Entry | Hydrolysis mode | Lignocellulosic materials | Pretreatment methods | Solids loading | Hydrolysis time (h) | Sugar concentration (g/L) | Â | Conversion rate | References | |||
---|---|---|---|---|---|---|---|---|---|---|---|---|
Glucose | Xylose | Cello-oligosaccharides | Xylo-oligosaccharides | TRS | ||||||||
1 | Fed-batch | Corncob | Irradiation pretreatment | 40% (w/v) | 120 | 235 | 16 | _ | _ | 251 | _ | [20] |
2 | Fed-batch | Corn stover | Steam explosion and alkaline hydrogen-peroxide pretreatment | 30% (w/v) | 144 | 175 | 22 | 20 | Â | 220 | Total conversion rate of 60% | [28] |
3 | Batch with mechanical stirring | Corn stover | NaOH pretreatment and mechanical refining | 28% (w/w), equals to 38.9% (w/v) | 120 | 135.2 | 99.4 | 7.3 | _ | 270 | Monomeric sugar yield of 87% | [12] |
4 | Fed-batch | Sugarcane bagasse | Alkali pretreatment | 33% (w/v) | 120 | 129.5 | 56.0 | 9.4 | _ | 200 | Glucan conversion of 59.9% | [16] |
5 | Fed-batch | Corn stover | SMs pretreatment | 40% (w/v) | 120 | 146.7 | 58.7 | 15.6 | 25.9 | 251.8 | Glucan and xylan conversions of 89.5% and 88.5%, respectively | This work |