US4158023A
Expired / Lapsed
US
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Process for the manufacture of octafluoropropane
Assignee: Solvay SA
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Filing: 1978-03-21
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Granted: 1979-06-12
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Expires: 1998-03-21
Abstract
Abstract Octafluoropropane, C 3 F 8 , is prepared by a two-step process. In the first step hexafluoropropene is reacted with hydrogen fluoride in the presence of a chromium oxyfluoride catalyst. The 2H-heptafluoropropane obtained is reacted with fluorine in the presence of a catalyst which contains a subgroup element of the Periodic System as a free metal or as a fluoride. Octafluoropropane is isolated from the resulting gas mixture. Hydrogen fluoride also obtained may be recycled to the first reaction step.
Inventors
- 👤 Sigmar P. von Halasz
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-28 11:59
CPC Classifications
C; C07; C07C; C07C19/00; C07C19/08; C07C17/00; C07C17/07; C07C17/08; C07C17/087; C07C17/093; C07C17/10
Claims Analysis
Total Claims: 8
Claim 1
Independent Claim
106 words
A process for the manufacture of octafluoropropane from hexafluoropropene, which comprises converting hexafluoropropene with hydrogen fluoride in a first reaction step to 2H-heptafluoropropane, at a temperature of from 100° to 350° C. and in the presence of a chromium oxyfluoride catalyst, and converting in a second reaction step the reaction gas obtained with elementary fluorine to octafluoropropane, at a temperature of from 100° to 350° C. in the presence of a catalyst containing an element of one of the groups IIIB to VIIB, VIII, IB or IIB of the Periodic System or a flouride compound thereof, and subsequently separating the hydrogen fluoride formed from the octafluoropropane.
Claim 2
Dependent Claim
106 words
A process for the manufacture of octafluoropropane from hexafluoropropene, which comprises converting hexafluoropropene with hydrogen fluoride in a first reaction step to 2H-heptafluoropropane, at a temperature of from 100° to 350° C. and in the presence of a chromium oxyfluoride catalyst, and converting in a second reaction step the reaction gas obtained with elementary fluorine to octafluoropropane, at a temperature of from 100° to 350° C. in the presence of a catalyst containing an element of one of the groups IIIB to VIIB, VIII, IB or IIB of the Periodic System or a flouride compound thereof, and subsequently separating the hydrogen fluoride formed from the octafluoropropane.
Claim 3
Dependent Claim
36 words
The process as claimed in claim 1, wherein the catalyst of the second reaction step contains an element of one of the groups IB, IIB or VIII of the Periodic System, or a fluoride compound thereof.
Claim 4
Dependent Claim
31 words
The process as claimed in claim 1, wherein the fluoride of the subgroup element of the catalyst of the second reaction step is neither liquid nor volatile at the reaction temperature.
Claim 5
Dependent Claim
23 words
The process as claimed in claim 1, which comprises recycling the hydrogen fluoride separated in the second step to the first reaction step.
Claim 6
Dependent Claim
27 words
The process as claimed in claim 1, which comprises carrying out the reaction in the second reaction step in the presence of a gas inert to fluorine.
Claim 7
Dependent Claim
16 words
The process as claimed in claim 5, wherein the gas inert to fluorine is hydrogen fluoride.
Claim 8
Dependent Claim
23 words
The process as claimed in claim 1, which comprises carrying out the reactions of the first and second step in the same reactor.
References Cited (Backward Citations)
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1982-06-11 | 1982-12-11 | 1983-06-12 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1986-06-11 | 1986-12-11 | 1987-06-12 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1990-06-11 | 1990-12-11 | 1991-06-12 | $7700.00 | Window Closed / Lapsed |