Liquid phase process for preparing (E)-1,1,1,4,4,4-hexafluorobut-2-ene

US10611709B2 · US · B2

Patent metadata
FieldValue
Publication numberUS-10611709-B2
Application numberUS-201816126560-A
CountryUS
Kind codeB2
Filing dateSep 10, 2018
Priority dateSep 11, 2017
Publication dateApr 7, 2020
Grant dateApr 7, 2020

How to read this patent

A practical reading order for non-experts. Skip the full description unless you need deep technical detail.

  1. Title

    What the patent document calls the invention.

  2. Abstract

    A short plain-language summary of the technical disclosure.

  3. Assignees and inventors

    Who owns or filed the patent and who is credited as inventor.

  4. Key dates

    Filing, priority, publication, and grant dates set the timeline.

  5. First independent claim

    The legal scope of protection — read this for what is actually claimed.

  6. CPC / IPC classifications

    Technology tags used to group this patent with similar filings.

  7. Citations and related patents

    Prior art links and similar publications in this corpus.

Abstract

Official abstract text for this publication.

Disclosed herein are methods of producing E-CF3CH═CHCF3 in a liquid phase. Also disclosed are methods of preparing CF3CH2CHClCF3 and CF3CHClCH2CCl3.

First claim

Opening claim text (preview).

