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Fig. 5 | Bioresources and Bioprocessing

Fig. 5

From: α-Farnesene production from lipid by engineered Yarrowia lipolytica

Fig. 5

Optimization of pH, air flux and stirring rate for fermentation of strain F10 in a bioreactor. a Titer of α-farnesene and metabolite accumulation at different pH. b Growth curve at different pH during fermentation. c Titer of α-farnesene and metabolite accumulation at different air flux and stirring rate. d Growth curve at different air flux and stirring rate during fermentation. α-Farnesene and metabolites were detected after 96 h of fermentation in a 1-L bioreactor containing 800 mL YP medium with oleic acid. This experiment was performed with n  =  1

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