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Production process of benzyl propionate

A benzyl propionate and production process technology, which is applied in the production process field of benzyl propionate, can solve the problems of strong corrosiveness of the catalyst, waste liquid pollution of the environment, troublesome product treatment, etc., achieve high catalytic activity, simple operation steps, Improve conversion rates and performance

Inactive Publication Date: 2019-07-12
天津大加化工有限公司
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0003] At present, there are two main industrial synthesis methods of benzyl propionate: one is the benzyl alcohol-propionic acid method, which is prepared by esterification, and the traditional catalyst is concentrated sulfuric acid or aluminum trichloride, iron trichloride, etc. Lewis acid, these catalysts have problems such as strong corrosiveness, many side reactions, troublesome product treatment, and environmental pollution from discharged waste liquid; Prepared after dissolving strong and toxic organic solvents, there are problems such as high toxicity and environmental pollution

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0037] A kind of production technology of benzyl propionate, specifically comprises following operation steps:

[0038] (1) Esterification reaction: Add 30 parts of sodium propionate solution to the reaction kettle, pump 80 parts of benzyl chloride into the metering tank through a vacuum pump, then put it into the reaction kettle, and put 3.08 parts into the reaction kettle part of dodecyltrimethylammonium chloride and 0.92 part of tetrabutylphosphine bromide, stir constantly, open the steam valve and raise the temperature to 120°C, so that the temperature of the reaction liquid in the kettle is 100°C, and carry out the esterification reaction for 15 hours , to obtain the first crude ester;

[0039] (2) Water washing once: put the first crude ester into the washing kettle, add cleaning water (distilled water+first water layer and second water layer) to clean the first crude ester, wash out the salt generated in the reaction process, and obtain The first brine and the second c...

Embodiment 2

[0044] The difference between embodiment 2 and embodiment 1 is:

[0045] In the esterification reaction, the temperature of the reaction liquid in the kettle was 127°C, and the esterification reaction was carried out for 18 hours; in the first water washing, the first oil layer was added to the esterification reaction raw materials, and the esterification reaction was continued for 4 hours; in the second water washing, the second oil layer Add the esterification reaction raw materials, and continue the esterification reaction for 3h. The purity of benzyl propionate in the product finally obtained was 99.50%, and the yield was 96.8%.

Embodiment 3

[0047] The difference between embodiment 3 and embodiment 1 is:

[0048] In the esterification reaction, the temperature of the reaction liquid in the kettle was 135°C, and the esterification reaction was carried out for 17 hours; in the first water washing, the first oil layer was added to the esterification reaction raw materials, and the esterification reaction was continued for 2 hours; in the second water washing, the second oil layer Add the esterification reaction raw materials and continue the esterification reaction for 1h. The purity of benzyl propionate in the finally obtained product was 99.56%, and the yield was 96.1%.

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PUM

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Abstract

The invention relates to the technical field of perfume processing, in particular to a production process of benzyl propionate. The production process comprises the following operation steps: carryingout an esterification reaction, namely putting benzyl chloride and a phase transfer catalyst into a sodium propionate solution to carry out the esterification reaction and obtain first crude ester; carrying out primary water washing, namely washing the first crude ester to obtain first saline water and second crude ester; carrying out secondary water washing, namely washing the second crude esterfor a second time with water to obtain second saline water and third crude ester; carrying out vacuum distillation, namely carrying out vacuum distillation on the third crude ester, and carrying outfraction condensation, thereby obtaining a finished product benzyl propionate, wherein the phase transfer catalyst is a mixture of quaternary ammonium salt and quaternary phosphonium salt in a mass ratio of (1-1.6):(0.3-0.7). The green and environmentally-friendly phase transfer catalyst is adopted to replace an organic solvent which is large in toxicity and a catalyst which is intensive in corrosion in a conventional process, the product treatment process is simplified, the production process has the advantages of being green and environmentally-friendly, and the yield of benzyl propionate can be increased when being compared with that of a conventional process.

Description

technical field [0001] The invention relates to the technical field of spice processing, in particular to a production process of benzyl propionate. Background technique [0002] Benzyl propionate (Benzyl propionate), also known as benzyl propionate, is a colorless oily liquid with volatility and a sweet scent of flowers. It is widely used in the preparation of food, cigarettes, soaps, and daily cosmetic essences. Such as jasmine flavor, fruit flavor and so on. [0003] At present, there are two main industrial synthesis methods of benzyl propionate: one is the benzyl alcohol-propionic acid method, which is prepared by esterification, and the traditional catalyst is concentrated sulfuric acid or aluminum trichloride, iron trichloride, etc. Lewis acid, these catalysts have problems such as strong corrosiveness, many side reactions, troublesome product treatment, and environmental pollution from discharged waste liquid; It is prepared after dissolving a strong and toxic orga...

Claims

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Application Information

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IPC IPC(8): C07C67/08C07C67/58C07C67/54C07C69/14
CPCC07C67/08C07C67/54C07C67/58C07C69/14
Inventor 游云深游乃生赵旭阳易于伟
Owner 天津大加化工有限公司
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