Method for preparing 2,3,3,3-tetrafluoropropene using methyl magnesium chloride

Abstract

The present invention discloses a method for preparing 2,3,3,3-tetrafluoropropene using methylmagnesium chloride, comprising the following steps: 1) preparing 1,1,2-trifluoropropene (CH.sub.3CFCF.sub.2); 2) preparing 1,1,1,2,2-pentafluoropane (CF.sub.3CF.sub.2CH.sub.3); 3) preparing 2,3,3,3-tetrafluoropropene (CF.sub.3CFCH.sub.2). In the present invention, using a Grignard reagent, namely methylmagnesium chloride, and tetrafluoroethylene as starting raw materials, 2,3,3,3-tetrafluoropropene is prepared by three steps of nucleophilic addition-elimination, fluorine addition, and dehydrofluorination in sequence. The process flow is relatively short, and the product yield is high.

Claims

1. A method for preparing 2,3,3,3-tetrafluoropropene by using methylmagnesium chloride, characterized by comprising the following steps: 1) preparing 1,1,2-trifluoropropene (CH.sub.3CFCF.sub.2), wherein tetrafluoroethylene and a Grignard reagent, namely methylmagnesium chloride, react in a first organic solvent to obtain 1,1,2-trifluoropropene, wherein the molar ratio of the methylmagnesium chloride to the tetrafluoroethylene is 1:1-1:5, the reaction temperature is from 20 C. to 40 C.; 2) preparing 1,1,1,2,2-pentafluoropane (CF.sub.3CF.sub.2CH.sub.3) by: adding a second organic solvent and the 1,1,2-trifluoropropene obtained in step 1) at a temperature of 30 C. into a reactor with a stirrer, wherein the mass ratio of the 1,1,2-trifluoropropene to the second organic solvent is 1:0.5-1:5; controlling the reaction temperature; adding continuously a mixture of fluorine and nitrogen gases into the reactor, wherein the molar ratio of the 1,1,2-trifluoropropene to the fluorine gas is 1:1-1:1.2; stopping the reaction when the amount of the input fluorine gas reaches a predetermined value; blowing the residual fluorine gas with nitrogen gas; rectifying the reaction liquid; obtaining the 1,1,1,2,2-pentafluoropane; 3) preparing 2,3,3,3-tetrafluoropropene (CF.sub.3CFCH.sub.2) by: adding 1,1,1,2,2-pentafluoropane obtained in step 2) into a reactor containing an alkaline solution, wherein the concentration of the alkaline solution is 10-50%, and the reaction temperature is 50-90 C.; drying a gas product to obtain the product 2,3,3,3-tetrafluoropropene.

2. The method for preparing 2,3,3,3-tetrafluoropropene by using methylmagnesium chloride according to claim 1, characterized in that the first organic solvent in step 1) is any one of tetrahydrofuran, diethyl ether and glycol dimethyl ether.

3. The method for preparing 2,3,3,3-tetrafluoropropene by using methylmagnesium chloride according to claim 1, characterized in that the second organic solvent in step 2) is any one of 1,1,2-trichlorotrifluoroethane, perfluoro-n-butane, perfluorohexane and perfluorooctane.

4. The method for preparing 2,3,3,3-tetrafluoropropene by using methylmagnesium chloride according to claim 1, characterized in that the mixture of fluorine and nitrogen gases in step 2) contains 5-30% of fluorine gas.

5. The method for preparing 2,3,3,3-tetrafluoropropene by using methylmagnesium chloride according to claim 1, characterized in that the alkaline solution in step 3) is potassium hydroxide, sodium hydroxide or a mixture thereof.

Description

DETAILED DESCRIPTION OF THE INVENTION

(1) The present invention provides a method for preparing 2,3,3,3-tetrafluoropropene by using methylmagnesium chloride, comprising the following steps:

(2) 1) preparing 1,1,2-trifluoropropene (CH.sub.3CFCF.sub.2)

(3) wherein tetrafluoroethylene and the Grignard reagent, namely methylmagnesium chloride, react in an organic solvent to obtain 1,1,2-trifluoropropene, wherein the organic solvent is any one of tetrahydrofuran, diethyl ether and glycol dimethyl ether, which can effectively enhance the reaction degree of the tetrafluoroethylene and the Grignard reagent, and the organic solvent serves as a catalyst, promoting smooth reaction, the molar ratio of methylmagnesium chloride to tetrafluoroethylene is 1:1-1:5, the reaction temperature is 20-40 C.; the reaction pressure is 1-3 Mpa, the main side product is CH.sub.3CFCFCF.sub.2CF.sub.2CH.sub.3;

(4) 2) preparing 1,1,1,2,2-pentafluoropane (CF.sub.3CF.sub.2CH.sub.3)

