Gas phase acid catalytic biomass hydrolysis continuous production method of furfural
An acid catalysis and biomass technology, applied in the direction of organic chemistry, etc., can solve the problems of difficult treatment of acid-containing waste residue, low furfural content, and many side reactions, and achieve the effects of less side reactions, high furfural yield, and less discharge of three wastes
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Embodiment 1
[0030] The diameter-to-height ratio of the reactor is 1:100, the amount of straw in a single reactor is 1500g, the total amount of straw in one cycle is 4500g, the mass concentration of hydrochloric acid is 5%, the steam flow rate is 15 mL / min, and the temperature in the reactor is 165 o C, according to the above operation steps, when the concentration of furfural at the outlet of reactor 3 is reduced to below 0.1%, 20.2 kg of furfural aqueous solution with a content of 1.4% is obtained, and the yield is 40%.
Embodiment 2
[0032] The ratio of diameter to height of the reactor is 1:100, the amount of straw in a single reactor is 1500g, the total amount of straw in one cycle is 4500g, the mass concentration of hydrochloric acid is 5%, the steam flow rate is 30 mL / min, and the temperature in the reactor is 155 o C, according to the above operation steps, when the concentration of furfural at the outlet of reactor 3 is reduced to below 0.1%, 15.2 kg of furfural aqueous solution with a content of 2.8% is obtained, and the yield is 60.2%.
Embodiment 3
[0034] The ratio of diameter to height of the reactor is 1:100, the amount of straw in a single reactor is 1500g, the total amount of straw in one cycle is 4500g, the mass concentration of hydrochloric acid is 5%, the steam flow rate is 25 mL / min, and the temperature in the reactor is 145 o C, according to the above operation steps, when the concentration of furfural at the outlet of reactor 3 is reduced to below 0.1%, 8.0 kg of furfural aqueous solution with a content of 8% is obtained, and the yield is 90.5%.
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