CN106117061B - The synthetic method of chloro-carbonic acid -2- chloroethene esters - Google Patents

The synthetic method of chloro-carbonic acid -2- chloroethene esters Download PDF

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CN106117061B
CN106117061B CN201610447459.5A CN201610447459A CN106117061B CN 106117061 B CN106117061 B CN 106117061B CN 201610447459 A CN201610447459 A CN 201610447459A CN 106117061 B CN106117061 B CN 106117061B
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phosgene
chloro
carbonic acid
passed
synthetic method
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CN106117061A (en
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祝红福
陈南方
张敦河
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Hunan Gofar Fine Chemical Industry Tech Co Ltd
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Hunan Gofar Fine Chemical Industry Tech Co Ltd
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    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C68/00Preparation of esters of carbonic or haloformic acids
    • C07C68/02Preparation of esters of carbonic or haloformic acids from phosgene or haloformates

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  • Organic Chemistry (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)

Abstract

The present invention provides a kind of synthetic method of 2 chloroethene ester of chloro-carbonic acid, includes the following steps:It is passed through phosgene in the solvent for being cooled to 10 DEG C ~ 5 DEG C, obtains gas-liquid mixture;The ethylene oxide being passed through in the gas-liquid mixture after phosgene and vaporization, reacts 2 hours at 0 DEG C ~ 10 DEG C, obtains reactant;Above-mentioned reactant is warming up to 20 DEG C ~ 40 DEG C, phosgene is removed, obtains 2 chloroethene ester of chloro-carbonic acid.The synthetic method of 2 chloroethene ester of above-mentioned chloro-carbonic acid does not generate that hydrogen chloride gas, product acidity are easily-controllable and yield is higher.

