WDE | Glycerol (g/L) | BC (g/L) | Productivity (g/L/d) | Carbon sources consumption (% w/w) | FAN consumption(% w/w) | WHC (w/w)1 | |||
---|---|---|---|---|---|---|---|---|---|
WDE (% v/v) | Glucose | Fructose | Glycerol | Total | Â | Â | |||
Thermal sterilization | |||||||||
 25 | Crude, ≈20 | 3.7 ± 0.25f | 0.42 ± 0.04e | 70.0 | 6.3 | 91.5 | 87.9 | 71.8 | 86.2 ± 6.89b |
 50 | Crude, ≈20 | 5.1 ± 0.22e | 0.56 ± 0.03d | 72.0 | 5.0 | 93.4 | 83.8 | 78.4 | 84.3 ± 5.99c |
 75 | Crude, ≈20 | 6.6 ± 0.22d | 0.67 ± 0.04c | 82.0 | 25.0 | 92.9 | 81.7 | 72.2 | 89.5 ± 6.35a |
 100 | Crude, ≈20 | 8.1 ± 0.45c | 0.81 ± 0.06b | 82.4 | 14.7 | 98.9 | 85.5 | 83.1 | 82.6 ± 4.75d |
 100 | Crude, ≈30 | 9.0 ± 0.38b | 0.90 ± 0.05a | 58.3 | 33.3 | 95.2 | 81.5 | 84.3 | 60.1 ± 3.75f |
 100 | Crude, ≈45 | 4.0 ± 0.25f | 0.45 ± 0.02e | 31.4 | 10.0 | 65.1 | 57.6 | 76.2 | 87.1 ± 5.76b |
 100 | Pure, ≈30 | 9.8 ± 0.42a | 0.98 ± 0.06a | 47.3 | 35.8 | 84.5 | 72.6 | 87.3 | 56.6 ± 4.01 g |
 0 | Crude, ≈30 | 5.1 ± 0.29e | 0.46 ± 0.03e | – | – | 57.6 | 57.6 | 52.1 | 68.4 ± 4.99e |
Filter sterilization | |||||||||
 100 | Crude, ≈30 | 6.6 ± 0.15d | 0.66 ± 0.02c | 100 | 17.2 | 60.4 | 57.4 | 72.7 | 86.0 ± 8.69b |