(5) wherein at a temperature of 30 C., the solvent and 1,1,2-trifluoropropene obtained in step 1) are added into a reactor with a stirrer, wherein the solvent is any one of 1,1,2-trichlorotrifluoroethane, perfluoro-n-butane, perfluorohexane and perfluorooctane which are fully halogenated solvents, ensuring that the reaction in step 2) proceeds in a tender state; the reaction temperature is controlled; then, the mixture of fluorine and nitrogen gases is continuously input into the reactor, and a reaction proceeds, wherein the mixture of fluorine and nitrogen gases contains 5-30% of fluorine gas, ensuring that the reaction in step 2) proceeds in a tender state, and improving safety, the mass ratio of 1,1,2-trifluoropropene to solvent is 1:0.5-1:5, the molar ratio of 1,1,2-trifluoropropene to fluorine gas is 1:1-1:1.2; when the amount of the input fluorine gas reaches a predetermined value, the reaction is stopped; the residual fluorine gas is blown using the nitrogen gas; the reaction liquid is rectified, and then the 1,1,1,2,2-pentafluoropane is obtained;

(6) 3) preparing 2,3,3,3-tetrafluoropropene (CF.sub.3CFCH.sub.2)

(7) wherein the 1,1,1,2,2-pentafluoropane obtained in step 2) is input into the reactor containing an alkaline solution, and then a reaction proceeds, wherein the alkaline solution is potassium hydroxide, sodium hydroxide or a mixture thereof; a gas product is dried and compressed to obtain the product 2,3,3,3-tetrafluoropropene, wherein the concentration of the alkaline solution is 10-50%, and the reaction temperature is 50-90 C.

(8) In the present invention, CH.sub.3MgCl and CF.sub.2CF.sub.2 react to synthesize CH.sub.3CF.sub.2CF.sub.2MgCl, but CH.sub.3CF.sub.2CF.sub.2MgCl itself is unstable and quickly performs the elimination reaction to generate CH.sub.3CFCF.sub.2; then, CH.sub.3CFCF.sub.2 and F.sub.2/N.sub.2 react at a low-temperature solvent to generate CH.sub.3CF.sub.2CF.sub.3; and finally, CH.sub.3CF.sub.2CF.sub.3 is removed from HF using the alkaline solution to synthesize and obtain CF.sub.3CFCH.sub.2. The reaction path is as follows.

(9) ##STR00002##

Embodiment 1

(10) 1) Preparation of 1,1,2-trifluoropropene

(11) A 2 L stainless steel high-pressure reactor was filled with the nitrogen gas three times to exchange the air therein; then 250 g (2 mol/Kg) of methylmagnesium chloride, namely the Grignard reagent, and 750 g of tetrahydrofuran were added into the reactor; the mixed materials were stirred while cooled; at the temperature of 13 C., 120 g of tetrafluoroethylene was input with stirring. After the tetrafluoroethylene was added, the mixed materials were slowly heated until the temperature in the container rose to 40 C., and the reaction proceeded for 5 h at the temperature of 40 C. When the reaction ended, heating was stopped and the materials were stirred. The residual tetrafluoroethylene is drained and then the materials were discharged. Then, the 1,1,2-trifluoropropene synthesizing liquid was obtained at a yield of 90.3%. After rectification and purification, the purity of the obtained product was 99.5%.

(12) 2) Preparation of 1,1,1,2,2-pentafluoropropane

(13) An identical 2 L stainless steel high-pressure reactor was degreased and passivated with the fluorine gas, and then added with 1,000 g of the solvent, 1,1,2-trichlorotrifluoroethane, 500 g (5.21 mol) of 1,1,2-trifluoropropene; the reactor was continuously cooled until the temperature reached 60 C., and 15% mixture of the fluorine and nitrogen gases was continuously input into the reactor within 2 h by using a flowmeter. When the amount of the input fluorine gas reached 5.47 mol, the reaction was stopped, and the residual fluorine gas was blown with the nitrogen gas. The reaction yield was 92%. After rectification, the 1,1,1,2,2-pentafluoropropane with a purity of 99.5% was obtained.

(14) 3) Preparation of 2,3,3,3-tetrafluoropropene

(15) The 1,1,1,2,2-pentafluoropropane obtained in step 2 passed through 40% potassium hydroxide solution at a temperature of 70 C.; the reaction product was dried, condensed and collected, and then the 2,3,3,3-tetrafluoropropene product with a purity of 99.5% was obtained at a yield of 98.2%.

(16) The total yield of the three reaction steps was 81.6%.

Embodiment 2

(17) 1) Preparation of 1,1,2-trifluoropropene

(18) The materials used in step 1 of embodiment 1 were replaced by 250 g (2 mol/Kg) of methylmagnesium chloride, 750 g of tetrahydrofuran and 250 g of tetrafluoroethylene. Other conditions were identical with the corresponding conditions in step 1 of embodiment 1. The 1,1,2-trifluoropropene synthesizing liquid was obtained at a yield of 93.6%.

