IP Library Granted Patent US 7,723,552
Granted Patent B2
US 7,723,552 · App. 12/537,805 · Granted May 25, 2010

Process for making chlorotrifluoroethylene from 1,1,2-Trichlorotrifluoroethane

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Quick Facts
Patent No.
US 7,723,552
App. No.
12/537,805
Granted
May 25, 2010
Kind
B2
Abstract

A process for the making chlorotrifluoroethylene. The process has the step of reacting 1,1,2-trichlorotrifluoroethane with a reducing metal in the presence of a polar aprotic solvent under conditions sufficient to form chlorotrifluoroethylene.

Claims (18)

1. A process for the making chlorotrifluoroethylene, comprising reacting 1,1,2-trichlorotrifluoroethane with a reducing metal in the presence of one or more polar aprotic solvents and one or more protic co-solvents under conditions sufficient to form chlorotrifluoroethylene.

2. The process of claim 1 , wherein the mixture has about 1 wt. % to about 80 wt. % of the one or more protic solvents based on the total weight of the mixture of the one or more polar aprotic solvents and the one or more protic co-solvents.

3. The process of claim 1 , wherein the mixture has about 5 wt. % to about 40 wt. % of the one or more protic solvents based on the total weight of the aprotic solvent(s) and the protic co-solvent(s).

4. The process of claim 1 , wherein the one or more polar aprotic solvents is selected from the group consisting of aldehydes, ketones, dimethyl sulfoxide, dimethyl formamide, and combinations thereof.

5. The process of claim 1 , wherein the one or more polar aprotic solvents is selected from the group consisting of ethyl ether, ethyl acetate, acetone, methyl ethyl ketone, and combinations thereof.

6. The process of claim 1 , wherein the polar aprotic solvent is ethyl acetate.

7. The process of claim 1 , wherein the polar aprotic solvent is acetone.

8. The process of claim 1 , wherein the polar aprotic solvent is methyl ethyl ketone.

9. The process of claim 1 , wherein the polar aprotic solvent is ethyl ether.

10. The process of claim 1 , wherein the protic solvent is selected from the group consisting of methanol, ethanol, propanol, isopropanol, and water.

11. The process of claim 10 , wherein the protic solvent is water.

12. The process of claim 1 , wherein the reducing metal is selected from the group consisting of zinc, magnesium, aluminum, and tin.

13. The process of claim 1 , wherein the reducing metal is zinc.

14. The process of claim 1 , wherein the reaction is carried out at a temperature of about 50° C. to about 100° C.

15. The process of claim 1 , wherein the reaction is carried out at a temperature of about 60° C. to about 90° C.

16. The process of claim 1 , wherein the reaction is most preferably carried out at a temperature of about 60° C. to about 85° C.

17. The process of claim 1 , wherein the reaction is carried out in batch.

18. The process of claim 1 , wherein the mixture has about 5 wt. % to about 40 wt. % of the one or more protic solvents based on the total weight of the aprotic solvent(s) and the protic co-solvent(s), wherein the one or more polar aprotic solvents is selected from the group consisting of ethyl ether, ethyl acetate, acetone, methyl ethyl ketone, and combinations thereof, wherein the protic solvent is selected from the group consisting of methanol, ethanol, propanol, isopropanol, and water wherein the reducing metal is selected from the group consisting of zinc, magnesium, aluminum, and tin, and wherein the reaction is carried out at a temperature of about 50° C. to about 100° C.

Assignments (2)
SECURITY INTEREST Recorded Jan 12, 2026
From: SOLSTICE ADVANCED MATERIALS US, INC.
To: JPMORGAN CHASE BANK, N.A., AS ADMINISTRATIVE AGENT
Reel/Frame 074569/0260 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Aug 7, 2009
From: MURPHY, MICHAEL JOHN; BEKTESEVIC, SELMA
To: HONEYWELL INTERNATIONAL INC.
Reel/Frame 023070/0265 →