Process for the manufacture of 2,3,3,3-tetrafluoropropene

US9296670B2 · US · B2

Patent metadata
FieldValue
Publication numberUS-9296670-B2
Application numberUS-201314377727-A
CountryUS
Kind codeB2
Filing dateFeb 8, 2013
Priority dateFeb 10, 2012
Publication dateMar 29, 2016
Grant dateMar 29, 2016

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Abstract

Official abstract text for this publication.

A method for forming 2,3,3,3-tetrafluoropropene (HFO-1234yf) comprising providing a dehydrochlorination starting material having relatively low concentrations of 2-chloro-3,3,3-trifluoropropene (HCFO-1233xf), especially and preferable less than about 8.0% when the dehydrochlorination reaction utilizes no substantial amount of catalyst or catalyst comprising austenitic nickel-based materials.

First claim

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What is claimed is: 1. A process for reducing the concentration of 2-chloro-3,3,3-trifluoropropene in a composition comprised of 2-chloro-1,1,1,2-tetrafluoropropane and 2-chloro-3,3,3-trifluoropropene which comprises conducting a process selected from (a) photochlorinating the composition to form 1,2,2-trichloro-3,3,3-trifluoropropane in the presence of at least one chlorination agent and separating the 2-chloro-1,1,1,2-tetrafluoropropane from the 1,2,2-trichloro-3,3,3-trifluoropropane; (b) passing the composition over a fixed bed of solid adsorbents selected from activated carbons and zeolites or molecular sieves, and collecting the 2-chloro-1,1,1,2-tetrafluoropropane from the fixed bed of solid adsorbents; and (c) mixing said composition with liquid hydrofluoric acid to form a mixture comprised of 2-chloro-1,1,1,2-tetrafluoropropane and 2-chloro-3,3,3-trifluoropropene and HF, said HF present in the mixture is less than about 10% by weight; distilling the mixture and collecting the distilled product substantially free of 2-chloro-3,3,3-trichloropropene and purer in 2-chloro-1,1,1,2-tetrafluoropropane. 2. The process according to claim 1 where the composition is photochlorinated. 3. The process according to claim 2 where photochlorinating comprises exposing the composition to radiation in the presence of said at least one chlorination agent. 4. The process according to claim 1 wherein the photochlorinating is carried out in the vapor phase at a temperature ranging from about −20 C to about 200 C. 5. The process according to claim 1 wherein 2-chloro-1,1,1,2-tetrafluoropropane is separated from 2-chloro-3,3,-trifluoropropene utilizing activated carbon. 6. The process according to claim 1 wherein 2-chloro-1,1,1,2-tetrafluoropropane is separated from 2-chloro-3,3,-trifluoropropene utilizing molecular sieves or zeolites. 7. The process according to claim 6 wherein the pores of the molecular sieves or zeolites ranges from about 3 Angstroms to about 10 Angstroms. 8. The process according to claim 1 comprising mixing said composition with liquid hydrofluoric acid to form a mixture comprised of 2-chloro-1,1,1,2-tetrafluoropropane and 2-chloro-3,3,3-trifluoropropene and HF, said HF is present in the mixture in less than about 10% by weight; and distilling the mixture; and collecting the distilled product substantially free of 2-chloro-3,3,3-trichloropropene and purer in 2-chloro-1,1,1,2-tetrafluoropropane. 9. A process for preparing 2,3,3,3-tetrafluoropropene comprising: (i) subjecting a first composition comprising a 2-chloro-1,1,1,2-tetrafluoropropane and 2-chloro-3,3,3-trifluoropropene to purification process that reduces the concentration of 2-chloro-3,3,3-trifluoropropene so that the composition is substantially free of 2-chloro-3,3,3-trifluoropropene; and (ii) contacting said purified composition with a dehydrochlorination catalyst to produce a final composition comprising 2,3,3,3-tetrafluoropropene, wherein said purification process is selected from (a) photochlorinating the first composition to form 1,2,2-trichloro-3,3,3-trifluoropropane in the presence of at least one chlorination agent and separating the 2-chloro-1,1,1,2-tetrafluoropropane from the 1,2,2-trichloro-3,3,3-trifluoropropane; (b) passing the first composition over a fixed bed of solid adsorbents selected from activated carbon and zeolites or molecular sieves, and collecting the 2-chloro-1,1,1,2-tetrafluoropropane from the of activated carbon, zeolites or molecular sieves; and (c) mixing said first composition with liquid hydrofluoric acid to form a mixture comprised of 2 chloro-1,1,1,2-tetrafluoropropane and 2-chloro-3,3,3-trifluoropropene and HF, said HF present in the mixture is less than about 10% by weight; and feeding the mixture and collecting the distilled product substantially free of 2-chloro-3,3,3-trichloropropene and purer in 2-chloro-1,1,1,2-tetrafluoropropane. 