IP Library Granted Patent US 7,285,692
Granted Patent B2
US 7,285,692 · App. 10/572,626 · Granted Oct 23, 2007

Process for the preparation of 1,1,1,3,3-pentafluoropropane and 1,1,1,2,3-pentafluoropropane

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Quick Facts
Patent No.
US 7,285,692
App. No.
10/572,626
Granted
Oct 23, 2007
Kind
B2
Abstract

A process is disclosed for the manufacture of CF 3 CH 2 CHF 2 and CF 3 CHFCH 2 F. The process involves (a) reacting hydrogen fluoride, chlorine, and at least one halopropene of the formula CX 3 CCl═CClX (where each X is independently F or Cl) to produce a product including both CF 3 CCl 2 CClF 2 and CF 3 CClFCCl 2 F; (b) reacting CF 3 CCl 2 CClF 2 and CF 3 CClFCCl 2 F produced in (a) with hydrogen to produce a product including both CF 3 CH 2 CHF 2 , and CF 3 CHFCH 2 F; and (c) recovering CF 3 CH 2 CHF 2 and CF 3 CHFCH 2 F from the product produced in (b). In (a), the CF 3 CCl 2 CClF 2 and CF 3 CClFCCl 2 F are produced in the presence of a chlorofluorination catalyst including a ZnCr 2 O 4 /crystalline α-chromium oxide composition, a ZnCr 2 O 4 /crystalline α-chromium oxide composition which has been treated with a fluorinating agent, a zinc halide/α-chromium oxide composition and/or a zinc halide/α-chromuim oxide composition which has been treated with a fluorinating agent.

Claims (10)

1. A process for the manufacture of 1,1,1,3,3-pentafluoropropane and 1,1,1,2,3-pentafluoropropane, comprising:

(a) reacting hydrogen fluoride, chlorine, and at least one halopropene of the formula CX 3 CCl═CClX, wherein each X is independently selected from the group consisting of F and Cl, to produce a product comprising CF 3 CCl 2 CClF 2 and CF 3 CClFCCl 2 F, wherein said CF 3 CCl 2 CClF 2 and CF 3 CClFCCl 2 F are produced in the presence of a chlorofluorination catalyst comprising at least one composition selected from the group consisting of (i) compositions comprising ZnCr 2 O 4 and crystalline α-chromium oxide, (ii) compositions comprising a zinc halide and α-chromium oxide and (iii) compositions of (i) or (ii) which have been treated with a fluorinating agent;

(b) reacting CF 3 CCl 2 CClF 2 and CF 3 CClFCCl 2 F produced in (a) with hydrogen to produce a product comprising CF 3 CH 2 CHF 2 and CF 3 CHFCH 2 F; and

(c) recovering CF 3 CH 2 CHF 2 and CF 3 CHFCH 2 F from the product produced in (b).

2. The process of claim 1 wherein in (a) the catalyst is selected from the group consisting of (i) compositions comprising ZnCr 2 O 4 and crystalline α-chromium oxide and (iii) compositions of (i) which have been treated with a fluorinating agent.

3. The process of claim 2 wherein the amount of zinc relative to the total of chromium and zinc in the catalyst composition is from about 1 atom % to about 25 atom %.

4. The process of claim 2 wherein the catalyst is selected from the group consisting of (i) compositions comprising ZnCr 2 O 4 and crystalline α-chromium oxide wherein the ZnCr 2 O 4 contains between about 10 atom percent and 67 atom percent of the chromium in the composition and at least about 70 atom percent of the zinc in the composition, and wherein at least about 90 atom percent of the chromium present as chromium oxide in the composition is present as ZnCr 2 O 4 or crystalline α-chromium oxide and (iii) compositions of (i) which have been treated with a fluorinating agent.

5. The process of claim 1 wherein in (a) the catalyst is selected from the group consisting of (ii) compositions comprising a zinc halide and α-chromium oxide and (iii) compositions of (ii) which have been treated with a fluorinating agent.

6. The process of claim 5 wherein the amount of zinc relative to the total of chromium and zinc in the catalyst composition is from about 0.1 atom % to about 25 atom %.

7. The process of claim 5 wherein the catalyst is selected from the group consisting of (ii) compositions wherein a zinc halide is supported on a support comprising α-chromium oxide and (iii) compositions of (ii) which have been treated with a fluorinating agent; and wherein the amount of zinc relative to the total of chromium and zinc in the catalyst composition is from about 2 atom % to about 10 atom %.

Assignments (4)
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 →
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 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 →