What is claimed is: 1. A process for preparing E-CF 3 CH═CHCF 3 , comprising: treating CF 3 CH 2 CHClCF 3 with an effective amount of a base in the presence of a phase transfer catalyst and a solvent component consisting of water, to form a mixture comprising the E-CF 3 CH═CHCF 3 , wherein the process is a liquid phase process and the base is sodium hydroxide. 2. The process of claim 1 , wherein the mixture further comprises one or more of hexafluoroisobutylene, 1,1,1,4,4,4-hexafluorobutane, (E)-1-chloro-1,1,4,4,4-pentafluorobut-2-ene, and Z—CF 3 CH═CHCF 3 . 3. The process of claim 1 , wherein the base is in an aqueous solution of from about 4 M to about 12 M. 4. The process of claim 1 , wherein the phase transfer catalyst is selected from the group consisting of a quaternary ammonium salt, a heterocyclic ammonium salt, an organic phosphonium salt, and a nonionic compound. 5. The process of claim 4 , wherein the phase transfer catalyst is selected from the group consisting of benzyltrimethylammonium chloride, benzyltriethylammonium chloride, methyltricaprylammonium chloride, methyltributylammonium chloride, methyltrioctylammonium chloride, dimethyldiphenylphosphonium iodide, methyltriphenoxyphosphonium iodide, tetrabutylphosphonium bromide, tetrabutylphosphonium chloride, hexadecyltributylphosphonium bromide, and DL-α-tocopherol methoxypolyethylene glycol succinate. 6. The process of claim 5 , wherein the phase transfer catalyst is methyltrioctylammonium chloride. 7. The process of claim 4 , wherein the base is sodium hydroxide and the phase transfer catalyst is methyltrioctylammonium chloride. 8. The process of claim 1 , wherein the E-CF 3 CH═CHCF 3 is substantially isolated from the mixture. 9. The process of claim 1 , wherein the CF 3 CH 2 CHClCF 3 is prepared according to a second process comprising contacting CF 3 CHClCH 2 CCl 3 with HF in the presence of a catalyst, wherein the second process is a liquid phase process. 10. The process of claim 9 , wherein the catalyst is a metal halide selected from the group consisting of SbF 5 , SbCl 5 , SbCl 3 , SnCl 4 , TaCl 5 , TiCl 4 , NbCl 5 , MoCl 6 , WC 16 , antimony (V) chlorofluorides, and combinations thereof. 11. The process of claim 10 , wherein the metal halide is selected from the group consisting of SbF 5 , TaCl 5 , and antimony (V) chlorofluorides. 12. The process of claim 9 , wherein the second process is performed at a temperature of from about 50° C. to about 100° C. 13. The process of claim 9 , wherein the CF 3 CHClCH 2 CCl 3 is prepared by a third process comprising contacting carbon tetrachloride with 3,3,3-trifluoropropene in the presence of an organophosphorus compound and a catalyst comprising a metal, wherein the third process is a liquid phase process. 14. The process of claim 13 , wherein the organophosphorus compound is selected from the group consisting of a phosphate ester, a phosphate amide, a phosphonic acid, a phosphonic ester, a phosphinic acid, a phosphinic ester, a phosphine oxide, a phosphine imide, a phosphonium salt, a phosphorene, a phosphite, a phosphonate, a phosphinite, and a phosphine. 15. The process of claim 14 , wherein the organophosphorus compound is tributylphosphate. 16. The process of claim 13 , wherein the metal of the catalyst is selected from the group consisting of Fe, Co, Ni, Cu, Mo, Cr, and Mn. 17. The process of claim 16 , wherein the metal is Fe. 18. The process of claim 13 , wherein the third process takes place at a temperature of from about 100° C. to about 120° C. 19. A process for preparing E-CF 3 CH═CHCF 3 , comprising: (a) contacting carbon tetrachloride with 3,3,3-trifluoropropene in the presence of an organophosphorus compound and a catalyst comprising a metal to produce CF 3 CHClCH 2 CCl 3 ; (b) contacting the CF 3 CHClCH 2 CCl 3 with HF in the presence of a catalyst to produce CF 3 CH 2 CHClCF 3 ; and (c) treating the CF 3 CH 2 CHClCF 3 with an effective amount of a base in the presence of a phase transfer catalyst and a solvent component consisting of water, to form a mixture comprising the E-CF 3 CH═CHCF 3 , wherein the process is a liquid phase process, and the base of step (c) is sodium hydroxide. 20. The process of claim 19 , wherein the mixture of step (c) further comprises one or more of hexafluoroisobutylene, 1,1,1,4,4,4-hexafluorobutane, (E)-1-chloro-1,1,4,4,4-pentafluorobut-2-ene, and Z—CF 3 CH═CHCF 3 . 21. The process of claim 19 , wherein the E-CF 3 CH═CHCF 3 is substantially isolated from the mixture. 22. A composition, consisting of comprising: E-CF 3 CH═CHCF 3 , hexafluoroisobutylene, 1,1,1,4,4,4-hexafluorobutane, (E)-1-chloro-1,1,4,4,4-pentafluorobut-2-ene, and Z—CF 3 CH═CHCF 3 . 23. The composition of claim 22 , wherein the composition consists of greater than about 99 mol % E-CF 3 CH═CHCF 3 . 24. The composition of claim 22 , which is prepared according to a process comprising treating CF 3 CH 2 CHClCF 3 with an effective amount of a base in the presence of a phase transfer catalyst and a solvent component consisting of water, wherein the process is a liquid phase process and the base is sodium hydroxide.

Assignees

Inventors

Classifications

  • Phosphonium compounds, i.e. phosphine with an additional hydrogen or carbon atom bonded to phosphorous so as to result in a formal positive charge on phosphorous · CPC title

  • the other compound being HX · CPC title

  • Iron · CPC title

  • Tetrafluoroethene · CPC title

  • Phase-transfer catalysis in a mixed solvent system containing at least 2 immiscible solvents or solvent phases · CPC title

Patent family

Related publications grouped by family.

External sources

Frequently asked questions

Answers are generated from the same data shown on this page.

What does patent US10611709B2 cover?
Disclosed herein are methods of producing E-CF3CH═CHCF3 in a liquid phase. Also disclosed are methods of preparing CF3CH2CHClCF3 and CF3CHClCH2CCl3.
Who is the assignee on this patent?
Chemours Co Fc Llc
What technology area does this patent fall under?
Primary CPC classification C07C17/25. Mapped technology areas include Chemistry & Metallurgy.
When was this patent published?
Publication date Tue Apr 07 2020 00:00:00 GMT+0000 (Coordinated Universal Time) (B2). Legal status and post-grant events are not shown on this page.
What related patents are in patentsdb?
We list 2 related publications on this page (citations in our corpus or others sharing the same primary CPC).