 40 g L−1. Severe biofilm formation prevented kinetic analysis of suspended cell (‘chemostat’) fermentation, while perlite packing enhanced the volumetric productivity by increasing the amount of immobilised cells. The highest productivity of 6.35 g L−1 h−1 was achieved at a dilution rate of 0.56 h−1. A constant succinic acid yield of 0.69 ± 0.02 g/(g of glucose consumed) was obtained and found to be independent of the dilution rate, transient state and extent of biofilm build-up – approximately 56% of the carbon that formed phosphoenolpyruvate ended up as succinate. Byproduct analysis indicated that pyruvate oxidation proceeded solely via the formate-lyase pathway. Cell growth and corresponding biofilm formation were rapid at dilution rates higher than 0.35 h−1 when the product concentrations were low (succinic acid < 10 g L−1), while minimal growth was observed at succinic acid concentrations above this threshold.
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