MOESM1 of Production of mannosylglycerate in Saccharomyces cerevisiae by metabolic engineering and bioprocess optimization

Additional file 1: Figure S1. Growth and end-products formation of the strains MG01 (A) and MG02 (B) cultivated in shake flask with SC medium containing 20 g L−1 of glucose. Data represent the mean of three independent experiments. Gly—glycerol; Acet—acetate; EtOH—ethanol. Table S1. MG and end-products production and yields for the engineered strains MG01 (mgsD) and MG02 (mgsD ↑pmi40 ↑psa1) cultivated in shake flask and batch fermenters. Data represent the mean ± SD of at least three independent experiments. Table S2. Physiological parameters and MG yields for the engineered strains MG01 (mgsD) and MG02 (mgsD ↑pmi40 ↑psa1) in chemostat cultivation at different dilution rates. Figure S2. Profile of glucose consumption, acetate, glycerol, ethanol and MG production from the beginning until steady-state for strains MG01 (A) and MG02 (B) cultivated in two independent chemostats (experiment 1 and 2) with dilution 0.1 h−1