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Continuous synthetic method for 3,5-dichloro-2-pentanone

A technology for chemical synthesis and pentanone, which is applied in the field of continuous synthesis of 3,5-dichloro-2-pentanone, can solve the problems of large usage of glacial acetic acid and concentrated hydrochloric acid, cumbersome operation, and poor operating environment. The temperature and feed rate are simple and controllable, the reaction by-products are reduced, and the synthesis cost is reduced

Active Publication Date: 2017-05-17
HUNAN CHEM RES INST
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

[0005] In 2014, Qin Yongqi and others disclosed a method for synthesizing 3,5-dichloro-2-pentanone using γ-butyrolactone and sulfonyl chloride as main raw materials, methanol, thionyl chloride, dioxane, concentrated hydrochloric acid, etc.; The method is cumbersome in operation, long in process, numerous in raw materials, and the specific yield content has not been reported.
[0006] In 2015, Li Yu and others disclosed a method for synthesizing 3,5-dichloro-2-pentanone with α-chloro-α-acetyl-γ-butyrolactone, glacial acetic acid and concentrated hydrochloric acid as main raw materials; The specific content of 3,5-dichloro-2-pentanone has not been reported, and its yield is 88.5%. The operation process of this method is relatively simple, but the consumption of glacial acetic acid and concentrated hydrochloric acid is large, the recovery is difficult, the amount of waste acid is large, and the three wastes large
[0007] Chen Mingming et al. reported in 2015 a batch synthesis of 3,5-dichloro-2-pentane with α-chloro-α-acetyl-γ-butyrolactone and solid phosgene as main raw materials under the catalytic action of a catalyst. The method of ketone; the operation of this method is more loaded down with trivial details, and reaction needs to add catalyst, and belongs to intermittent reaction, and yield is not high
[0008] In 2015, Zhang Yu and others disclosed a method to synthesize 3,5-dichloro-2-butyrolactone by reaction and distillation using α-chloro-α-acetyl-γ-butyrolactone, salt, phase transfer catalyst and concentrated hydrochloric acid as the main raw materials. The method of pentanone; the method is cumbersome to operate, the reaction time is long, the reaction of some raw materials is not complete, the amount of three wastes is large, and the operating environment is poor
[0009] The synthesis method of this similar compound reported at present is mainly a batch method, method one: the sulfuryl chloride method, this method has the following disadvantages: the operation process is loaded down with trivial details, the flow process is long, involves many raw materials, and the amount of three wastes is large
Method 2: Concentrated hydrochloric acid method, this method has the following disadvantages: the use of glacial acetic acid and concentrated hydrochloric acid is large, recovery is difficult, the amount of waste acid is large, and the amount of three wastes is large
Method three: solid phosgene method, this method has the following disadvantages: the operation is cumbersome, a catalyst must be involved in the reaction, it is an intermittent reaction, the yield is not high, and the amount of three wastes is large

Method used

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  • Continuous synthetic method for 3,5-dichloro-2-pentanone
  • Continuous synthetic method for 3,5-dichloro-2-pentanone

Examples

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Embodiment 1

[0028] Dissolve 17.09g (95.10%, 0.10mol) of α-chloro-α-acetyl-γ-butyrolactone in 120.00g of dichloroethane to form α-chloro-α-acetyl-γ-butyrolactone A mixed solution of dichloroethane, and the mixed solution is placed in a raw material bottle with a double plunger pump; open the temperature control system, keep the temperature of the microreactor at 45 ° C, and put the mixed solution in the raw material bottle through a double plunger pump The mixed solution is injected in the microreactor with the feeding speed of 0.5mL / min, simultaneously with 10.10g (98%, 0.10mol) phosgene is directly injected in the microreactor with the rate of 0.0119L / min by gas flowmeter metering, α -Chloro-α-acetyl-γ-butyrolactone and phosgene undergo a continuous chlorination ring-opening reaction in the microreactor, and the reaction solution after the reaction is received at the outlet of the microreactor, and the resulting reaction solution is distilled Finally, 14.81 g of 3,5-dichloro-2-pentanone ...

