IP Library Granted Patent US 8,618,339
Granted Patent B2
US 8,618,339 · App. 12/110,890 · Granted Dec 31, 2013

High selectivity process to make dihydrofluoroalkenes

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Quick Facts
Patent No.
US 8,618,339
App. No.
12/110,890
Granted
Dec 31, 2013
Kind
B2
Abstract

Disclosed is a method for the synthesis of fluorinated alkenes comprising contacting a fluorinated alkyne of the formula R 1 C≡C R 2 , wherein R 1 and R 2 are independently selected from CF 3 , C 2 F 5 , C 3 F 7 , and C 4 F 9 , in a pressure vessel, with a Lindlar catalyst, with substantially one molar equivalent of hydrogen, to make the corresponding cis-alkene of formula R 1 C≡C R 2 with high selectivity, wherein said hydrogen is added in portions over a period of time, so as to produce an initial pressure in the pressure in the vessel of no more than about 100 psi.

Claims (11)

1. A process for hydrogenation, comprising: contacting a fluorinated alkyne of the formula R 1 C≡C R 2 , wherein R 1 and R 2 are independently selected from CF 3 , C 2 F 5 , C 3 F 7 , and C 4 F 9 , with substantially one equivalent or less of hydrogen in a reaction zone, in the gas phase in the presence of a Lindlar catalyst to make a fluorinated alkene of formula R 1 CH═CH R 2 .

2. The process of claim 1 wherein the fluorinated alkyne is selected from the group consisting of hexafluoro-2-butyne, octafluoro-2-pentyne, decafluoro-2-hexyne, decafluoro-3-hexyne, dodecafluoro-2-heptyne, dodecafluoro-3-heptyne, tetradecafluoro-3-octyne and tetradecafluoro-4-octyne.

3. The process of claim 1 wherein the ratio of hydrogen to fluorinated alkyne is from about 0.67:1 to about 1:1.

4. The process of claim 1 wherein the weight percent of palladium catalyst on calcium carbonate support is from about 1% by weight to about 10% by weight.

5. The process of claim 1 wherein the weight percent of palladium catalyst on calcium carbonate support is from about 1% by weight to about 5% by weight.

6. The process of claim 1 wherein the fluorinated alkyne fed to the reaction zone further comprises an inert carrier gas.

7. The process of claim 6 wherein the inert carrier gas is selected from the group consisting of nitrogen, helium or argon.

8. The process of claim 1 , further comprising, recovering a product mixture comprising the said cis- isomer of said fluorinated alkene of formula R 1 CH═CH R 2 by factional distillation.

9. The process of claim 1 , wherein the said fluorinated alkene product of formula R 1 CH═CH R 2 comprises both the cis- and trans- isomers.

10. The process of claim 9 , wherein the trans- isomer of the fluorinated alkene product is at least 5% by weight of the fluorinated alkene product.

11. The process of claim 9 , wherein the trans- isomer of the fluorinated alkene product is at least 10% by weight of the fluorinated alkene product.

Assignments (5)
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 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Jun 23, 2008
From: SWEARINGEN, EKATERINA N.
To: E. I. DU PONT DE NEMOURS AND COMPANY
Reel/Frame 021136/0843 →