<p>Black: Cultures without rotenone. Red: Cultures with rotenone. Open circles: Biomass concentration. Filled circles: Ethanol concentration. Open diamonds: Xylose concentration. (a): Xylose consumption and biomass production at <i>k</i><sub><i>L</i></sub><i>a</i> = 15 h<sup>−1</sup>. (b): Ethanol production at <i>k</i><sub><i>L</i></sub><i>a</i> = 15 h<sup>−1</sup>. (c): Xylose consumption and biomass production at <i>k</i><sub><i>L</i></sub><i>a</i> = 25 h<sup>−1</sup>. (d): Ethanol production at <i>k</i><sub><i>L</i></sub><i>a</i> = 25 h<sup>−1</sup>. Solid lines: Culture model. All experiences were repeated five times, error bars are shown.</p
<p>Fermentation experiments were performed using 2× YNB medium containing 20 g L<sup>−1</sup> glucos...
A) Strains were grown anaerobically in 9% ACSH, YPDX 9%/4.5%, YPDX 6%/3%, and YPDX 6%/3% + lignotoxi...
<p>(A) Growth of strains Z5, Z5Δ<i>GPD2</i> and SZ3-1 on different concentration of ethanol. Cells w...
1<p>D-xylose consumption (%) – percentage of initial D-xylose consumed.</p>2<p>Y<sub>p/s</sub><sup>e...
Production of bio-ethanol from lignocellulose requires the efficient fermentation of glucose and xyl...
Batch cultures of Y128, Y184, Y184 hog1Δ, and Y184 Bcy1-AiD were grown anaerobically for 92 hours in...
<p>Symbols: <i>open diamonds</i>, glucose; <i>closed diamonds</i>, xylose; <i>closed squares</i>, et...
Batch cultures were grown in YPDX 6%/3% for 96 hours. Measurements are averages from three biologica...
<p>(A) Mean expression of all genes of each of the 24 strains from our collection grown on xylulose,...
Ethanolic fermentation is a means of utilizing xylose-rich industrial wastes, but an optimized biopr...
<p>The initial sugar concentrations are 40 g/L cellobiose+40 g/L xylose (A) and 80 g/L cellobiose+40...
<p>Experimental and model simulated profiles of (A) cell growth, (B) xylose consumption and (C) etha...
A remaining challenge for the development of economically feasible 2nd generation bio-ethanol is low...
<p>By-product formation rates are calculated per hour and gram dry cell weight [mmol*g<sup>−1</sup>*...
<p>Time profiles for cell density (OD<sub>600</sub>), residual xylose, xylonate and xylonolactone co...
<p>Fermentation experiments were performed using 2× YNB medium containing 20 g L<sup>−1</sup> glucos...
A) Strains were grown anaerobically in 9% ACSH, YPDX 9%/4.5%, YPDX 6%/3%, and YPDX 6%/3% + lignotoxi...
<p>(A) Growth of strains Z5, Z5Δ<i>GPD2</i> and SZ3-1 on different concentration of ethanol. Cells w...
1<p>D-xylose consumption (%) – percentage of initial D-xylose consumed.</p>2<p>Y<sub>p/s</sub><sup>e...
Production of bio-ethanol from lignocellulose requires the efficient fermentation of glucose and xyl...
Batch cultures of Y128, Y184, Y184 hog1Δ, and Y184 Bcy1-AiD were grown anaerobically for 92 hours in...
<p>Symbols: <i>open diamonds</i>, glucose; <i>closed diamonds</i>, xylose; <i>closed squares</i>, et...
Batch cultures were grown in YPDX 6%/3% for 96 hours. Measurements are averages from three biologica...
<p>(A) Mean expression of all genes of each of the 24 strains from our collection grown on xylulose,...
Ethanolic fermentation is a means of utilizing xylose-rich industrial wastes, but an optimized biopr...
<p>The initial sugar concentrations are 40 g/L cellobiose+40 g/L xylose (A) and 80 g/L cellobiose+40...
<p>Experimental and model simulated profiles of (A) cell growth, (B) xylose consumption and (C) etha...
A remaining challenge for the development of economically feasible 2nd generation bio-ethanol is low...
<p>By-product formation rates are calculated per hour and gram dry cell weight [mmol*g<sup>−1</sup>*...
<p>Time profiles for cell density (OD<sub>600</sub>), residual xylose, xylonate and xylonolactone co...
<p>Fermentation experiments were performed using 2× YNB medium containing 20 g L<sup>−1</sup> glucos...
A) Strains were grown anaerobically in 9% ACSH, YPDX 9%/4.5%, YPDX 6%/3%, and YPDX 6%/3% + lignotoxi...
<p>(A) Growth of strains Z5, Z5Δ<i>GPD2</i> and SZ3-1 on different concentration of ethanol. Cells w...