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

Active Publication Date: 2018-04-24
SHANXI INST OF COAL CHEM CHINESE ACAD OF SCI
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

However, levulinic acid contains a ketone carbonyl group. In theory, it can realize the formation of a new carbon-carbon bond through its own aldol condensation, thereby generating a C10 compound, and this compound often contains 1-2 carboxyl groups. After selective catalysis Hydrogenation can generate dicarboxylic acids / diols and branched alkanes. These compounds are important fine chemicals or polymer monomer raw materials, but there are still few studies on the self-condensation reaction of levulinic acid
Spanish scientists invented a reaction process that uses basic metals to catalyze the aldol condensation of levulinic acid. The reaction temperature of this process is low and the harmony is mild. However, since levulinic acid is an organic acid, it will react with the basic catalyst and the catalyst is stable. Because the acidity of the carboxyl group is stronger than that of α-H on levulinic acid, the basic catalyst is often more likely to interact with the carboxyl group, resulting in low activity of the catalytic system
Shell uses strong acids such as molecular sieves and acid resins as catalysts to catalyze the dimerization of levulinic acid, but there are many products, and the acid resin itself has poor stability in the organic phase, and the pores of molecular sieves are easy to block, which brings great restrictions to its industrial production.

Method used

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  • Method for preparing 2-methyl-5, gamma-dioxotetrahydrofuran-2-pentanoic acid by catalysis of levulinic acid on basis of solvent process
  • Method for preparing 2-methyl-5, gamma-dioxotetrahydrofuran-2-pentanoic acid by catalysis of levulinic acid on basis of solvent process
  • Method for preparing 2-methyl-5, gamma-dioxotetrahydrofuran-2-pentanoic acid by catalysis of levulinic acid on basis of solvent process

Examples

Experimental program
Comparison scheme
Effect test

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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Abstract

The invention provides a method for preparing 2-methyl-5, gamma-dioxotetrahydrofuran-2-pentanoic acid by catalysis of levulinic acid on the basis of a solvent process. The method comprises the following steps: mixing a solvent with levulinic acid as usual, then adding a catalyst, and performing heating to 70-200 DEG C for a reaction for 0.25-96 h; performing reduced-pressure distillation to removea reaction solvent and unreacted levulinic acid, then fully dissolving a distilled residue with an organic solvent, performing filtering, removing the catalyst, and distilling a filtrate to obtain anaddition product. The method has the advantages that the conversion rate of levulinic acid is higher than 34%, and the product yield is higher than 28 %.

Description

technical field [0001] The invention relates to a method for preparing 2-methyl-5,γ-dioxotetrahydrofuran-2-pentanoic acid by self-addition of levulinic acid. technical background [0002] Levulinic acid (4-pentanone acid) is an important biomass-based platform compound, which is listed as the 12 most important platform compounds for sugar conversion by the US National Energy Administration. In terms of chemical structure, levulinic acid is a five-carbon linear compound containing two functional groups, carbonyl and carboxyl. Currently, lignocellulose can be efficiently converted to levulinic acid through a biorefinery process in continuous industrial reactors. In view of the fact that lignocellulose is the largest biomass resource in the world, the generation of levulinic acid, a biomass-based platform compound, will have strong competitiveness (at present, it has reached 0.06-0.18 pounds), and it has the potential to become a bulk chemical. potential. [0003] The cataly...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C07D307/33
CPCC07D307/33
Inventor 侯相林李政邓天昇王玉琪王英雄
Owner SHANXI INST OF COAL CHEM CHINESE ACAD OF SCI
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