High yield lactic acid production using mixed cultures
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[0045]Materials and Methods
[0046]Reactor Operation
[0047]The enrichment was carried out in a 3 L bioreactor with a working volume of 2 L. Anaerobic conditions were maintained by continuously sparging the reactor with N2 at a rate of 216 mL min-1 (@T=273K, P=105 kPa). The culture was taken out of the reactor for biofilm removal from reactor walls and head three times per week. The reactor was continuously agitated at a speed of 300 rpm using mechanical stirrers. Reactor temperature was maintained at 30□C by recirculating water heated at 31° C. (E300 thermostat, Lauda, Germany) in the outer wall of the reactor. To prevent culture broth evaporation, the off-gas was cooled using a cryostat set to 5° C. Reactor pH was maintained at 5.0±0.2 using 8 mol L−1 NaOH and 1 mol L−1 HCl solutions (ADI 1030 Bio controller, Applikon, The Netherlands). To prevent excessive foaming, anti-foaming agent (3% v:v anti-foam C, Sigma Aldrich, Germany) was added in equal amounts and at equal speed as NaOH du...
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