Table 5.
Bioproducts | Natural Fibres | Pretreatments | Conditions | Yield Improvement/Product Properties | References |
---|---|---|---|---|---|
Biohydrogen | Corn stover | Steam explosion | 1.5 Mpa and 198 °C for 1.5 min | 51.9 L H2 kg−1 TS * | [79] |
Rice straw | Hydrothermal | pH 7.0, 210 °C, 15.4 °C min−1, and 20% TS | 28.0 mL H2 g−1 VS * | [80] | |
Biomethane | Sugarcane bagasse | Hydrolysis | 178.6 °C, 43.4 min, and solid to liquid ratio of 0.24 | 1.56 Nm3 CH4 kg−1 TOC * | [81] |
Wheat straw | Microwave irradiation | 260 °C, 33 bars, 3 min | 28% | [82] | |
Pennisetum hybrid | 12% | [83] | |||
Blend of maize, ryegrass, and rice straw | Extrusion | Exit slit opened at 60% | 11.5–13.4% | [84] | |
Hay | Steam explosion | 220 °C for 15 min | 16% | [85] | |
Vine trimming shoot | Extrusion | 200 g h−1 feed rate | 51–58% hemicellulose reduction, 15.7–21.4% CH4 increased | [78] | |
Biosugar | Wheat straw | Supercritical CO2 & steam explosion | A steam explosion at 200 °C for 15 min and supercritical CO2 of 12 MPa at 190 °C for 60 min | 36.5% | [86] |
Poplar wood chips | Mechanical pulping & steam | Disc clearance set 0.5–0.1 mm for mechanical pulping and steam pretreatment at 210 °C for 5 min | 76% | [87] | |
Poplar wood | Steam explosion | 180 °C and 18 min | 94% | [88] | |
Cane bagasse | Hydrothermal | 200 °C | 4 mg xylose ml−1 * | [89] | |
Pinewood | 240 °C and 10 min | 32% ** | [90] | ||
Rapeseed meal | 260 °C and 10 min | 51 g glucose kg−1 * | [91] | ||
Nanocellulose | Poplar wood | Steam explosion | 2 MPa for 180 s | 13.2% | [92] |
Cotton | High-pressure homogenization | 80 MPa for 30 HPH | 10–20 nm in diameter, reduced thermal stability, and crystallinity | [93] | |
Sugarcane bagasse | 10–20 nm in diameter, reduced thermal stability, and crystallinity | [94] | |||
Oil palm biomass | Superheated steam | 260 °C for 30 min | <100 nm diameter, 27% crystallinity reduced | [35] |
* The highest yield obtained. ** In carbohydrate.