Additional file 4: Figure S2. Time courses of low cell density shaken bottle fermentations with xylose or with glucose and xylose in a hydrolyzate matrix. Fermentations were performed in H-YX (a, b) and H-YGX (c, d) media using strains IBB10B05 (a, c) and KE6-12.A (b, d). The starting OD600 was 0.1. Data points are mean values from biological replicates. Error bars indicate the spread. Symbols: Xylose (filled squares), glucose (empty diamonds), ethanol (empty circles), glycerol (empty triangles), xylitol (filled triangles), and OD600 (crosses and dashed lines)
<p>(a) Growth comparison of QM 9414 to the Δ3405 strain on minimal media supplemented with D-glucose...
<p>Comparison of cell growth (A) and sugar consumption of genetically engineered <i>Saccharomyces ce...
Additional file 1: Figure S1. Growth and end-products formation of the strains MG01 (A) and MG02 (B)...
Additional file 2: Figure S1. Time courses of low cell density shaken bottle fermentations in comple...
Additional file 5: Table S3. Comparison of the physiological parameters of strains IBB10B05 and KE6-...
Additional file 3: Table S2. Comparison of the physiological parameters of strains IBB10B05 and KE6-...
Additional file 6: Figure S3. Comparison of the change in viability over time in high gravity SSCF f...
Additional file 5. Ethanol yield (%) for ancestral synthetic hybrids and evolved synthetic hybrids d...
<p>Symbols: <i>open diamonds</i>, glucose; <i>closed diamonds</i>, xylose; <i>closed squares</i>, et...
Additional file 13. Compound time course curves for engineered S. cerevisiae and wild Saccharomyces ...
Background: The most advanced strains of xylose-fermenting Saccharomyces cerevisiae still utilize xy...
Additional file 4: Figure S2. Microaerobic xylose fermentation by recombinant PP600 strains. S. cere...
Abstract Background The most advanced strains of xylose-fermenting Saccharomyces cerevisiae still ut...
Additional file 4. Plots of ln(OD660) values versus time in anaerobic bioreactor batch cultures of S...
<p>The initial sugar concentrations are 40 g/L cellobiose+40 g/L xylose (A) and 80 g/L cellobiose+40...
<p>(a) Growth comparison of QM 9414 to the Δ3405 strain on minimal media supplemented with D-glucose...
<p>Comparison of cell growth (A) and sugar consumption of genetically engineered <i>Saccharomyces ce...
Additional file 1: Figure S1. Growth and end-products formation of the strains MG01 (A) and MG02 (B)...
Additional file 2: Figure S1. Time courses of low cell density shaken bottle fermentations in comple...
Additional file 5: Table S3. Comparison of the physiological parameters of strains IBB10B05 and KE6-...
Additional file 3: Table S2. Comparison of the physiological parameters of strains IBB10B05 and KE6-...
Additional file 6: Figure S3. Comparison of the change in viability over time in high gravity SSCF f...
Additional file 5. Ethanol yield (%) for ancestral synthetic hybrids and evolved synthetic hybrids d...
<p>Symbols: <i>open diamonds</i>, glucose; <i>closed diamonds</i>, xylose; <i>closed squares</i>, et...
Additional file 13. Compound time course curves for engineered S. cerevisiae and wild Saccharomyces ...
Background: The most advanced strains of xylose-fermenting Saccharomyces cerevisiae still utilize xy...
Additional file 4: Figure S2. Microaerobic xylose fermentation by recombinant PP600 strains. S. cere...
Abstract Background The most advanced strains of xylose-fermenting Saccharomyces cerevisiae still ut...
Additional file 4. Plots of ln(OD660) values versus time in anaerobic bioreactor batch cultures of S...
<p>The initial sugar concentrations are 40 g/L cellobiose+40 g/L xylose (A) and 80 g/L cellobiose+40...
<p>(a) Growth comparison of QM 9414 to the Δ3405 strain on minimal media supplemented with D-glucose...
<p>Comparison of cell growth (A) and sugar consumption of genetically engineered <i>Saccharomyces ce...
Additional file 1: Figure S1. Growth and end-products formation of the strains MG01 (A) and MG02 (B)...