Fig. 2From: Dynamic simulation of continuous mixed sugar fermentation with increasing cell retention time for lactic acid production using Enterococcus mundtii QU 25Tested 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 dataBack to article page