Fig. 4From: High-titer production of 13R-manoyl oxide in metabolically engineered Saccharomyces cerevisiae13R-MO and GGOH production by the strain LZJ7 in shake flasks with various glucose concentrations. YPD media containing 30 g/L, 40 g/L, 60 g/L, and 80 g/L of glucose were used for fermentation. Three independent experiments were performed, and the error bars represent their standard deviationBack to article page