IP Library Granted Patent US 8,318,992
Granted Patent B2
US 8,318,992 · App. 12/444,462 · Granted Nov 27, 2012

Processes for the production of fluoropropanes and halopropenes

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Quick Facts
Patent No.
US 8,318,992
App. No.
12/444,462
Granted
Nov 27, 2012
Kind
B2
Abstract

A process is disclosed for making CF 3 CF 2 CH 3 , CF 3 CF═CH 2 and/or CF 3 CCl═CH 2 . The process involves reacting at least one starting material selected from the group consisting of halopropanes of the formula CX 3 CH 2 CH 2 X, halopropenes of the formula CX 3 CH═CH 2 and halopropenes of the formula CX 2 ═CHCH 2 X, wherein each X is independently F or Cl, with HF and Cl 2 in a reaction zone to produce a product mixture comprising HF, HCl, CF 3 CF 2 CH 3 , CF 3 CF═CH 2 , and CF 3 CCl═CH 2 ; and recovering the CF 3 CF 2 CH 3 , CF 3 CF═CH 2 and/or CF 3 CCl═CH 2 from the product mixture. Also disclosed is a process for making CF 3 CH 2 CHF 2 , CF 3 CH═CHF, and/or CF 3 CH═CHCl. This process involves reacting at least one starting material selected from the group consisting of halopropenes of the formula CX 3 CH═CH 2 and halopropenes of the formula CX 2 ═CHCH 2 X, wherein each X is independently F or Cl, with HF and Cl 2 in a reaction zone to produce a product mixture comprising HF, HCl, CF 3 CH 2 CHF 2 , CF 3 CH═CHF and CF 3 CH═CHCl; and recovering the CF 3 CH 2 CHF 2 , CF 3 CH═CHF, and/or CF 3 CH═CHCl from the product mixture. The molar ratio of HF to the total amount of starting materials fed to the reaction zone for both of these processes is at least stoichiometric, and the molar ratio of Cl 2 to total amount of starting material fed to the reaction zone for both of these processes is 2:1 or less.

Claims (22)

1. A process for making at least one product compound selected from the group consisting of CF 3 CF 2 CH 3 , CF 3 CF═CH 2 and CF 3 CCl═CH 2 , comprising:

reacting at least one starting material selected from the group consisting of halopropanes of the formula CX 3 CH 2 CH 2 X, halopropenes of the formula CX 3 CH═CH 2 and halopropenes of the formula CX 2 ═CHCH 2 X, wherein each X is independently selected from the group consisting of F and Cl, with HF and Cl 2 in a reaction zone, optionally in the presence of a chlorofluorination catalyst, to produce a product mixture comprising at least one product compound selected from the group consisting of CF 3 CF 2 CH 3 , CF 3 CF═CH 2 and CF 3 CCl═CH 2 , wherein the molar ratio of HF to total amount of starting material fed to the reaction zone is at least stoichiometric and wherein the molar ratio of Cl 2 to total amount of starting material fed to the reaction zone is 2:1 or less; and

recovering said at least one product compound from the product mixture.

2. The process of claim 1 wherein CF 3 CF═CH 2 is recovered.

3. The process of claim 2 wherein CF 3 CF 2 CH 3 from the product mixture is dehydrofluorinated to produce additional CF 3 CF═CH 2 .

4. The process of claim 1 wherein CF 3 CCl═CH 2 from the product mixture is fluorinated to produce at least one of CF 3 CF═CH 2 and CF 3 CF 2 CH 3 .

5. The process of claim 1 wherein the product mixture further comprises CF 3 CH═CHF; and wherein CF 3 CH═CHF from the product mixture is recovered.

6. The process of claim 1 wherein the product mixture further comprises CF 3 CH═CHCl; and wherein CF 3 CH═CHCl from the product mixture is fluorinated to produce at least one of CF 3 CH═CHF and CF 3 CH 2 CHF 2 .

7. The process of claim 1 wherein the product mixture further comprises CF 3 CH 2 CHF 2 ; and wherein CF 3 CH 2 CHF 2 from the product mixture is recovered.

8. The process of claim 1 wherein the product mixture further comprises CF 3 CH 2 CHF 2 ; and wherein CF 3 CH 2 CHF 2 from the product mixture is dehydrofluorinated to produce CF 3 CH═CHF.

9. The process of claim 1 wherein the product mixture further comprises CF 3 CH═CHF; and wherein a mixture of CF 3 CF 2 CH 3 and CF 3 CH═CHF is recovered and further reacted under dehydrofluorination conditions in the presence of a dehydrofluorination catalyst to produce a mixture comprising CF 3 CH═CHF and CF 3 CF═CH 2 .

