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Fig. 2 | Biotechnology for Biofuels

Fig. 2

From: Dynamic simulation of continuous mixed sugar fermentation with increasing cell retention time for lactic acid production using Enterococcus mundtii QU 25

Fig. 2

Tested and simulated systems with key model parameters; a batch reactor; b continuous flow; and c continuous flow with cell recycling (dilution ratio (D) is the inverse of cell retention time). Controlled parameters described the experimental design; growth kinetics is given after references or model validation; outputs are simulated data

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