Method for producing ethanol by wood fiber raw material
A technology for lignocellulosic raw materials and ethanol, applied in the field of ethanol production from lignocellulosic raw materials, can solve problems such as low yield of total sugar, achieve the effects of continuous operation, increase effective specific surface area, and improve utilization rate of total sugar
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Embodiment 1
[0023]In the first stage of the three-stage screw extruder, 500 grams of corn stalks were pulverized, then continuously impregnated with 1.3% dilute sulfuric acid at 60°C, with a residence time of 7 minutes, extruded, dehydrated and preliminarily expanded. In the second stage of the three-stage screw extruder, the dehydrated corn stalks were maintained at 160° C. and 0.7 MPa for 20 minutes. In the third section of the three-section screw extruder, the cooked material is steamed and exploded by screw extrusion, and instantly decompressed and puffed to obtain a porous and fluffy wet material. After adding water to the above-mentioned porous and fluffy wet material (the dry matter concentration ratio is 19%), the concentration of adding penicillin is 3 × 10 -4 g / L, temperature controlled at 55°C, and pH=5.0, add cellulase in an amount of 0.12 g / g cellulose, and enzymatically hydrolyze to obtain an enzymatic hydrolysis solution containing pentoses and hexoses. Transfer the obtain...
Embodiment 2
[0026] In the first stage of the three-stage screw extruder, 500 g of wheat straw was crushed, then continuously impregnated with 1.3% dilute sulfuric acid at 60°C, and after a residence time of 9 minutes, it was extruded, dehydrated and preliminarily expanded. In the second stage of the three-stage screw extruder, the dehydrated wheat straw was maintained at 170° C. and 0.8 MPa for 18 minutes. In the third section of the three-section screw extruder, the cooked material is steamed and exploded by screw extrusion, and instantly decompressed and puffed to obtain a porous and fluffy wet material. After adding water to the above-mentioned porous and fluffy wet material (dry substance concentration proportioning is 23%), the concentration of adding penicillin is 3 × 10 -4 g / L, temperature controlled at 55°C, and pH=4.5, cellulase was added in an amount of 0.12 g / g cellulose to obtain an enzymatic hydrolysis solution containing pentoses and hexoses. Transfer the obtained enzymatic...
Embodiment 3
[0029] In the first stage of the three-stage screw extruder, 500 grams of rice straw was crushed, then continuously impregnated with 1.3% dilute sulfuric acid at 60°C, and after a residence time of 8 minutes, extruded, dehydrated and preliminarily expanded. The dehydrated rice straw in the second stage of the three-stage screw extruder was maintained at 170° C. and 0.8 MPa for 25 minutes. In the third section of the three-section screw extruder, the cooked material is steamed and exploded by screw extrusion, and instantly decompressed and puffed to obtain a porous and fluffy wet material. After adding water to the above-mentioned porous and fluffy wet material (dry substance concentration proportioning is 23%), the concentration of adding penicillin is 3 × 10 -4 g / L, temperature controlled at 55°C, and pH=4.5, cellulase was added in an amount of 0.12 g / g cellulose to obtain an enzymatic hydrolysis solution containing pentoses and hexoses. Transfer the obtained enzymatic solut...
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