Embodiment 2

[0030] Dissolve 17.09g (95.10%, 0.10mol) of α-chloro-α-acetyl-γ-butyrolactone in 90.00g of dichloroethane to form α-chloro-α-acetyl-γ-butyrolactone A mixed solution of dichloroethane, and the mixed solution is placed in a raw material bottle with a double plunger pump; open the temperature control system, keep the temperature of the microreactor at 45 ° C, and put the mixed solution in the raw material bottle through a double plunger pump The mixed solution was injected into the microreactor at a feed rate of 2.0mL / min, while 10.10g (98%, 0.10mol) phosgene was metered directly into the reactor by a gas flow meter at a rate of 0.0641L / min, α- Chloro-α-acetyl-γ-butyrolactone and phosgene undergo a continuous chlorination ring-opening reaction in the microreactor, and the reaction solution after the reaction is received at the outlet of the microreactor, and the resulting reaction solution is distilled 14.27 g of 3,5-dichloro-2-pentanone with a mass percentage of 96.83% was obtai...

Embodiment 3

[0032] Dissolve 17.09g (95.10%, 0.10mol) of α-chloro-α-acetyl-γ-butyrolactone in 120.00g of dichloroethane to form α-chloro-α-acetyl-γ-butyrolactone A mixed solution of dichloroethane, and the mixed solution is placed in a raw material bottle with a double plunger pump; open the temperature control system, keep the microreactor at a constant temperature of 30 ° C, and put the mixed solution in the raw material bottle through a double plunger pump The mixed solution was injected into the microreactor at a feed rate of 0.5mL / min, while 11.11g (98%, 0.11mol) phosgene was metered directly into the reactor by a gas flow meter at a rate of 0.0131L / min, α- Chloro-α-acetyl-γ-butyrolactone and phosgene undergo a continuous chlorination ring-opening reaction in the microreactor, and the reaction solution after the reaction is received at the outlet of the microreactor, and the resulting reaction solution is distilled 14.66 g of 3,5-dichloro-2-pentanone with a mass percentage of 97.10% w...

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Abstract

The invention discloses a continuous synthetic method for 3,5-dichloro-2-pentanone. The method comprises the steps of adding a dichloroethane solution of alpha-chloro-alpha-acetyl-gamma-butyrolactone and carbonyl chloride into a microreactor, and conducting continuous chlorination ring-opening reaction to generate 3,5-dichloro-2-pentanone. The continuous synthetic method for 3,5-dichloro-2-pentanone has the advantages of no catalyst, simplicity in operation, high reaction selectivity, low energy consumption, high purity, high yield and the like.

Description

technical field [0001] The invention belongs to the technical field of preparation of fine chemical products, and in particular relates to a continuous synthesis method of 3,5-dichloro-2-pentanone. Background technique [0002] 3,5-dichloro-2-pentanone, English name: 3,5-dichloro-2-pentanone, molecular formula: C 5 h 8 Cl 2 O, molecular weight: 155, molecular structure formula: [0003] [0004] 3,5-Dichloro-2-pentanone is an important pharmaceutical and pesticide intermediate, which can be used to synthesize γ-aminobutyric acid (GABA) modulator clomethiazole, and can also be used to synthesize a series of medical compounds for inhibiting leukemia and anti-tumor , or an important intermediate of triazole fungicide prothioconazole. Prothioconazole is a new type of broad-spectrum triazolethione fungicide developed by Bayer, mainly used to prevent and control many diseases of cereals, wheat and legumes. Prothioconazole has low toxicity, no teratogenicity, and no mutageni...

Claims

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Application Information

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IPC IPC(8): C07C45/59C07C49/16
CPCC07C45/59C07C49/16
Inventor 王胜得陈明曾雪云刘伟曾敬
Owner HUNAN CHEM RES INST
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