Method for synthetizing 2,3-butanediol
A technology of butanediol and butanol, applied in the chemical industry, can solve the problems of long fermentation period, low selectivity and complicated process of biological method technology, and achieve the effects of broad industrial application prospect, simple process and high selectivity.
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Embodiment 1
[0017] ① Take 20% of A1 2 o 3 Mix the two evenly with 80% titanium-silicon molecular sieve catalyst, extrude, dry at 100 °C for 4 h, and roast at 500 °C for 4 h to obtain a titanium-silicon molecular sieve catalyst modified by aluminum oxide.
[0018] ② Dilute 15g of the catalyst prepared in step ① with 10g of quartz sand and put it in a fixed-bed reactor. The molar ratio of methanol, mixed C4 hydrocarbons and hydrogen peroxide is 40:1:1. Methanol and hydrogen peroxide are injected into the reactor with a metering pump, and the mixed C4 hydrocarbons are injected into the reactor through a metering pump. The three reactants are in contact with the modified titanium-silicon molecular sieve catalyst. Reaction, synthesis of 2,3-butanediol. Reaction conditions: reaction temperature 0 ℃, reaction pressure 0.5 Mpa, reaction bed liquid space velocity 60 h -1 . The obtained product was analyzed by chromatography, and the selectivity of 2,3-butanediol was 40.5%, and the conversion r...
Embodiment 2
[0020] Catalyst preparation is as shown in step ① of Example 1.
[0021] The catalyst is loaded in the slurry bed reactor, the total liquid volume is 3 liters, and the catalyst loading accounts for 5% of the total liquid volume. The molar ratio of ethanol, mixed C4 hydrocarbons and hydrogen peroxide is 40:10:1, reaction conditions: reaction temperature 60 ℃, reaction pressure 8.5 MPa, reaction bed liquid space velocity 10 h -1 , other steps are as in embodiment 1. The obtained product was analyzed by chromatography, and the selectivity of 2,3-butanediol was 41.8%, and the conversion rate of hydrogen peroxide was 99.5%.
Embodiment 3
[0023] Catalyst preparation is as shown in step ① of Example 1.
[0024] 10g of the prepared catalyst was diluted with 20g of quartz sand and placed in a continuous tube reactor. Reaction conditions: reaction temperature 80 ℃, reaction pressure 2.1 MPa, molar ratio of propanol, mixed C4 hydrocarbons and hydrogen peroxide is 1:1:1, reaction bed liquid space velocity 0.1 h -1 , other steps are with embodiment 1. The obtained product was analyzed by chromatography, and the selectivity of 2,3-butanediol was 39.5%, and the conversion rate of hydrogen peroxide was 99.1%.
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