Page 165 - Lignocellulosic Biomass to Liquid Biofuels

Thermal [45,46] volatile of Production liquid and Gas char and products production of decomposition temperature High cellulose requirement main the of Separation production Ash of portions can reduction size Particle and hemicellulose costly be from lignin residual cellulose [47,48] more requires Pro

cooling kV/ duration milliseconds) H 2 SO 4 ,HCl, for (5% high ratio 60°C, 4 h 35° v/v),

then condensing (5 20 short to process loads solids substrate/ for (10% 40% substrate/mixture) H 2 SO 4 Solid/Liquid NaOH, 120°C, H 2 O 2
T . 300°C, and voltage High for cm) (nano (Dilute) 0.75% 5% HNO 3 T 5 160°C 200°C P 5 1 MPa Continuous low 10% mixture) process Batch loads (Concentrated) 10% 30% T 5 170°C 190°C 1:2 Dilute h 24 Ca(OH) 2 , of Adding (0.5 2.15% C

waste corn switchgrass chip, switchgrass wood corn bagasse, wheat rye rice switchgrass corn bagasse, cane
Wood, cotton, stover, Wood Poplar stover, straw, straw, hulls, Hardwood, stover, leaves

electric hydrolysis hydrolysis
Pyrolysis Pulsed field Chemical Acid Alkaline