Additional file 3: Table S2. Physiological parameters of strain IBB14LA1_5 in glucose conversions under anaerobic and aerobic conditions
Additional file 5: Table S3. Comparison of the physiological parameters of strains IBB10B05 and KE6-...
Additional file 4: Figure S2. Fermentation profiles of XR-XDH-inserted and XI-inserted strains with ...
Additional file 1: Figure S1. Comparison of the volumetric concentrations of extracellular and intra...
Additional file 1: Table S1. Physiological parameters of strain IBB14LA1 in glucose and xylose conve...
Abstract Background Saccharomyces cerevisiae, engineered for l-lactic acid production from glucose a...
Additional file 4. Plots of ln(OD660) values versus time in anaerobic bioreactor batch cultures of S...
Additional file 3: Table S2. Comparison of the physiological parameters of strains IBB10B05 and KE6-...
Additional file 1: Figure S1. Growth and end-products formation of the strains MG01 (A) and MG02 (B)...
Additional file 1: Table S1. Fermentation products of E. coli MG1655 mutants in mineral medium with ...
Additional file 13. Compound time course curves for engineered S. cerevisiae and wild Saccharomyces ...
Additional file 1: Table S1. Kinetic constants (Km and Vmax) of Pdc enzymes, Figure S1. Batch cultiv...
Additional file 3: Figure S1. Fermentation profiles of XR-XDH-inserted and XI-inserted strains with ...
Additional file 1: Fig S1. Comparison of the ethanol and biomass production, and glucose consumption...
Economics of ethanol production from lignocellulosic biomass depends on complete utilization of cons...
Additional file 2. Organic acid production in anaerobic bioreactor batch and chemostat cultures of S...
Additional file 5: Table S3. Comparison of the physiological parameters of strains IBB10B05 and KE6-...
Additional file 4: Figure S2. Fermentation profiles of XR-XDH-inserted and XI-inserted strains with ...
Additional file 1: Figure S1. Comparison of the volumetric concentrations of extracellular and intra...
Additional file 1: Table S1. Physiological parameters of strain IBB14LA1 in glucose and xylose conve...
Abstract Background Saccharomyces cerevisiae, engineered for l-lactic acid production from glucose a...
Additional file 4. Plots of ln(OD660) values versus time in anaerobic bioreactor batch cultures of S...
Additional file 3: Table S2. Comparison of the physiological parameters of strains IBB10B05 and KE6-...
Additional file 1: Figure S1. Growth and end-products formation of the strains MG01 (A) and MG02 (B)...
Additional file 1: Table S1. Fermentation products of E. coli MG1655 mutants in mineral medium with ...
Additional file 13. Compound time course curves for engineered S. cerevisiae and wild Saccharomyces ...
Additional file 1: Table S1. Kinetic constants (Km and Vmax) of Pdc enzymes, Figure S1. Batch cultiv...
Additional file 3: Figure S1. Fermentation profiles of XR-XDH-inserted and XI-inserted strains with ...
Additional file 1: Fig S1. Comparison of the ethanol and biomass production, and glucose consumption...
Economics of ethanol production from lignocellulosic biomass depends on complete utilization of cons...
Additional file 2. Organic acid production in anaerobic bioreactor batch and chemostat cultures of S...
Additional file 5: Table S3. Comparison of the physiological parameters of strains IBB10B05 and KE6-...
Additional file 4: Figure S2. Fermentation profiles of XR-XDH-inserted and XI-inserted strains with ...
Additional file 1: Figure S1. Comparison of the volumetric concentrations of extracellular and intra...