Table 3 Titer, yield, productivity, residual glycerol, fermentation mode and initial glucose level for 2,3-BDO production by different engineered S. cerevisiae cell factory microorganisms reported in the literature and in this study
From: Development of an industrial yeast strain for efficient production of 2,3-butanediol
Reference | 2,3-BDO titer (g/L) | Yield (g/g glucose) | Productivity (g.L−1.h−1) | By-product (Glycerol) (g/L) | Batch or Fed batch | Initial glucose (g/L) |
|---|---|---|---|---|---|---|
[33] | 2.29 | 0.113 | – | – | Batch | – |
[32] | 96.2 | 0.28 | 0.39 |  ± 30 | Fed batch | 100 |
[37] | 32.0 | 0.367 | 0.403 | 6.00 | One batch | 90 |
[35] | 72.9 | 0.41 | 1.43 | 0.34 | Fed Batch | 95 |
[38] | 154.3 | 0.404 | 1.98 | 34.00 | Fed batch | 330 |
[59] | 132.4 | 0.34 | 0.41 | 25.3 | Fed batch | 120 |
[61] | 81.0 | 0.27 | 0.16 | 71.8 | Fed batch | 100.0 |
[31] | 178.0 | 0.335 | 1.88 |  > 90 | Fed batch | 100.0 |
HGS37 (this study) | 130.64 | 0.48 | 1.58 | 8.06 | Batch | 280 |
HGS37 (this study) | 133.91 | 0.45 | 1.33 | 7.75 | Batch | 310 |
HGS37 (this study) | 119.99 | 0.36 | 0.99 | 6.51 | Batch | 340 |
HGS50 (this study) | 121.04 | 0.48 | 1.57 | 10.99 | Batch | 250 |