A comprehensive comparison of the main fermentation parameters, productivity, yield and final L-lactic acid concentration, obtained through batch, fed-batch and continuous cultivations using Lactobacillus casei CCDM 198 and a model cultivation medium was carried out. Using this data, a pulse-feed fed-batch process was established for testing chicken feather hydrolysate as a replacement for all complex nitrogen sources (yeast and beef extracts and peptone) in the medium. As comparably high values of productivity (about 4.0 g/L/h) and yield (about 98 %) were reached under all cultivation conditions, the maximum final L-lactic acid concentration (116.5 g/L), as achieved through pulse-feed fed-batch fermentation, was chosen as the most important criterion for process selection. Fed-batch cultivation with chicken feather hydrolysate as both a complex nitrogen source and a neutralizing agent for maintaining constant culture pH yielded half the concentration of L-lactic acid compared to the model medium. We demonstrate here that chicken feather hydrolysate has potential for use in the production of L-lactic acid but its utilization requires further optimization
Keywords:
Lactic acid; homofermentative fermentation; process design; Lactobacillus casei; chicken feather hydrolysate
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Cultivation conditions: 37 °C; stirring rate 300 rpm; constant pH 6.5; neutralizing agent - 20% NaOH or chicken feather hydrolysate for standard MRS and feather hydrolysate media, respectively. Composition of MRS medium for batch phase of the cultivation (in 1 L): 20 g glucose, 10 g/L peptone, 10 g beef extract, 5 g yeast extract, 1 mL Tween 80, 2 g dipotassium hydrogen phosphate, 5 g sodium acetate, 2 g ammonium citrate, 0.2 g magnesium sulphate heptahydrate, 0.2 g manganese sulphate monohydrate. Composition of feather hydrolysate medium (in 1 L): 20 g glucose, 450 mL chicken feather hydrolysate, 1 mL Tween 80, 2 g dipotassium hydrogen phosphate, 5 g sodium acetate, 2 g ammonium citrate, 0.2 g magnesium sulphate heptahydrate, 0.2 g manganese sulphate monohydrate. The arrow shows the start of feeding i.e. end of the batch phase.