“…Net energy output 61 kWh/d Zieliński et al 2019 | Conifer and Eucalyptus pulp | ARHCR | - | 6000 rpm, 15.2 L/min, 98 kPa, 9 min, T = 34 °C, 3% solid loading | Paper with tensile index 50.5 kN m/kg, burst index at 3 kPa.m 2 /g. Energy consumption 58.4 kWh/m 3 | Kosel et al 2019 |
Sugarcane bagasse (< 0.250 mm) | Venturi tube (1.5 mm of throat diameter, length 40 mm) | Biomass slurry (Mixed with catalyst and circulated in a closed loop) | 4.9% NaOH, 2.03% solid loading, 58.33 min, operating temperature 65 °C, inlet pressure 300 kPa | Lignin removal 56.14%, 97.2% enzymatic hydrolysis yield at the optimal condition obtained by RSM | Bimestre et al 2020 |
Corncob (≤ 212 μm) | Orifice plate | Biomass slurry (Mixed with acetate buffer and circulated in a closed loop) | Laccase enzyme 6.5 U/g of biomass, 5% solid loading, 60 min, operating temperature 70 °C | Lignin removal 64.1%, Hemicellulose removal 6.57%, saccharification efficiency of 55% with multifunctional cellulases at 50 °C and pH. 5.0 | Ganesan et al 2020 |
Sugarcane bagasse (10 mesh) | Vortex based cavitation device | Biomass slurry (Mixed with catalyst and circulated in a closed loop) | Solid loading 1% w/v, 1.2m 3 /h, 100 passes at 30 °C, 0.75 M NaOH, 60 min | Lignin removal 77.4%, 75.5% ± 1.9 g/L glucose was released with 70.3% Cellulose hydrolysis, hemicellulose conversion 69.4% | Nalawade et al 2020 |
Wheat straw (< 0.05 mm) | ARHCR | Biomass slurry (Mixed with catalyst and circulated in a closed loop) | 3000 rpm, 50 °C, 0.4% NaOH, solid–liquid ratio 1:50, 30 min | Lignin removal 24.05% | Lauberte et al 2021 |
Miscanthus × giganteus stalks (5 mm) | ARHCR | Biomass slurry (Mixed with catalyst and circulated in a closed loop) | 0.3 M KOH, 2200 rpm, 20 min, 7% solid loading, Room Temperature | Lignin removal 41.54%. |
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