Strains | Strain description | Conditions | Xylose consumption rate (g/g−1 h−1) | Ethanol production rate (g/g−1 h−1) | Ethanol yield (g/g−1) | Reference |
---|---|---|---|---|---|---|
SXA-R2P-E | xylA*3, tal1, XKS1, Δgre3, Δpho13 Evolved (24 days) | Anaerobic batch in bioreactor, synthetic medium (40 g/L xylose) | 0.98 | 0.44 | 0.45 | This study |
H131-A3-CS | xylA, xyl3, TAL1, TKL1, RPE1, RKI1, evolved (160 days) | Anaerobic batch in bioreactor, syntheticmedium (40 g/L xylose) | 0.94 | 0.40 | 0.43 | [16] |
H131-A3-ALCS | xylA, xyl3, TAL1, TKL1, RPE1, RKI1, evolved (160 days) | Anaerobic batch in bioreactor, synthetic medium (40 g/L xylose) | 1.87 | 0. 77 | 0.41 | [16] |
CEN.PK- RWB218 | xylA, XKS1, TKL1, RPE1, RKI1, Δgre3, evolved (70 days) | Anaerobic batch in bioreactor, synthetic medium (20 g/L xylose) | - | 0.49 (projected) | 0.41 | [17] |
SR8 | Xyl1, xyl2, xyl3, Δald6, Evolved (no detailed information) | Anaerobic batch in flasks, synthetic medium (40 g/L xylose) | 0.65 | 0.25 | 0.39 | [24] |
CEN.PK2-1C -TMB 3424 | Xyl1, xyl2, XKS1, GAL2, TKL1, RPE1, RKI1, Δgre3 Selected (70 days) | Anaerobic batch in bioreactor, synthetic medium (60 g/L xylose) | 0.89 | 0.32 | 0.36 | [6] |
SR8 | Xyl1, xyl2, xyl3, Δald6, Evolved (no detailed information) | Oxygen-limited batch in flasks, complete medium (40 g/L xylose) | 0.87 | 0.28 | 0.31 | [15] |