Production technology of sclareolide synthesized from sclareol
A technology of sclareolide and sclareolide, applied in the direction of organic chemistry and the like, can solve the problems of low conversion rate, long reaction time, unsuitable for industrial production and the like, and achieve the effect of improving the conversion rate and shortening the reaction time
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Embodiment 1
[0014] Follow the steps below to synthesize sclareolide:
[0015] a, cracking section, add 30% acetic acid solution 190L, hydrogen peroxide composite oxidant 90L, heteropolyacid salt catalyst 0.4kg, tetrabutylammonium bromide 2kg, sclareol 6kg in the cracking kettle, heat up to 90 ℃, The reaction solution was passed into ozone gas at a rate of 10 L / min, cooled after 4 hours of reaction, the reaction solution was transferred to a receiving tank, 200 L of toluene was added, stirred for extraction;
[0016] b. In the hydrolysis section, pump the upper organic phase in the receiving tank into the hydrolysis tank, then add 4kg of tetrabutylammonium bromide and 15kg of 1% potassium hydroxide solution, raise the temperature to 90°C, keep it for 3 hours, then add 1000L of water to stir, stand still;
[0017] c, acidification section, put the lower water phase in the hydrolysis tank into the neutralization tank, adjust the pH to 3 with sulfuric acid solution, let it stand, and then ca...
Embodiment 2
[0021] Follow the steps below to synthesize sclareolide:
[0022] a, cracking section, add 30% acetic acid solution 200L, hydrogen peroxide composite oxidant 100L, heteropolyacid salt catalyst 0.5kg, tetrabutylammonium bromide 5kg, sclareol 6kg in the cracking kettle, heat up to 90 ℃, The reaction solution was passed into ozone gas at a rate of 10 L / min, cooled after 4 hours of reaction, the reaction solution was transferred to a receiving tank, 200 L of toluene was added, stirred for extraction;
[0023] b. In the hydrolysis section, the upper organic phase in the receiver tank is pumped into the hydrolysis tank, then 5 kg of tetrabutylammonium bromide and 20 kg of 1% potassium hydroxide solution are added, the temperature is raised to 90 ° C, and maintained for 3 hours, then 1000 L of water is added to stir, stand still;
[0024] c, acidification section, put the lower water phase in the hydrolysis tank into the neutralization tank, adjust the pH to 3 with sulfuric acid sol...
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