10. The process of claim 1 wherein the product mixture further comprises CF 3 CH 2 CHF 2 and CF 3 CH═CHCl; and wherein the CF 3 CCl═CH 2 , CF 3 CH 2 CHF 2 and CF 3 CH═CHCl from the product mixture are further reacted with HF in the liquid phase under fluorination conditions in the presence of a fluorination catalyst to produce a mixture comprising CF 3 CH 2 CHF 2 and CF 3 CF 2 CH 3 .

11. The process of claim 1 wherein the starting material is reacted in the vapor phase in the presence of a chlorofluorination catalyst.

12. The process of claim 11 wherein the chlorofluorination catalyst comprises at least one chromium-containing component selected from the group consisting of crystalline alpha-chromium oxide where from about 0.05 atom % to about 6 atom % of the chromium atoms in the alpha-chromium oxide lattice are replaced by trivalent cobalt atoms, and crystalline alpha-chromium oxide where from about 0.05 atom % to about 6 atom % of the chromium atoms in the alpha-chromium oxide lattice are replaced by trivalent cobalt atoms which has been treated with a fluorinating agent.

13. A process for making at least one product compound selected from the group consisting of CF 3 CF 2 CH 3 , CF 3 CF═CH 2 and CF 3 CCl═CH 2 , comprising:

reacting at least one starting material selected from the group consisting of halopropanes of the formula CX 3 CH 2 CH 2 X, halopropenes of the formula CX 3 CH═CH 2 and halopropenes of the formula CX 2 ═CHCH 2 X, wherein each X is independently selected from the group consisting of F and Cl, with HF and Cl 2 in a reaction zone, in the presence of a chlorofluorination catalyst, to produce a product mixture comprising HF, HCl, CF 3 CF 2 CH 3 , CF 3 CF═CH 2 and CF 3 CCl═CH 2 , wherein the molar ratio of HF to total amount of starting material fed to the reaction zone is at least stoichiometric and wherein the molar ratio of Cl 2 to total amount of starting material fed to the reaction zone is 2:1 or less; and

recovering said at least one product compound from the product mixture.

14. The process of claim 13 wherein said at least one starting material is halopropenes of the formula CX 3 CH═CH 2 .

15. The process of claim 14 wherein said at least one starting material is CF 3 CH═CH 2 .

16. A process for making at least one product compound selected from the group consisting of CF 3 CF 2 CH 3 , CF 3 CF═CH 2 , CF 3 CCl═CH 2 , CF 3 CH 2 CHF 2 , CF 3 CH═CHF and CF 3 CH═CHCl, comprising:

reacting at least one starting material selected from the group consisting of halopropanes of the formula CX 3 CH 2 CH 2 X, halopropenes of the formula CX 3 CH═CH 2 and halopropenes of the formula CX 2 ═CHCH 2 X, wherein each X is independently selected from the group consisting of F and Cl, with HF and Cl 2 in a reaction zone, in the presence of a chlorofluorination catalyst, to produce a product mixture comprising CF 3 CF 2 CH 3 , CF 3 CF═CH 2 , CF 3 CCl═CH 2 , CF 3 CH 2 CHF 2 , CF 3 CH═CHF and CF 3 CH═CHCl, wherein the molar ratio of HF to total amount of starting material fed to the reaction zone is at least stoichiometric and wherein the molar ratio of Cl 2 to total amount of starting material fed to the reaction zone is 2:1 or less; and

recovering said at least one product compound from the product mixture.

Assignments (4)
RELEASE OF SECURITY INTEREST Recorded Apr 4, 2018
From: JPMORGAN CHASE BANK, N.A., AS ADMINISTRATIVE AGENT
To: THE CHEMOURS COMPANY FC, LLC
Reel/Frame 045845/0913 →
SECURITY INTEREST Recorded Apr 4, 2018
From: THE CHEMOURS COMPANY FC, LLC
To: JPMORGAN CHASE BANK, N.A., AS ADMINISTRATIVE AGENT
Reel/Frame 045846/0011 →
SECURITY AGREEMENT Recorded Jun 10, 2015
From: THE CHEMOURS COMPANY FC LLC; THE CHEMOURS COMPANY TT, LLC
To: JPMORGAN CHASE BANK, N.A.
Reel/Frame 035839/0675 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Apr 15, 2015
From: E. I. DU PONT DE NEMOURS AND COMPANY
To: THE CHEMOURS COMPANY FC, LLC
Reel/Frame 035432/0023 →