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Table 3 Growth parameters with xylose as carbon source

From: Simultaneously improving xylose fermentation and tolerance to lignocellulosic inhibitors through evolutionary engineering of recombinant Saccharomyces cerevisiaeharbouring xylose isomerase

Parameter

No liquor

Supplemented with liquor

 

D5A+

D5A+

D5A+H

TMB3400

μmax (h-1)

0.37 ± 0.002

N/D

0.12 ± 0.01

0.14 ± 0.01

Biomass† (g/L)

2.08 ± 0.01

N/D

0.82 ± 0.1

0.84 ± 0.01

Ethanol† (g/L)

N/D

N/D

1.54 ± 0.14

N/D

Glycerol† (g/L)

0.15 ± 0.01

N/D

2.7 ± 0.27

0.19 ± 0.05

Yx/s‡ (g/g)

0.55 ± 0.023

N/D

0.07 ± 0.001

0.51 ± 0.06

Yp/s§ (g/g)

N/D

N/D

0.06 ± 0.001

N/D

Yp/x¶ (g/g)

N/D

N/D

1.9 ± 0.03

N/D

qs* (g/gh)

0.17 ± 0.003

N/D

2.08 ± 0.05

0.23 ± 0.02

qp†† (g/gh)

N/D

N/D

0.02 ± 0.003

N/D

  1. Yield coefficients and specific rates of growth, substrate consumption and ethanol production for strains D5A+, D5A+H and TMB3400 with 20 g xylose/L as primary carbon source in batch culture with and without with 50% (v/v) hydrolysate liquor from steam-pretreated triticale. Standard deviations from duplicate fermentations are shown.
  2. N/D None detected.
  3. †Biomass and product concentrations at the end of the exponential growth phase.
  4. ‡Yx/s, biomass yield on xylose, calculated from the slope of the biomass concentration plotted as a function of the residual xylose concentration.
  5. §Yp/s, ethanol yield on xylose, calculated from the slope of the ethanol concentration plotted as a function of the residual xylose concentration.
  6. ¶Yp/x, ethanol yield on biomass, calculated from the slope of the ethanol concentration plotted as a function of the biomass concentration.
  7. *qs, specific rate of substrate utilisation in g xylose/g biomass per hour during the mid-exponential phase.
  8. ††qp, specific rate of product formation in g ethanol/g biomass per hour during the mid-exponential phase.