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A kind of preparation method of 1,1,1,3,3-pentachloropropane

A technology for pentachloropropane and vinyl chloride, which is applied in the field of preparation of 1,1,1,3,3-pentachloropropane, can solve the problems of unstable properties, deposition of iron powder, affecting rectification operation and product yield, etc. , to achieve the effect of shortening the reaction time, increasing the reaction speed, and shortening the residence time

Active Publication Date: 2018-08-03
JUHUA GROUP TECH CENT
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

But this method adopts the ferrous chloride of unstable property as main catalyst, simultaneously iron powder is in the raffinate activation process to containing main catalyst and cocatalyst, because fine iron powder is suspended in the product stream of circulation very likely, not only It is easy to cause iron powder to deposit in the pipeline, and it will also affect the subsequent rectification operation and product yield

Method used

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  • A kind of preparation method of 1,1,1,3,3-pentachloropropane

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[0024] The invention is a preparation method of 1,1,1,3,3-pentachloropropane, which uses carbon tetrachloride and vinyl chloride as raw materials, and then mixes corresponding catalysts and co-catalysts in a tubular reactor for adjustment. Polymerization reaction, thereby obtain 1,1,1,3,3-pentachloropropane, its concrete preparation steps are as follows:

[0025] (1) Carbon tetrachloride, vinyl chloride and cocatalyst are fully mixed to form a mixture, fully stirred to ensure that carbon tetrachloride and vinyl chloride are fully mixed, the mixture is placed in a preheater, and the mixture is preheated by the preheater Heat to 100-140°C, preferably preheating to 100-120°C; wherein the molar ratio of carbon tetrachloride to vinyl chloride is (1-10):1, wherein the preferred molar ratio of carbon tetrachloride to vinyl chloride The ratio is (1.5-5): 1. When retrieving the materials, the weight of each reclaimed material is generally converted into molar mass, so as to control the...

Embodiment 1

[0034] First, fully mix 432.4g carbon tetrachloride, 69.4g vinyl chloride and 7.4g trimethyl phosphate to form a mixture. The calculated molar ratio of carbon tetrachloride to vinyl chloride is 2:1, and the cocatalyst trimethyl phosphate accounts for The mass percentage of raw materials is 1.45%. Fully stir the mixture, put the mixture in the preheater, and use the preheater to preheat the mixture to 120°C; then take the telomerization reactor, the diameter of the telomerization reactor is Ф20×2.5mm, and the length is 1m externally heated tubular glass reactor. In the externally heated tubular glass reactor, the composite metal catalyst is loaded, and the filling amount of the composite metal catalyst is 80% of the reactor volume, wherein the content of each component in the composite metal catalyst is: iron is 90%, nickel is 4.5%, chromium is 5.5%. Next, the preheated mixture was introduced into an externally heated tubular glass reactor, and the telomerization reaction was...

Embodiment 2

[0043] First, fully mix 426.7g carbon tetrachloride, 40.1g vinyl chloride and 12.5g triethyl phosphate to form a mixture. The calculated molar ratio of carbon tetrachloride to vinyl chloride is 4.32:1, and the cocatalyst triethyl phosphate accounts for The mass percentage of raw materials is 2.61%. Fully stir the mixture, put the mixture in the preheater, and use the preheater to preheat the mixture to 120°C; then take the telomerization reactor, the diameter of the telomerization reactor is Ф20×2.5mm, and the length is 1m externally heated tubular glass reactor. In the externally heated tubular glass reactor, the composite metal catalyst is loaded, and the filling amount of the composite metal catalyst is 90% of the reactor volume, wherein the content of each component in the composite metal catalyst is: iron is 90%, nickel is 4.5%, and chromium is 90%. 5.5%. Next, the preheated mixture was introduced into an externally heated tubular glass reactor, and the telomerization r...

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Abstract

The invention discloses a preparation method of 1,1,1,3,3-pentachloropropane, comprising the following preparation steps: (1) fully mixing carbon tetrachloride, vinyl chloride and cocatalyst, and preheating to 100 ~140℃, the molar ratio of carbon tetrachloride and vinyl chloride is 1~10:1, the mass percentage of co-catalyst in the mixed raw material is 0.5~10%; (2) the preheated mixed raw material enters the composite metal catalyst In a tubular reactor, the telomerization reaction is carried out under the conditions of a reaction pressure of 0.2-1.0MPa, a reaction temperature of 80-140°C, and a residence time of 5-90 minutes; (3) the reacted mixture is recovered by rectification. The raw materials and co-catalysts of the reaction also utilize the rectification method to obtain the 1,1,1,3,3-pentachloropropane product. The invention provides a continuous preparation method of 1,1,1,3,3-pentachloropropane with simple equipment and easy implementation. The method can greatly shorten the reaction time, the catalyst does not need to be separated in the subsequent process, and the operation is simple and convenient.

Description

technical field [0001] The present invention relates to a kind of preparation method of 1,1,1,3,3-pentachloropropane, especially to a kind of using carbon tetrachloride and vinyl chloride as raw materials, telomerization synthesis 1,1,3-pentachloropropane in a tubular reactor Process for the preparation of 1,3,3-pentachloropropane. Background technique [0002] 1,1,1,3,3-Pentachloropropane (HCC-240fa) is an intermediate for the preparation of 1,1,1,3,3-pentafluoropropane (HCC-245fa). 1,1,1,3,3-Pentafluoropropane has zero atmospheric ozone depletion potential (ODP) and is a fluorinated hydrocarbon compound that is safe for the atmospheric ozone layer. It is currently mainly used as a fluorodichloromethane (CFC -11) and 1,1,1-dichlorofluoroethane (HCFC-141b), widely used as blowing agents, solvents and cleaning agents. [0003] In the existing 1,1,1,3,3-pentachloropropane preparation technology, carbon tetrachloride and vinyl chloride are mainly used as raw materials, and th...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C07C19/01C07C17/278
Inventor 马利勇李宏峰周强林晓云
Owner JUHUA GROUP TECH CENT