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Method for preparing n-ethyl-l-menthyl formamide by inverting configuration of n-ethyl-neo-menthyl formamide

A technology of menthyl formamide and configuration inversion, applied in the field of configuration inversion of fine chemicals, can solve the problem of increasing equipment investment and production cost, increasing separation difficulty, and increasing the total yield of N-ethyl-L-menthyl formamide. The problem of unsatisfactory rate and other problems can achieve the effect of convenient post-reaction treatment, lower energy consumption and lower production cost.

Active Publication Date: 2022-03-11
WANHUA CHEM GRP CO LTD
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0004] However, the overall yield of N-ethyl-L-menthyl formamide is not ideal, and a certain proportion of isomers are mixed in the product
Thereby increasing separation difficulty, also greatly increased equipment investment and production cost
There is no report on the conversion of the final product menthylamide isomers

Method used

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  • Method for preparing n-ethyl-l-menthyl formamide by inverting configuration of n-ethyl-neo-menthyl formamide
  • Method for preparing n-ethyl-l-menthyl formamide by inverting configuration of n-ethyl-neo-menthyl formamide
  • Method for preparing n-ethyl-l-menthyl formamide by inverting configuration of n-ethyl-neo-menthyl formamide

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0027] N- ethyl - New - menthyl carboxamide with N- ethyl carboxamide -L- menthyl mixture 30g (N- ethyl - New - menthyl carboxamide / N- ethyl carboxamide menthyl = -L- 0.38) was dissolved in 150ml of toluene was added 0.6gN, N'- dicyclohexylmethylamine to the system. Under nitrogen blanket with stirring at conditions of 135 ℃ 24h. After washing twice with water after cooling water was added to the reaction system (wash to pH between 7 and 7.5), allowed to stand waiting layers were separated and the organic layer was removed and then the amount of delamination, delamination was allowed to stand again the organic layer was removed under reduced pressure to recover the solvent toluene was distilled off, to obtain about 27.4g product, the GC internal standard: N- ethyl - new - menthyl carboxamide / N- ethyl carboxamide menthyl = -L- 0.02, conversion was 91.3%, the selectivity 99.3%.

Embodiment 2

[0029] N- ethyl - New - menthyl carboxamide with N- ethyl carboxamide -L- menthyl mixture 30g (N- ethyl - New - menthyl carboxamide / N- ethyl carboxamide menthyl = -L- 0.26) was dissolved in 150ml of toluene was added 0.6gN, N'- dicyclohexyl-ethylamine to the system. Under nitrogen blanket with stirring at conditions of 135 ℃ 24h. Suitable water was added after cooling the reaction system which was washed with water until a pH of between 7 and 7.5, allowed to stand waiting stratification, the organic layer was removed and the layers were separated and washed twice with an appropriate amount of water, layered again, remove the organic recovering the toluene layer was distilled off under reduced pressure, to obtain about 28.5g product, GC internal standard quantification: N- ethyl - new - menthyl carboxamide / N- ethyl carboxamide -L- menthyl = 0.01, conversion was 95%, the selectivity was 99.1%.

Embodiment 3

[0031] N- ethyl - New - menthyl carboxamide with N- ethyl carboxamide -L- menthyl mixture 50g (N- ethyl - New - menthyl carboxamide / N- ethyl carboxamide menthyl = -L- 0.38) were dissolved in 250ml of toluene was added to the system 2.5gN, N'- diisopropylethylamine. Under nitrogen blanket with stirring at conditions of 135 ℃ 24h. The filtrate was added to pure water to a pH of between 7 and 7.5, allowed to stand waiting stratification, the organic layer was removed and the layers were separated and washed twice with an appropriate amount of purified water, allowed to stand again separated and the organic layer was removed under reduced pressure conditions recovering the toluene was distilled, to obtain about 46.7g product, the GC internal standard: N- ethyl - new - menthyl carboxamide / N- ethyl carboxamide -L- menthyl = 0.025, the conversion was 93% and the selectivity 98.9%.

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Abstract

The invention discloses a method for preparing N-ethyl-L-menthyl formamide by inverting the configuration of N-ethyl-neo-menthyl formamide, the method comprising N-ethyl-neo-menthyl formamide or The mixture of N-ethyl-neo-menthyl formamide and N-ethyl-L-menthyl formamide is dissolved in an organic solvent, and a catalyst is added to the system for configuration inversion reaction, and then the reaction system is washed, dried and separated , finally obtaining N-ethyl-L-menthyl formamide. The yield of this method is about 91%. The method is simple in operation, convenient in post-reaction treatment, environmentally friendly, and can increase the utilization rate of reaction atoms, and is a method suitable for industrial production.

Description

Technical field [0001] The present invention relates to a fine chemical methods with inversion of configuration, specifically an efficient, simple N- ethyl - New - menthyl carboxamide inversion of configuration method, such N- ethyl - New - mint formamide converted to product ethyl-N- -L- menthyl carboxamide. Background technique [0002] As the end product of the cooling agent, N- ethyl carboxamide -L- menthyl no stimulation such as menthol-like smell, cool feeling strength, pure flavor, mint cool times of 3-5, which is widely used in high-end daily chemical products and food products. Preparation of N- ethyl carboxamide -L- menthyl generally menthol as raw material, obtained through multi-step reaction product only, so that its price is higher. With economic development, people's living standards improve, people are also rapidly increasing demand for high-end products, cool taste, which makes -L- menthyl N- ethyl formamide has a very broad market prospects. The structural formu...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C07C233/58C07C231/18
Inventor 李建锋郭斌陈来中张永振黎源李文滨李晶
Owner WANHUA CHEM GRP CO LTD