IP Library Granted Patent US 8,487,145
Granted Patent B2
US 8,487,145 · App. 13/417,582 · Granted Jul 16, 2013

Catalysts and process to manufacture 2,3,3,3-tetrafluoropropene

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Quick Facts
Patent No.
US 8,487,145
App. No.
13/417,582
Granted
Jul 16, 2013
Kind
B2
Abstract

Disclosed is a process for the manufacture of 2,3,3,3-tetrafluoropropene comprising: (a) contacting 1,1,1,2,3-pentafluoropropane with a catalyst comprised of chromium (III) oxide having a surface area of at least 150 m 2 /g and having an alkali metal loading of at least 7 milligrams of alkali metal per 100 square meters of catalyst surface area, to produce a product mixture comprising 2,3,3,3-tetrafluoropropene and hydrogen fluoride; and (b) recovering said 2,3,3,3-tetrafluoropropene from the product mixture produced in (a).

Claims (9)

1. A process for the manufacture of 2,3,3,3-tetrafluoropropene comprising: (a) contacting 1,1,1,2,3-pentafluoropropane with a catalyst comprised of chromium (III) oxide having a surface area of at least 150 m 2 /g and having an alkali metal loading of at least 7 milligrams of alkali metal per 100 square meters of catalyst surface area, to produce a product mixture comprising 2,3,3,3-tetrafluoropropene and hydrogen fluoride; and (b) recovering said 2,3,3,3-tetrafluoropropene from the product mixture produced in (a).

2. The process of claim 1 , wherein said alkali metal is potassium.

3. A process of claim 1 , wherein said product mixture comprising 2,3,3,3-tetrafluoropropene comprises less than 20 parts per hundred on a molar basis of 1,1,1,2,2-pentafluoropropane.

4. The process of claim 1 , wherein said product mixture comprising 2,3,3,3-tetrafluoropropene comprises less than 10 parts per hundred on a molar basis of 1,1,1,2,2-pentafluoropropane.

5. The process of claim 1 , wherein the catalyst has a surface area of at least 200 m 2 /g.

6. The process of claim 1 , wherein the catalyst has an alkali metal loading of at least 8 milligrams of alkali metal per 100 square meters of catalyst surface area.

7. The process of claim 1 , wherein the catalyst has an alkali metal loading of at least 9 milligrams of alkali metal per 100 square meters of catalyst surface area.

8. The process of claim 1 , wherein the temperature of the catalyst is maintained at a set point of from 250° C. to 350° C.

9. The process of claim 6 , wherein the temperature of the catalyst is maintained at a set point of from 250° C. to 300° C.

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 →