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Method for preparing unsaturated ketone from alkoxy propylene and propargyl alcohol

A technology of alkoxypropene and propargyl alcohol, which is applied in the field of producing VE main intermediates, to achieve the effects of reducing catalytic costs, improving catalytic efficiency, and reducing by-product formation

Active Publication Date: 2019-07-05
WANHUA CHEM GRP CO LTD
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0004] The purpose of the present invention is to provide a method for preparing unsaturated ketones from alkoxypropene and propargyl alcohol, thereby solving many problems in the existing "Saucy-Marbet" reaction process for preparing unsaturated ketones

Method used

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  • Method for preparing unsaturated ketone from alkoxy propylene and propargyl alcohol
  • Method for preparing unsaturated ketone from alkoxy propylene and propargyl alcohol
  • Method for preparing unsaturated ketone from alkoxy propylene and propargyl alcohol

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Experimental program
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Effect test

Embodiment 1

[0048] First, 224.4 g (1 mol) of tetrahydro-dehydronerolidol, 204.2 g (2 mol) of acetic anhydride, and 1.4 g (0.01 mol) of methyl iodide were added to the autoclave. Seal the autoclave, and after confirming that the sealing is good, replace 6 times with nitrogen gas and 6 times with carbon monoxide gas with a hydrogen volume content of 1%, and press to an absolute pressure of 3.0 MPa. Turn on the stirring paddle and slowly add 72.1 g (1 mol) of methoxypropylene dropwise over 3 hours, keep the carbon monoxide pressure at an absolute pressure of 3.0 MPa, and keep the inner temperature of the reactor at 180° C. for 3 hours. After the stirring was stopped, the gas was discharged and the pressure was lowered to normal pressure, and a small amount of the reaction solution was taken for GC analysis.

[0049] Composition of the reaction liquid: 49.89% of tetrahydrofarnesone, 0.08% of tetrahydronerolidol, 38.51% of acetic anhydride, 11.37% of acetic acid, and 0.15% of others. The conv...

Embodiment 2

[0053] First, 154.1 g (1 mol) of dihydrodehydrolinalool, 20.4 g (0.2 mol) of acetic anhydride, and 2.1 g (0.015 mol) of methyl iodide were charged into the autoclave. Seal the autoclave, confirm that the sealing is good, replace 6 times with nitrogen and then 6 times with carbon monoxide gas with a hydrogen volume content of 2%, and press to an absolute pressure of 5.0 MPa. Turn on the stirring paddle and slowly add 79.2 g (1.1 mol) of methoxypropylene dropwise over 3 hours, keep the carbon monoxide pressure at 5.0 MPa absolute, and keep the inner temperature of the reactor at 220°C for 6 hours. After stopping the stirring and cooling down to normal pressure, a small amount of reaction solution was taken for GC analysis.

[0054] Composition of the reaction liquid: 67.85% of dehydrogeranone, 1.09% of dihydrodehydrolinalool, 7.21% of acetic anhydride, 21.31% of acetic acid, 2.38% of methoxypropylene, and 0.16% of others. The conversion rate of dihydrodehydrolinalool is 98.4%, ...

Embodiment 3

[0056] First, 154.1 g (1 mol) of dihydrodehydrolinalool, 51.1 g (0.5 mol) of acetic anhydride, and 4.2 g (0.03 mol) of methyl iodide were charged into the autoclave. Seal the autoclave, and after confirming that the sealing is good, replace 6 times with nitrogen and then 6 times with carbon monoxide gas with a hydrogen volume content of 0.5%, and press to an absolute pressure of 5.0 MPa. Turn on the stirring paddle and slowly add 79.2 g (1.1 mol) of methoxypropylene dropwise over 4 hours, keep the carbon monoxide pressure at 5.0 MPa absolute, and keep the inner temperature of the reactor at 200°C for 4 hours. After stopping stirring and cooling down to normal pressure, a small amount of reaction liquid was taken for GC analysis.

[0057] Composition of the reaction liquid: 62.01% of dehydrogeranone, 0.15% of dihydrodehydrolinalool, 16.27% of acetic anhydride, 19.16% of acetic acid, 1.85% of methoxypropylene, and 0.56% of others. The conversion rate of dihydrodehydrolinalool i...

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Abstract

The invention provides a method for preparing unsaturated ketone from alkoxy propylene and propargyl alcohol. Alkoxy propylene is adopted as a raw material, and in the presence of acetic anhydride andCO, propargyl alcohol and alkoxy propylene are subjected to a Saucy-Marbet reaction to prepare unsaturated ketone. According to the method, the adopted acetic anhydride is a non-acid catalyst, reaction conditions are mild, the catalyst can be activated, generated and recycled, and the method has the advantages of being high in conversion rate and selectivity, low in reaction cost, good in environmentally friendly and the like.

Description

technical field [0001] The invention relates to a method for producing VE main intermediates, pyrethroid intermediates, vitamin A, vitamin K1, carotenoid intermediates and spices. Specifically, it is a method for preparing unsaturated ketone by "Saucy-Marbet" reaction of alkoxypropene and propargyl alcohol. Background technique [0002] Isophytol is a key intermediate in the synthesis of VE and VK, and unsaturated ketone is an intermediate product in the synthesis step of isophytol. The industry widely uses propargyl alcohol as the starting material to obtain the corresponding unsaturated ketone through the Carroll route method and the alkoxypropene method. [0003] One of the advantages of the alkoxypropene method over the Carroll route is that the propargyl alcohol only needs to undergo a one-step "Saucy- Marbet" reaction to obtain unsaturated ketones. The "Saucy-Marbet" reaction needs to be reacted under acidic catalytic conditions. Commonly used acidic catalysts inclu...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C07C45/51C07C49/203
CPCC07C45/513C07C49/203
Inventor 鲍元野杨宗龙宋明焱贾海兵黄文学张永振黎源
Owner WANHUA CHEM GRP CO LTD