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Fig. 2 | Microbial Cell Factories

Fig. 2

From: Metabolic engineering of Corynebacterium crenatum for enhanced L-tyrosine production from mannitol and glucose

Fig. 2

Shake-flask fermentation parameters using glucose as a carbon source. (A) Cell growth and glucose consumption curves of CCGT03 in different concentrations of L-Phe. (B) L-Tyr production of CCGT03 in different concentrations of L-Phe. (C) Cell growth and L-Tyr following the modification of transporter proteins and accumulation of PEP. (D) Pyruvate production by different strains

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