(19) 2) Preparation of 1,1,1,2,2-pentafluoropropane

(20) The materials used in step 2 of embodiment 1 were replaced by 1,000 g of solvent, namely 1,1,2-trichlorotrifluoroethane, 500 g (5.21 mol) of 1,1,2-trifluoropropene, and 5% mixture of fluorine and nitrogen gases that has a total fluorine gas content of 6.25 mol. Other conditions were identical with the corresponding conditions in step 2 of embodiment 1. The reaction yield of the 1,1,1,2,2-pentafluoropane was 95.4%.

(21) 3) Preparation of 2,3,3,3-tetrafluoropropene

(22) The concentration of the alkaline solution used in step 3 of embodiment 1 was changed into 60%, and the 2,3,3,3-tetrafluoropropene yield was 99.1%.

(23) The total yield of the three reaction steps was 88.5%.

Embodiment 3

(24) 1) Preparation of 1,1,2-trifluoropropene

(25) The temperature of the 1,1,2-trifluoropropene synthesis reaction in step 1 of embodiment 1 was changed into 10 C. Other conditions were identical with the corresponding conditions in step 1 of embodiment 1. The 1,1,2-trifluoropropene synthesizing liquid was obtained at a yield of 86.7%.

(26) 2) Preparation of 1,1,1,2,2-pentafluoropropane

(27) The fluorine gas in step 2 of embodiment 1 was changed into 30% mixture of fluorine and nitrogen gases, and the input amount was unchanged. Other conditions were identical with the corresponding conditions in step 2 of embodiment 1. The reaction yield of the 1,1,1,2,2-pentafluoropane was 89.3%.

(28) 3) Preparation of 2,3,3,3-tetrafluoropropene

(29) The reaction temperature in step 3 of embodiment 1 was changed into 90 C. Other conditions were identical with the corresponding conditions in step 1 of embodiment 3. The 2,3,3,3-tetrafluoropropene was obtained at a yield of 99.2%.

(30) The total yield of the three reaction steps was 76.8%.

Embodiment 4

(31) The preparation of the 1,1,2-trifluoropropene was identical with the reaction step 1 of embodiment 2. The reaction temperature duration preparation of the 1,1,1,2,2-pentafluoropane was changed into 30 C., other conditions were identical with the corresponding conditions of embodiment 1, and the yield was 91%. The preparation of 2,3,3,3-tetrafluoropropene was identical with embodiment 1. The total yield of the three reaction steps was 83.6%.

Embodiment 5

(32) The preparation of the 1,1,2-trifluoropropene was identical with the reaction step 1 of embodiment 2. The solvent used to prepare the 1,1,1,2,2-pentafluoropane was changed into 1,200 g perfluorooctane, other conditions were identical with the corresponding conditions of embodiment 1, and the yield was 94.7%. The preparation of 2,3,3,3-tetrafluoropropene was identical with embodiment 1. The total yield of the three reaction steps was 87%.

Embodiment 6

(33) The solvent used in step 2 of embodiment 1 was changed into 1,500 g carbon tetrachloride; the alkaline solution in step 3 was changed into 15% sodium hydroxide solution; step 1 and other conditions were identical with those of embodiment 1. The yields of the 1,1,1,2,2-pentafluoropane and 2,3,3,3-tetrafluoropropene were respectively 87.1% and 94.8%. The total yield of the three reaction steps was 74.6%.

(34) Comparative Example 1

(35) A 2 L stainless steel high-pressure reactor was degreased, passivated with the fluorine gas, cooled to 60 C., and then added with 500 g (5.21 mol) of 1,1,2-trifluoropropene; and 15% mixture of the fluorine and nitrogen gases was continuously input into the reactor within 2 h by using a flowmeter. When the amount of the input fluorine gas reached 5.47 mol, the reaction was stopped, and the residual fluorine gas was blown with the nitrogen gas. The 1,1,1,2,2-pentafluoropane has a selectivity of 81% and a yield of 78%. Other side products include 1,1,1,2,2,3-hexafluoropropane, 1,1,1,2,2,3,3-heptafluoropropane, 1,1,1,1,2,2,3,3,3-octafluoropropane, 1,1,2,3-tetrafluoropropene, 1,1,2,3,3-pentafluoropropene, 1,1,2,3,3,3-hexafluoropropylene, etc.

(36) The above are specific embodiments of the present invention only, but the technical characteristics of the present invention are not limited to the above embodiment. Any simple changes, equivalent substitution or modifications on the basis of the present invention to realize the basically the same technical effects shall be incorporated into the protective scope of the present invention.