IP Library Granted Patent US 10,399,915
Granted Patent B2
US 10,399,915 · App. 15/929,024 · Granted Sep 3, 2019

Manufacturing method of 1-chloro-2,3,3,3-tetrafluoropropene

Inventors: Tomoaki Taniguchi (Chiyoda-ku, JP); Shoji Furuta (Chiyoda-ku, JP); Hidefumi Shiota (Chiyoda-ku, JP)
Assignee: AGC Inc.
C07C17/25C07C17/04C07C19/10C07C21/18C07B61/00
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Quick Facts
Patent No.
US 10,399,915
App. No.
15/929,024
Granted
Sep 3, 2019
Kind
B2
Abstract

There is provided an economically advantageous manufacturing method capable of efficiently obtaining 1-chloro-2,3,3,3-tetrafluoropropene by using 1,2-dichloro-2,3,3,3-tetrafluoropropane as a raw material. A manufacturing method of 1-chloro-2,3,3,3-tetrafluoropropene is characterized in that it includes subjecting 1,2-dichloro-2,3,3,3-tetrafluoropropane to a dehydrochlorination reaction in a liquid phase in a presence of a base.

Claims (24)

1. A manufacturing method of 1-chloro-2,3,3,3-tetrafluoropropene, comprising;

subjecting 1,2-dichloro-2,3,3,3-tetrafluoropropane to a dehydrochlorination reaction at a reaction temperature of 50 to 100° C. in a liquid phase in the presence of a base.

2. The manufacturing method according to claim 1 , wherein

1,2-dichloro-2,3,3,3-tetrafluoropropane is subjected to the dehydrochlorination reaction in the liquid phase in the presence of a solvent to dissolve the base, and the base.

3. The manufacturing method according to claim 1 , wherein

the base is selected from a group consisting of a metal hydroxide, a metal oxide, and a metal carbonate, or a mixture thereof.

4. The manufacturing method according to claim 1 , wherein

the base is used in a ratio of 0.2 to 2.5 mol with respect to 1 mol of the 1,2-dichloro-2,3,3,3-tetrafluoropropane.

5. The manufacturing method according to claim 1 , wherein

a reaction temperature in the dehydrochlorination reaction is 60 to 100° C.

6. The manufacturing method according to claim 2 , wherein

the solvent is water.

7. The manufacturing method according to claim 2 , wherein

an amount of the base is 10 to 50 mass % with respect to total mass of the solvent and the base.

8. The manufacturing method according to claim 1 , wherein

the dehydrochlorination reaction is performed in a presence of a phase-transfer catalyst.

9. The manufacturing method according to claim 8 , wherein

the phase-transfer catalyst is a quaternary ammonium salt.

10. The manufacturing method according to claim 9 , wherein

the quaternary ammonium salt is selected from a group consisting of tetra-n-butylammonium chloride, tetra-n-butylammonium bromide, and methyltri-n-octylammonium chloride, or a mixture thereof.

11. The manufacturing method according to claim 1 , further comprising;

reacting 2,3,3,3-tetrafluoropropene with chlorine to produce 1,2-dichloro-2,3,3,3-tetrafluoropropane.

12. The manufacturing method according to claim 11 , wherein

a reaction of the 2,3,3,3-tetrafluoropropene and chlorine is caused under irradiation of light in a wavelength region of 400 to 750 nm.

Assignments (2)
CHANGE OF NAME Recorded Sep 7, 2018
From: ASAHI GLASS COMPANY, LIMITED
To: AGC INC.
Reel/Frame 047278/0081 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Jun 20, 2018
From: TANIGUCHI, TOMOAKI; FURUTA, SHOJI; SHIOTA, HIDEFUMI
To: ASAHI GLASS COMPANY, LIMITED
Reel/Frame 046148/0233 →
Priority Claims (1)
JP 2015-254136 · Dec 25, 2015 · national
Continuity (2)
Continuation PCTJP2016088052 · Dec 21, 2016
Related Publication 20180297918A1 · Oct 18, 2018