10. A process for preparing 2,3,3,3-tetrafluoropropene comprising: (i) providing a first composition including a compound of Formulae I, II, or III: CX 2 ═CCl—CH 2 X  (I); CX 3 —CCl═CH 2   (II); or CX 3 —CHCl—CH 2 X  (III) wherein X is independently selected from F, Cl, Br, and I, provided that at least one X is not fluorine; (ii) contacting the first composition with a first fluorinating agent to produce a first intermediate composition including 2-chloro-3,3,3-trifluoropropene and a first chlorine-containing byproduct; (iii) contacting the first intermediate composition with a second fluorinating agent to produce a second intermediate composition including 2-chloro-1,1,1,2-tetrafluoropropane and 2-chloro-3,3,3-trifluoropropene; (iv) reducing the concentration of 2-chloro-3,3,3-trifluoropropene in the second intermediate composition to produce a third intermediate composition comprising 2-chloro-1,1,1,2-tetrafluoropropane that is substantially free of 2-chloro-3,3,3-trifluoropropene; and (v) dehydrochlorinating at least a portion of the third intermediate composition comprising 2-chloro-1,1,1,2-tetrafluoropropane to produce a reaction product including 2,3,3,3-tetrafluoropropene, wherein the second intermediate composition comprised of 2-chloro-1,1,1,2-tetrafluoropropene is made substantially free of 2-chloro-3,3,3-trifluoropropene by subjecting the second intermediate composition to a process selected from (a) photochlorinating the second intermediate composition to form 1,2,2,-trichloro-3,3,3-trifluoropropane in the presence of at least one chlorination agent and separating the 2-chloro-1,1,1,2-tetrafluoropropane from the 1,2,2,-trichloro-3,3,3-trifluoropropane; (b) passing the second intermediate composition over a fixed bed of solid adsorbents selected from activated carbons and zeolites or molecular sieves and collecting the 2-chloro-1,1,1,2-tetrafluoropropane from the activated carbon, zeolites or molecular sieves; and (c) mixing said second intermediate composition with liquid hydrofluoric acid to form a mixture comprised of 2-chloro-1,1,1,2-tetrafluoropropane and 2-chloro-3,3,3-trifluoropropene and HF, said HF present in the mixture is less than about 10% by weight; distilling the mixture; and collecting the distilled product substantially free of 2-chloro-3,3,3-trichloropropene and purer in 2-chloro-1,1,1,2-tetrafluoropropane. 11. The process according to claim 9 wherein the third intermediate composition comprises 2-chloro-3,3,3-trifluoropropene in an amount less than about 20 wt %. 12. The process according to claim 10 wherein the third intermediate composition comprises 2-chloro-3,3,3-trifluoropropene in an amount less than about 5 wt %. 13. A process of preparing 2,3,3,3-tetrafluoropropene that is substantially free of 3,3,3-trifluoropropyne comprising: (i) Providing a first composition comprising a 2-chloro-1,1,1,2-tetrafluoropropane that is substantially free of 2-chloro-3,3,3-trifluoropropene; and (ii) contacting said first composition with a dehydrochlorination catalyst to produce a final composition comprising 2,3,3,3-tetrafluoropropene, said final composition being substantially free of 3,3,3-trifluoropropyne. 14. A process for producing 2,3,3,3-tetrafluoropropene that is substantially free of 3,3,3-trifluoropropyne comprising: (i) providing a first composition including a compound of Formulae I, II, or III: CX 2 ═CCl—CH 2 X  (I); CX 3 —CCl═CH 2   (II); or CX 3 —CHCl—CH 2 X  (III) wherein X is independently selected from F, Cl, Br, and I, provided that at least one X is not fluorine; (ii) contacting the first composition with a first fluorinating agent to produce a first intermediate composition including 2-chloro-3,3,3-trifluoroprope

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Classifications

  • Recycling of unreacted starting or intermediate materials · CPC title

  • by adsorption on solids · CPC title

  • Halides · CPC title

  • C07C17/06Primary

    combined with replacement of hydrogen atoms by halogens · CPC title

  • to unsaturated halogenated hydrocarbons · CPC title

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What does patent US9296670B2 cover?
A method for forming 2,3,3,3-tetrafluoropropene (HFO-1234yf) comprising providing a dehydrochlorination starting material having relatively low concentrations of 2-chloro-3,3,3-trifluoropropene (HCFO-1233xf), especially and preferable less than about 8.0% when the dehydrochlorination reaction utilizes no substantial amount of catalyst or catalyst comprising austenitic nickel-based materials.
Who is the assignee on this patent?
Honeywell Int Inc, Chemours Co Fc Llc
What technology area does this patent fall under?
Primary CPC classification C07C17/06. Mapped technology areas include Chemistry & Metallurgy.
When was this patent published?
Publication date Tue Mar 29 2016 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 8 related publications on this page (citations in our corpus or others sharing the same primary CPC).