Sample 7 mg enzyme/g (glucan + xylan) | Energy input during fine milling (MJ/kg) | Monomeric + oligomeric Glucose % theor. yield | Glucose mass yield (kg/kg biomass) | Energy efficiency (glucose mass yield/energy input) (MJ/kg) | Monomeric + oligomeric Xylose % theor. yield | Xylose mass yield (kg/kg biomass) | Energy efficiency (xylose mass yield/energy input) (MJ/kg) | Energy efficiency (glucose + xylose mass yield/energy input) (MJ/kg) |
---|---|---|---|---|---|---|---|---|
Union process attritor mill, 5Â min | 0.958 | 61.75 | 0.2334 | 0.244 | 81.13 | 0.1874 | 0.196 | 0.439 |
Hosokowa 2ACM Air-classifier mill | 1.801 | 55.81 | 0.2110 | 0.117 | 74.56 | 0.1722 | 0.0957 | 0.213 |
Fluid energy model 4 microjet, jet mill | 5.40 | 57.06 | 0.2157 | 0.0399 | 75.74 | 0.1750 | 0.0461 | 0.0886 |
Kemutec 5H universal pin mill, 2 passages | ND | 53.57 | 0.2025 | Â | 74.88 | 0.1730 | Â | Â |
NH3-treated unmilled | NA | 49.58 | 0.1874 | Â | 59.61 | 0.1377 | Â | Â |
Sample 14Â mg enzyme/g (glucan + xylan) | ||||||||
 Attritor mill | 0.958 | 81.77 | 0.3091 | 0.323 | 91.81 | 0.2121 | 0.221 | 0.544 |
 Air-classifier mill | 1.801 | 70.62 | 0.2669 | 0.148 | 83.18 | 0.1921 | 0.1068 | 0.255 |
 Jet mill | 5.40 | 66 | 0.2495 | 0.0462 | 74.11 | 0.1712 | 0.0319 | 0.0779 |
 Pin mill, 2 passages | ND | 59.69 | 0.2256 |  | 73.46 | 0.1697 |  |  |
 NH3-treated unmilled | NA | 57.09 | 0.2158 |  | 63.07 | 0.1457 |  |  |
Sample 28Â mg enzyme/g (glucan + xylan) | ||||||||
 Attritor mill | 0.958 | 82.57 | 0.3121 | 0.326 | 87.36 | 0.2018 | 0.211 | 0.537 |
 Air-classifier mill | 1.801 | 79.83 | 0.3018 | 0.168 | 87.65 | 0.2025 | 0.112 | 0.280 |
 Jet mill | 5.40 | 76.31 | 0.2885 | 0.0534 | 85.23 | 0.1969 | 0.0365 | 0.0899 |
 Pin mill, 2 passages | ND | 72.54 | 0.2742 |  | 79.36 | 0.1833 |  |  |
 NH3-treated unmilled | NA | 61.89 | 0.2339 |  | 64.21 | 0.1483 |  |  |