Description

The synthetic method of chloro-carbonic acid -2- chloroethene esters
Technical field
The present invention relates to the field of chemical synthesis, more particularly to the synthetic method of chloro-carbonic acid -2- chloroethene esters.
Background technology
Chloro-carbonic acid -2- chloroethene esters are used as medicine, pesticide intermediate, harsher to product quality requirement, especially product acid Degree requires extremely stringent.The synthetic method of traditional chloro-carbonic acid -2- chloroethene esters is mainly chlorethanol phosgenation, and this method uses chloroethene It is passed through phosgene after alcohol sub-cooled thereto again, then insulation reaction is complete, then heats up and catch up with light.But this method generates largely Hydrogen chloride emission, product acidity is not easy to control, and yield is relatively low.
Invention content
Based on this, it is necessary to for traditional chloro-carbonic acid -2- chloroethene esters synthetic method generate a large amount of hydrogen chloride emission, The problem that product acidity is not easy to control, yield is relatively low provides and a kind of does not generate that hydrogen chloride gas, product acidity is easily-controllable and yield The synthetic method of higher chloro-carbonic acid -2- chloroethene esters.
A kind of synthetic method of chloro-carbonic acid -2- chloroethene esters, includes the following steps:
It is passed through phosgene in the solvent for being cooled to -10 DEG C ~ -5 DEG C, obtains gas-liquid mixture;
The ethylene oxide being passed through in the gas-liquid mixture after phosgene and vaporization, reacts 2 ~ 4 hours at 0 DEG C ~ 10 DEG C, obtains To reactant;
The reactant is warming up to 20 DEG C ~ 40 DEG C, phosgene is removed, obtains chloro-carbonic acid -2- chloroethene esters.
The solvent is toluene, chlorobenzene or chloro-carbonic acid -2- chloroethene esters in one of the embodiments,.
The step of ethylene oxide being passed through in the gas-liquid mixture in one of the embodiments, after phosgene and vaporization In, the mass ratio of the ethylene oxide and phosgene is 1:2.8~3.2.
The method for removing phosgene is specially in one of the embodiments,:It is passed through nitrogen and drives away phosgene, until phosgene It eliminates.
The speed that is passed through of the nitrogen is 15L/h ~ 25L/h in one of the embodiments,.
In one of the embodiments, when the solvent is toluene or chlorobenzene, the step of the removings phosgene after and also Include the following steps:
Rectifying removes solvent.
The synthetic method of above-mentioned chloro-carbonic acid -2- chloroethene esters carries out opening, no chlorine by ethylene oxide and phosgene Change hydrogen to generate, and phosgene is easier than hydrogen chloride gas eliminates, acidity is easy to control.In addition, by the way that first a part of phosgene is dissolved in In solvent, the utilization rate of phosgene can be improved, increases the yield of product.
Specific implementation mode
In order to make the foregoing objectives, features and advantages of the present invention clearer and more comprehensible, below to the specific reality of the present invention The mode of applying is described in detail.Many details are elaborated in the following description in order to fully understand the present invention.But The invention can be embodied in many other ways as described herein, and those skilled in the art can be without prejudice to this hair Similar improvement is done in the case of bright intension, therefore the present invention is not limited to the specific embodiments disclosed below.
A kind of synthetic method of chloro-carbonic acid -2- chloroethene esters, includes the following steps:
S110, it is passed through phosgene in the solvent for being cooled to -10 DEG C ~ -5 DEG C, obtains gas-liquid mixture.
Wherein, solvent is toluene, chlorobenzene or chloro-carbonic acid -2- chloroethene esters.
Toluene, chlorobenzene can preferably absorb phosgene, improve the utilization rate of phosgene as solvent.Chloro-carbonic acid -2- chloroethene esters are made For solvent, phosgene can not only be preferably absorbed, and subsequently no longer need to detach solvent, product quality is high, production cost is low.
The boiling point of phosgene is 8.2 DEG C, and solvent, which is cooled to -10 DEG C ~ -5 DEG C, so that phosgene is liquefied, be conducive to react into Row increases product yield.
It should be noted that phosgene can be pure phosgene in step S110, can also be containing foreign gas(Carbon monoxide And chlorine)Phosgene, the volume content of phosgene is 72% ~ 75% in the phosgene containing foreign gas.
S120, the ethylene oxide being passed through in above-mentioned gas-liquid mixture after phosgene and vaporization, it is small that 2 are reacted at 0 DEG C ~ 10 DEG C When, obtain reactant.
Wherein, in the step of ethylene oxide being passed through in above-mentioned gas-liquid mixed after phosgene and vaporization, ethylene oxide and light The mass ratio of gas is 1:2.8~3.2.
It should be noted that phosgene can be pure phosgene in step S120, can also be containing foreign gas(Carbon monoxide And chlorine)Phosgene, the volume content of phosgene is 72% ~ 75% in the phosgene containing foreign gas.
S130, above-mentioned reactant is warming up to 20 DEG C ~ 40 DEG C, removes phosgene, obtains chloro-carbonic acid -2- chloroethene esters.
In the present embodiment, the method for removing phosgene is specially:It is passed through nitrogen and drives away phosgene, until phosgene eliminates.
Wherein, the speed that is passed through of nitrogen is 20L/h ~ 25L/h.
Further include after the step of being appreciated that when solvent is toluene or chlorobenzene, phosgene is removed in above-mentioned steps S130 Following steps:Rectifying removes solvent.
The synthetic method of above-mentioned chloro-carbonic acid -2- chloroethene esters carries out opening, no chlorine by ethylene oxide and phosgene Change hydrogen to generate, and phosgene is easier than hydrogen chloride gas eliminates, acidity is easy to control.
It is specific embodiment below.
Embodiment 1
It is passed through the phosgene of 10L/h in the chloro-carbonic acid -2- chloroethene esters that 200g is cooled to -5 DEG C 1.5 hours, it is mixed to obtain gas-liquid Close object.
The phosgene and the ethylene oxide 10 hours after 30L/h vaporizations that 40L/h is passed through in above-mentioned gas-liquid mixture, at 0 DEG C Reaction 2 hours, obtains reactant.
Above-mentioned reactant is warming up to 20 DEG C, the nitrogen for being passed through 15L/h drives away phosgene, until phosgene eliminates, obtains 1670g Chloro-carbonic acid -2- chloroethene esters(Contain the 200g chloro-carbonic acid -2- chloroethene esters as solvent).
It is computed, the yield of chloro-carbonic acid -2- chloroethene esters is 99.1%.The mass concentration of product free acid is 0.07%.
Embodiment 2
It is passed through the phosgene of 10L/h in the chloro-carbonic acid -2- chloroethene esters that 200g is cooled to -10 DEG C 1.5 hours, it is mixed to obtain gas-liquid Close object.
The phosgene and the ethylene oxide 10 hours after 30L/h vaporizations that 40L/h is passed through in above-mentioned gas-liquid mixture, at 10 DEG C Reaction 4 hours, obtains reactant.
Above-mentioned reactant is warming up to 40 DEG C, the nitrogen for being passed through 25L/h drives away phosgene, until phosgene eliminates, obtains 1676g Chloro-carbonic acid -2- chloroethene esters(Contain the 200g chloro-carbonic acid -2- chloroethene esters as solvent).
It is computed, the yield of chloro-carbonic acid -2- chloroethene esters is 99.5%.The mass concentration of product free acid is 0.06%.
Embodiment 3
It is passed through the phosgene of 10L/h in the toluene that 200g is cooled to -5 DEG C 1.5 hours, obtains gas-liquid mixture.
The phosgene and the ethylene oxide 10 hours after 30L/h vaporizations that 40L/h is passed through in above-mentioned gas-liquid mixture, at 0 DEG C Reaction 2 hours, obtains reactant.
Above-mentioned reactant is warming up to 20 DEG C, the nitrogen for being passed through 15L/h drives away phosgene, until phosgene eliminates, rectifying removes Toluene obtains 1461g chloro-carbonic acid -2- chloroethene esters.
It is computed, the yield of chloro-carbonic acid -2- chloroethene esters is 98.5%.The mass concentration of product free acid is 0.08%.
Embodiment 4
It is passed through the phosgene of 10L/h in the chlorobenzene that 200g is cooled to -5 DEG C 1.5 hours, obtains gas-liquid mixture.
The phosgene and the ethylene oxide 10 hours after 30L/h vaporizations that 40L/h is passed through in above-mentioned gas-liquid mixture, at 0 DEG C Reaction 2 hours, obtains reactant.
Above-mentioned reactant is warming up to 20 DEG C, the nitrogen for being passed through 20L/h drives away phosgene, until phosgene eliminates, rectifying removes Chlorobenzene obtains 1463g chloro-carbonic acid -2- chloroethene esters.
It is computed, the yield of chloro-carbonic acid -2- chloroethene esters is 98.6%.The mass concentration of product free acid is 0.08%.
Several embodiments of the invention above described embodiment only expresses, the description thereof is more specific and detailed, but simultaneously Cannot the limitation to the scope of the claims of the present invention therefore be interpreted as.It should be pointed out that for those of ordinary skill in the art For, without departing from the inventive concept of the premise, various modifications and improvements can be made, these belong to the guarantor of the present invention Protect range.Therefore, the protection domain of patent of the present invention should be determined by the appended claims.

