A kind of preparation method of α-acetyl-γ-butyrolactone
A technology of butyrolactone and acetyl group, applied in the field of preparation of α-acetyl-γ-butyrolactone, can solve problems such as high energy consumption, pollution, hidden dangers, etc., and achieves increasing feeding amount, reducing environmental pollution and eliminating pollution Effect
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Embodiment 1
[0019] The acetylating agent used in this embodiment is ethyl acetate. The acylation reactor (5L) was evacuated, then purged with nitrogen, then 1232g of γ-butyrolactone, 1894g of ethyl acetate and 100g of sodium metal were added, stirring was started, and the temperature was raised. After the system was refluxed, the nitrogen flow was stopped. Under the reflux state of the system, 280g of sodium metal was added continuously, and the speed of adding sodium metal was advisable to keep the reaction system stable. After the addition, continue the insulation reaction for 8h. Cool down to 30°C, gradually add about 2930g of 51% phosphoric acid solution under stirring, and neutralize until the pH of the system is between 3-4. After the neutralization, the layers were separated, the organic phase was separated, the aqueous phase was extracted once with 433g of toluene, and the organic phases were combined. Then first normal pressure (71 DEG C-90 DEG C) distills out the light compone...
Embodiment 2
[0021] The acetylating agent used in this embodiment is methyl acetate. Except that the acetylating agent uses 1595g methyl acetate to replace 1894g ethyl acetate in Example 1, all the other steps are the same as in Example 1. 1663.6 g of the product was obtained, the product purity was greater than 99.2%, and the yield reached 90.0%. The extracted aqueous phase was dehydrated to obtain 1878 grams of phosphate.
Embodiment 3
[0023] The acetylating agent used in this embodiment is a mixed ester of ethyl acetate and methyl acetate. Except that acetylating agent uses 947g ethyl acetate and 797g methyl acetate to replace 1894g ethyl acetate in embodiment 1, all the other steps are all the same as embodiment 1. 1674.5 g of the product was obtained, the product purity was greater than 99.1%, and the yield reached 90.5%. The extracted aqueous phase was dehydrated to obtain 1875 grams of phosphate.
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