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Method for preparing 2-chloro-1,1,1,4,4,4-hexafluoro-2-butene

A technology of butene and trifluorobutane, which is applied in the field of liquid-phase fluorination to prepare 2-chloro-1,1,1,4,4,4-hexafluoro-2-butene, which can solve the problem of poor product selectivity, Poor thermal stability, short life and other problems, achieve high reaction selectivity, improve reaction selectivity, and long catalyst life

Active Publication Date: 2019-09-27
XIAN MODERN CHEM RES INST
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  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

[0003] Chinese patent CN 104072333B reports the synthesis of 2-chloro-1,1,1,4,4,4 by liquid-phase fluorination of hexachlorobutadiene and anhydrous hydrogen fluoride under the catalysis of antimony pentachloride at a reaction temperature of 100°C -hexafluoro-2-butene. Under this condition, antimony pentachloride has the disadvantages of reduced valence, inactivation, poor thermal stability, etc., and its life is extremely short, making it difficult to achieve large-scale synthesis; Synthesis of 2-chloro-1,1,1,4,4,4,4-hexafluoro-2-butene from dichloro-1,1,1,4,4,4-hexafluoro-2-butene by hydrodechlorination Butene, but because the hydrogenation reaction is difficult to control, the process has problems such as poor product selectivity

Method used

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  • Method for preparing 2-chloro-1,1,1,4,4,4-hexafluoro-2-butene

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Experimental program
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Effect test

Embodiment 1

[0017] The preparation of 2-chloro-1,1,1,4,4,4-hexafluoro-2-butene by liquid phase fluorination was carried out in a stirred 250mL stainless steel autoclave. Put 12.4g TiF into the reactor in sequence 4 , 5.1g triethylamine, 12g HF and 5.96g 1,1,1,3,3-pentachloro-4,4,4-trifluorobutane, the reaction temperature is 120°C, and the reaction is 5h. After the reaction, the sample was washed with water to remove acid and analyzed by gas chromatography. The results showed that the conversion rate of 1,1,1,3,3-pentachloro-4,4,4-trifluorobutane was 100%, and 2-chloro-1 , The selectivity of 1,1,4,4,4-hexafluoro-2-butene was 96.5%.

Embodiment 2~14

[0019] Examples 2-14 The preparation of 2-chloro-1,1,1,4,4,4-hexafluoro-2-butene by liquid phase fluorination reaction is the same as that of Example 1, except that the liquid phase composite catalyst group is changed Minutes, reaction temperature and reaction time, the reaction results are shown in Table 1.

[0020] Table 1

[0021]

Embodiment 15

[0023] In the reactor identical with embodiment 1. Add 19.0g TiCl to the reactor in sequence 4 , and then add 60g HF to carry out fluorination treatment. During the treatment process, the generated HCl is eliminated through the gas phase port, and the pressure is controlled within 0.20MPa. Raise the temperature to 90°C, keep the temperature constant for 2 hours, and the treatment process ends. Add 5.96g of 1,1,1,3,3-pentachloro-4,4,4-trifluorobutane into the reaction kettle, the reaction temperature is 120°C, and cool down after 2 hours of reaction. After the sample was washed with water to remove acid, the gas chromatography analysis showed that the conversion rate of 1,1,1,3,3-pentachloro-4,4,4-trifluorobutane was 100%, and 2-chloro-1,1,1, The selectivity of 4,4,4-hexafluoro-2-butene was 98.0%.

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Abstract

The invention discloses a method for preparing 2-chloro-1,1,1,4,4,4-hexafluoro-2-butene. The method comprises the steps: in the presence of a liquid phase composite catalyst, hydrogen fluoride and 1,1,1,3,3-pentachloro-4,4,4-trifluorobutane are subjected to liquid phase fluorination to prepare 2-chloro-1,1,1,4,4,4-hexafluoro-2-butene, wherein the molar ratio of HF to 1,1,1,3,3-pentachloro-4,4,4-trifluorobutane is (3 to 50):1, the molar ratio of 1,1,1,3,3-pentachloro-4,4,4-trifluorobutane to the liquid phase composite catalyst is (0.1 to 3):1, the reaction temperature is 50-150 DEG C, the reaction time is 0.5-10 h, the liquid phase composite catalyst consists of metal fluoride and a compounding agent, the metal fluoride is TaF5, NbF5, TiF4 or SnF4, the compounding agent is an organic amine or a quaternary ammonium salt, and the molar ratio of the compounding agent to the metal fluoride is (0-2):1. The invention is mainly used for preparing 2-chloro-1,1,1,4,4,4-hexafluoro-2-butene.

Description

technical field [0001] The present invention relates to a method for preparing 2-chloro-1,1,1,4,4,4-hexafluoro-2-butene, in particular to 1,1,1,3,3-pentachloro-4, A method for preparing 2-chloro-1,1,1,4,4,4-hexafluoro-2-butene by liquid-phase fluorination of 4,4-trifluorobutane as a raw material. Background technique [0002] cis-1,1,1,4,4,4-hexafluoro-2-butene (Z-HFO-1336mzz) has the same foaming, heat insulation and heat preservation properties as traditional foaming agents, and its ozone depletion potential (ODP ) is zero, the greenhouse effect potential value (GWP) is 9, has little impact on the environment, and is regarded as a new generation of green and environmentally friendly blowing agent. As an important intermediate in the synthesis of Z-HFO-1336mzz, the large-scale synthesis of 2-chloro-1,1,1,4,4,4-hexafluoro-2-butene is the key to the industrial preparation of Z-HFO-1336mzz One of the techniques. [0003] Chinese patent CN 104072333B reports the synthesis of...

Claims

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Application Information

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IPC IPC(8): C07C17/20C07C17/25C07C21/18
CPCC07C17/206C07C17/25C07C21/18
Inventor 韩升吕剑赵波曾纪珺张伟杨志强唐晓博郝志军亢建平李凤仙淡保松
Owner XIAN MODERN CHEM RES INST
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