Claims (6)

1. a kind of synthetic method of chloro-carbonic acid -2- chloroethene esters, which is characterized in that include the following steps:
It is passed through phosgene in the solvent for being cooled to -10 DEG C ~ -5 DEG C, obtains gas-liquid mixture;
The ethylene oxide being passed through in the gas-liquid mixture after phosgene and vaporization, reacts 2 ~ 4 hours at 0 DEG C ~ 10 DEG C, obtains anti- Answer object;
The reactant is warming up to 20 DEG C ~ 40 DEG C, phosgene is removed, obtains chloro-carbonic acid -2- chloroethene esters.
2. the synthetic method of chloro-carbonic acid -2- chloroethene esters according to claim 1, which is characterized in that the solvent be toluene, Chlorobenzene or chloro-carbonic acid -2- chloroethene esters.
3. the synthetic method of chloro-carbonic acid -2- chloroethene esters according to claim 1, which is characterized in that in the gas-liquid mixed In the step of ethylene oxide being passed through in object after phosgene and vaporization, the mass ratio of the ethylene oxide and phosgene is 1:2.8~3.2.
4. the synthetic method of chloro-carbonic acid -2- chloroethene esters according to claim 1, which is characterized in that the removing phosgene Method is specially:It is passed through nitrogen and drives away phosgene, until phosgene eliminates.
5. the synthetic method of chloro-carbonic acid -2- chloroethene esters according to claim 4, which is characterized in that the nitrogen is passed through Speed is 15L/h ~ 25L/h.
6. the synthetic method of chloro-carbonic acid -2- chloroethene esters according to claim 2, which is characterized in that when the solvent is first When benzene or chlorobenzene, the step of the removing phosgene after it is further comprising the steps of:
Rectifying removes solvent.
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CN111662176B (en) * 2020-06-10 2023-01-24 湖南维摩新材料有限公司 Method for synthesizing n-hexyl chloroformate by phosgene method
CN111792996B (en) * 2020-06-10 2022-12-13 湖南维摩新材料有限公司 Method for synthesizing chloroformic acid-2-chloroethyl ester by phosgene method

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Denomination of invention: The synthetic method of chloroformic acid-2-chloroethyl ester

Effective date of registration: 20220801

Granted publication date: 20180817

Pledgee: Hunan Linxiang rural commercial bank Limited by Share Ltd.

Pledgor: HUNAN GOFAR FINE CHEMICAL TECH. CO.,LTD.

Registration number: Y2022980011705