US4281119A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Cryogenically controlled direct fluorination process, apparatus and products resulting therefrom
Assignee: Massachusetts Institute of Technology
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Filing: 1976-06-23
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Granted: 1981-07-28
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Expires: 1996-06-23
Abstract
Abstract An apparatus and process useful in direct fluorination of a variety of compositions, as well as the fluorinated compositions themselves, are disclosed. The apparatus comprises a cryogenic zone reactor, such as a packed column reactor, suitably divided into a plurality of independently controllable cryogenic temperature zones. Means are also provided to introduce a reactant to be fluorinated as well as to introduce a mixture of fluorine gas and an inert gas. New fluorinated compounds are also disclosed. These include: perfluoro-2-methoxyethyl ether; perfluoro-1,4-dioxane; perfluoro-2,5-diketohexane; perfluorohexamethylethane; and monohydropentadecafluoroadamantane. Additionally, new syntheses for trifluoroacetic acid, a commercially significant bulk chemical, are disclosed. One synthesis comprises producing perfluoroethyl acetate by direct fluorination using a cryogenic zone reactor, followed by hydrolysis of perfluoroethyl acetate. Two moles of the acid are produced for each mole of ester. A second synthesis comprises fluorinating an acyl chloride followed by hydrolysis of the resulting acyl fluoride.
Inventors
- 👤 Richard J. Lagow
- 👤 James L. Adcock
- 👤 Norma J. Maraschin
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-29 12:12
CPC Classifications
C; C07; C07D; C07D265/00; C07D265/28; C07D265/30; B; B01; B01J; B01J19/00; B01J19/0006; B01J19/0013; B01J8/00; B01J8/02; C07B; C07B39/00; C07C; C07C17/00; C07C17/093; C07C17/10; C07C41/00; C07C41/01; C07C41/18; C07C41/22; C07C41/48; C07C41/50; C07C43/00; C07C43/30; C07C43/313; C07C45/00; C07C45/61; C07C45/63; C07C49/00; C07C49/04; C07C49/16; C07C49/167; C07C51/00; C07C51/04; C07C51/347; C07C51/363; C07C51/58; C07D319/00; C07D319/10; C07D319/12; B01J2219/00; B01J2219/00049; B01J2219/00051; B01J2219/00054; B01J2219/00056; B01J2219/00058; B01J2219/00074; B01J2219/00076; B01J2219/00083; B01J2219/00087; B01J2219/00099; B01J2219/00132; B01J2219/00135; B01J2219/0015; B01J2219/00155
Claims Analysis
Total Claims: 12
Claim 1
Independent Claim
210 words
A direct fluorination process for fluorinating a reactant with elemental fluorine, comprising: a. providing a packed column fluorination reactor having a multiplicity of temperature zones independently controllable to a temperature within a range of about -190° C. to about +20° C.; b. lowering the temperature of a first zone below the condensation point of the reactant to be fluorinated; c. introducing said reactant to be fluorinated into said first zone while it is maintained at the lowered temperature whereby said reactant condenses on the column packings in said first zone; d. introducing a source of elemental fluorine and an inert gas into said first zone, the source of elemental fluorine initially comprising a very small percentage of said mixture and which gradually rises as fluorination proceeds; e. maintaining the temperature of said first zone until at least partial fluorination of the condensed reactant has occurred; f. raising the temperature in said first zone to volatilize said partially fluorinated reactant and lowering the temperature in a second zone below the freezing point of said partially fluorinated reactant whereby the partially fluorinated reactant is transported to said second zone wherein it condenses on the column packings therein; and, g. repeating step f. until said reactant has been fluorinated to the desired degree.
Claim 2
Dependent Claim
210 words
A direct fluorination process for fluorinating a reactant with elemental fluorine, comprising: a. providing a packed column fluorination reactor having a multiplicity of temperature zones independently controllable to a temperature within a range of about -190° C. to about +20° C.; b. lowering the temperature of a first zone below the condensation point of the reactant to be fluorinated; c. introducing said reactant to be fluorinated into said first zone while it is maintained at the lowered temperature whereby said reactant condenses on the column packings in said first zone; d. introducing a source of elemental fluorine and an inert gas into said first zone, the source of elemental fluorine initially comprising a very small percentage of said mixture and which gradually rises as fluorination proceeds; e. maintaining the temperature of said first zone until at least partial fluorination of the condensed reactant has occurred; f. raising the temperature in said first zone to volatilize said partially fluorinated reactant and lowering the temperature in a second zone below the freezing point of said partially fluorinated reactant whereby the partially fluorinated reactant is transported to said second zone wherein it condenses on the column packings therein; and, g. repeating step f. until said reactant has been fluorinated to the desired degree.
Claim 3
Dependent Claim
16 words
A direct fluorination process of claim 1 wherein said source of elemental fluorine comprises fluorine gas.
Claim 4
Dependent Claim
16 words
A direct fluorination process of claim 2 wherein said reactant to be fluorinated comprises a ketone.
Claim 5
Dependent Claim
16 words
A direct fluorination process of claim 2 wherein said reactant to be fluorinated comprises an ether.
Claim 6
Dependent Claim
16 words
A direct fluorination process of claim 2 wherein said reactant to be fluorinated comprises an ester.
Claim 7
Dependent Claim
17 words
A direct fluorination process of claim 2 wherein said reactant to be fluorinated comprises a carboxylic acid.
Claim 8
Dependent Claim
16 words
A direct fluorination process of claim 2 wherein said reactant to be fluorinated comprises a nitrile.
Claim 9
Dependent Claim
125 words
A direct fluorination process comprising contacting, at a first fluorination site, a source of elemental fluorine and a reactant to be fluorinated at a temperature below the condensation point of said reactant and in the presence of fluorination surface capable of removing heat generated during fluorination whereby said reactant is partially fluorinated, warming said first fluorination site to a temperature at which said partially fluorinated reactant volatilizes whereby it is volatilized and passes to a fresh fluorination site, lowering the temperature of said fresh fluorination site below the condensation point of said partially fluorinated reactant and contacting the partially fluorinated reactant, at said fresh site, with a source of elemental fluorine in the presence of a fluorination surface capable of removing heat generated during fluorination.
Claim 10
Dependent Claim
125 words
A direct fluorination process comprising contacting, at a first fluorination site, a source of elemental fluorine and a reactant to be fluorinated at a temperature below the condensation point of said reactant and in the presence of fluorination surface capable of removing heat generated during fluorination whereby said reactant is partially fluorinated, warming said first fluorination site to a temperature at which said partially fluorinated reactant volatilizes whereby it is volatilized and passes to a fresh fluorination site, lowering the temperature of said fresh fluorination site below the condensation point of said partially fluorinated reactant and contacting the partially fluorinated reactant, at said fresh site, with a source of elemental fluorine in the presence of a fluorination surface capable of removing heat generated during fluorination.
Claim 11
Dependent Claim
16 words
A direct fluorination process of claim 8 wherein said source of elemental fluorine comprises fluorine gas.
Claim 12
Dependent Claim
21 words
A direct fluorination process of claim 9 wherein said fluorination surface capable of removing heat generated during fluorination comprises copper metal.
References Cited (Backward Citations)
No citation records indexed.
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1984-07-27 | 1985-01-26 | 1985-07-28 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1988-07-27 | 1989-01-26 | 1989-07-28 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1992-07-27 | 1993-01-26 | 1993-07-28 | $7700.00 | Window Closed / Lapsed |