TABLE 2.
Activity | Concn obtained for R transformed with:
|
|||
---|---|---|---|---|
pVT100-U-ZEO
|
pVT100-U-ZEO-GPD1
|
|||
g/liter | mM | g/liter | mM | |
Consumption of: | ||||
Glucose | 187.5 | 1,041.7 | 196 | 1,088.9 |
Malate | 0 | 0 | 0.65 | 4.85 |
Production of: | ||||
Ethanol | 88.4 | 1,921.7 | 85.7 | 1,863.0 |
CO2 | 84.2 | 1,913.6 | 86.2 | 1,959.1 |
Glycerol | 7.4 | 80.4 | 16.5 | 179.3 |
Pyruvic acid | 0.12 | 1.4 | 0.21 | 2.4 |
Acetaldehyde | 0.01 | 0.23 | 0.04 | 1 |
Acetate | 0.42 | 7.1 | 1.18 | 19.7 |
Acetoin | 0 | 0.0 | 0.06 | 0.7 |
2,3-Butanediol | 0.24 | 2.7 | 1.92 | 21.3 |
Succinate | 0.4 | 3.4 | 1.11 | 9.4 |
Biomass formationb | 6.5 | 64.56 | 5.8 | 57.61 |
Carbon recovery | 100.8% | 101.1% | ||
Redox balancec | 101.8% | 101.7% |
Fermentation conditions were as described in the legend to Fig. 1.
The carbon-molar mass of biomass was estimated with the elemental composition (C4H7.32O2.24N0.68S0.006) previously used (47).
The redox balance represents the ratio between the reductance degree of fermentation products (including biomass) and the reductance degree of glucose, expressed as a percentage.