A method for preparing lignocellulosic biomass coupled with phenols and furan derivatives
A technology of lignocellulose and furan derivatives is applied in the field of biomass energy conversion and utilization, which can solve the problems of environmental pressure, increase the biomass refining process technology and energy consumption, waste resources, etc., so as to save costs and improve the utilization rate of raw materials. , the effect of a wide range of raw materials
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Embodiment 1
[0026] With 5g of pennisetum (containing 32% cellulose, 22% hemicellulose, and 28% lignin) with a particle size of 0.5mm as raw material, in the reactor, add raw material, CeO2 solid alkali in a mass ratio of 1:0.5:25 Catalyst and water, after reacting at 180°C for 30 minutes, pass through a 80-mesh sieve, collect the raw material slag left on the sieve, and then separate the solid from the sieve to obtain a solid alkali catalyst; collect the liquid phase, the liquid phase Containing 0.41g of phenolic products, wherein, monophenolic product 0.19g (calculated based on raw material lignin, phenolic product yield is 29.3%, single phenolic product yield is 13.6%); Furan derivative 1.21g (based on raw material total sugar calculation, the yield is 44.8%) and cyclopentenone derivatives 0.04g (calculated with the total sugar of the raw material, the yield is 1.5%); the raw material slag collected after the previous step pretreatment is placed in a pH value of 4.8 In the acetic acid / s...
Embodiment 2
[0028] With 5g of pennisetum (containing 32% cellulose, 22% hemicellulose, and 28% lignin) with a particle size of 0.5mm as raw material, in the reactor, add raw material, CeO2 solid alkali in a mass ratio of 1:0.5:25 Catalyst and water, react at 270°C for 60 minutes, pass through a 80-mesh sieve, collect the raw material slag left on the sieve, and separate the under-sieve from solid-liquid to obtain a solid alkali catalyst; collect the liquid phase, the liquid phase Containing 0.97g of phenolic products, wherein, 0.59g of monophenolic products (based on raw material lignin, the yield of phenolic products is 69.3%, and the yield of monophenolic products is 42.1%); furan derivatives 0.42g (based on the total raw material sugar calculation, the yield is 15.6%) and cyclopentenone derivatives 0.68g (calculated with the total sugar of the raw material, the yield is 25.2%); the raw material slag collected after the previous step pretreatment is placed in a pH value of 4.8 In the ac...
Embodiment 3
[0030] With 5g of pennisetum with a particle size of 0.5mm (containing 32% cellulose, 22% hemicellulose, and 28% lignin) as a raw material, in the reactor, add raw materials, KOH / Al2O3 at a mass ratio of 1:0.1:10 Solid alkali catalyst and water react at 240°C for 30 minutes, pass through a sieve of 80 meshes, collect the raw material slag left on the sieve, and separate the undersieve from solid-liquid to obtain a solid alkali catalyst; collect the liquid phase, Containing 0.73g of phenolic products in the liquid phase, wherein, 0.36g of monophenolic products (calculated based on raw material lignin, the yield of phenolic products is 52.1%, and the yield of monophenolic products is 25.7%); 0.55g of furan derivatives (based on raw material total sugar calculation, yield is 20.4%) and cyclopentenone derivative 0.74g (calculation based on raw material total sugar, yield is 27.4%); the raw material slag collected after the previous step pretreatment is placed in a pH value of Add ...
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