Method for preparing 2-methyl-5, gamma-dioxotetrahydrofuran-2-pentanoic acid by catalysis of levulinic acid on basis of solvent process
A technology of dioxotetrahydrofuran and levulinic acid, applied in directions such as organic chemistry, can solve problems such as poor catalyst stability, low reaction temperature, poor stability, etc., and achieve the effects of reducing adverse effects, wide sources, and low price
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Embodiment 1
[0027] Mix 10g of levulinic acid and 100ml of γ-valerolactone thoroughly, and then add 1.36g of ZnCl 2 Dubbed the reaction system. The reaction solution was heated to 130°C and reacted for 6h. The structure of 2-methyl-5, γ-dioxotetrahydrofuran-2-pentanoic acid is shown in the attached drawing (see attached for NMR and MS results Figure 1-5 ). The reaction product was distilled under reduced pressure at 150° C. and 3 kPa until no liquid distilled out. The distillation residue was dissolved with 10 ml of acetone, filtered, and the filtrate was evaporated to dryness to obtain 3.8 g of the target product with a purity of 85%. The conversion of levulinic acid was 40%, and the overall yield of the process was 32%.
Embodiment 2
[0029] Mix 10g of levulinic acid and 5ml of γ-butyrolactone thoroughly, and then add 0.2g of ZnBr 2 Dubbed the reaction system. The reaction solution was heated to 120°C and reacted for 6h. The reaction product was distilled under reduced pressure at 140° C. and 2.5 kPa until no liquid distilled out, dissolved in 20 ml of ethyl acetate, filtered, and the filtrate was evaporated to dryness to obtain 4 g of the target product with a purity of 88%. The conversion of levulinic acid was 42%, and the overall yield of the process was 35%.
Embodiment 3
[0031] Mix 10g of levulinic acid and 8ml of γ-valerolactone thoroughly, and then add 0.5g of FeCl 3 Filled into a reaction system. The reaction solution was heated to 70°C and reacted for 96h. The reaction product was distilled under reduced pressure at 130° C. and 2 kPa until no liquid distilled out, dissolved in 30 ml of acetone, filtered, and the filtrate was evaporated to dryness to obtain 4.1 g of the target product with a purity of 85%. The conversion of levulinic acid was 43%, and the overall yield of the process was 35%.
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