One-pot process using heterogeneous catalyst

US9944571B2 · US · B2

Patent metadata
FieldValue
Publication numberUS-9944571-B2
Application numberUS-201515528338-A
CountryUS
Kind codeB2
Filing dateNov 16, 2015
Priority dateNov 19, 2014
Publication dateApr 17, 2018
Grant dateApr 17, 2018

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  1. Title

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  2. Abstract

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  3. Assignees and inventors

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  4. Key dates

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  5. First independent claim

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  6. CPC / IPC classifications

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  7. Citations and related patents

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Abstract

Official abstract text for this publication.

The present invention relates to a process for the one-pot hydrogenation and dehydration or isomerization of an organic compound, and to a catalyst composition for this process comprising transition metal particles having particle size below 50 nm supported on a material comprising at least one fluorinated polymer (P), wherein polymer (P) bears —SO 2 X functional groups, X being selected from X′ and OM, X′ being selected from the groups consisting of F, Cl, Br and I; and M being selected from the group consisting of H, and alkaline metal and NH 4 .

First claim

Opening claim text (preview).

The invention claimed is: 1. A process for the one-pot hydrogenation and acid-catalysed isomerisation or dehydration of a substrate (I) containing at least a C═C, a C═O, an acetal, a 1,2-diol or a hemiacetal moiety to obtain a product (II), wherein said process comprises reacting the substrate (I) with hydrogen (H 2 ) in the presence of a catalyst (III), said catalyst comprising transition metal particles having particle size below 50 nm supported on a material comprising at least one fluorinated polymer (P), wherein polymer (P) bears —SO 2 X functional groups, X being selected from X′ and OM, X′ being selected from the group consisting of F, Cl, Br, and I; and M being selected from the group consisting of H, an alkaline metal and NH 4 . 2. The process according to claim 1 , wherein the transition metal particles in the catalyst consist of at least one transition metal, in non-charged or ionic form, selected from ruthenium, rhodium, platinum, palladium, copper, nickel, iridium, cobalt, osmium, rhenium, iron, and combinations thereof. 3. The process according to claim 1 , wherein the step of reacting the substrate (I) with catalyst (III) is carried out at a temperature from 50 to 150° C. 4. The process according to claim 1 , wherein levulinic acid (Ia) is converted into gamma-valerolactone (IIa), hemicellulose or cellulose (Ib) is converted into sorbitol (IIb), xylose (Ic) is converted into levulinic acid or an ester thereof (IIc), gamma-valerolactone (IIa) is converted into pentanoic acid (IId), glycerol (Ie) is converted into 1,2-propanediol (IIe), citronellal (If) is converted into menthol (IIf), acetone (Ig) is converted into methyl isobutyl ketone (IIg), or glucose (Ih) is converted into 1,6-hexanediol or 2,5-dimethylfuran (IIh). 5. The process according to claim 4 , wherein the substrate (I) is levulinic acid (Ia) and the product (II) is gamma-valerolactone (IIa). 6. The process according to claim 1 , wherein the a least one fluorinated polymer bearing —SO 2 X functional groups comprises recurring units derived from at least one ethylenically unsaturated fluorinated monomer containing at least one —SO 2 X′ functional group (monomer A) and recurring units derived from at least one ethylenically unsaturated fluorinated monomer (monomer B). 7. The process according to claim 6 , wherein the a least one fluorinated polymer (P) comprises: recurring units derived from at least a monomer (A), wherein monomer (A) is selected from: sulfonyl halide fluoroolefins of formula: CF 2 ═CF(CF 2 ) p SO 2 X′ wherein p is an integer between 0 and 10; sulfonyl halide fluorovinylethers of formula: CF 2 ═CF—O—(CF 2 ) m SO 2 X′ wherein m is an integer between 1 and 10; sulfonyl halide fluoroalkoxyvinyl ethers of formula: CF 2 ═CF—(OCF 2 CF(R F1 )) w —O—CF 2 (CF(R F2 )) y SO 2 X′ wherein w is an integer between 0 and 2, R F1 and R F2 , equal or different from each other, are independently F, Cl or a C 1 -C 10 fluoroalkyl group, optionally substituted with one or more ether oxygens, y is an integer between 0 and 6; sulfonyl halide aromatic fluoroolefins of formula CF 2 ═CF—Ar—SO 2 X′ wherein Ar is a C 5 -C 15 aromatic or heteroaromatic substituent; and recurring units derived from at least a monomer (B), wherein monomer (B) is selected from C 2 -C 8 fluoroolefins; C 2 -C 8 chloro- and/or bromo- and/or iodo-fluoroolefins; fluoroalkylvinylethers of formula CF 2 ═CFOR f1 , wherein R f1 is a C 1 -C 6 fluoroalkyl; fluoro-oxyalkylvinylethers of formula CF 2 ═CFOR O1 , wherein R O1 is a C 1 -C 12 fluoro-oxyalkyl having one or more ether groups; fluoroalkyl-methoxy-vinylethers of formula CF 2 ═CFOCF 2 OR f2 in which R f2 is a C 1 -C 6 fluoroalkyl or a C 1 -C 6 fluorooxyalkyl having one or more ether groups; fluorodioxoles, of formula: wherein each of R f3 , R f4 , R f5 , R f6 , equal or different each other, is independently a fluorine atom, a C 1 -C 6 fluoroalkyl, optionally comprising one or more oxygen atom. 8. The process of claim 7 , wherein monomer (A) is selected from the group of the fluorovinylethers of formula CF 2 ═CF—O—(CF 2 ) m —SO 2 F, wherein m is an integer between 1 and 6, and/or monomer (B) is selected from: C 3 -C 8 fluoroolefins; chloro- and/or bromo- and/or iodo-C 2 -C 6 fluoroolefins; fluoroalkylvinylethers of formula CF 2 ═CFOR f1 wherein R f1 is a C 1 -C 6 fluoroalkyl; fluoro-oxyalkyl- vinylethers of formula CF 2 ═CFOR O1 , wherein R O1 is a C 1 -C 12 fluorooxyalkyl having one or more ether groups. 9. The process of claim 8 , wherein monomer (A) is CF 2 ═CFOCF 2 CF 2 —SO 2 F (perfluoro-5-sulfonylfluoride-3-oxa-1-pentene) and/or monomer (B) is tetrafluoroethylene. 10. The process of claim 1 , wherein the step of reacting the substrate (I) with hydrogen (H 2 ) in the presence of a catalyst (III) is carried out in a solvent system comprising water. 11. Use of a catalyst (III) comprising transition metal particles having particle size below 50 nm supported on a material comprising at least one fluorinated polymer (P), wherein polymer (P) bears —SO 2 X functional groups, X being selected from X′ and OM, X′ being selected from the group consisting of F, Cl, Br, and I; and M being selected from the group consisting of H, an alkaline metal and NH 4 , in the one-pot hydrogenation and acid-catalysed isomerisation or dehydration of a substrate (I) containing at least a C═C or C═O moiety to obtain a product (II), wherein said process comprises reacting the substrate with hydrogen (H 2 ) in the presence of catalyst (III). 12. A solid composition comprising transition metal particles having particle size below 50 nm supported on a material comprising at least one fluorinated polymer (P), wherein polymer (P) bears —SO 2 X functional groups, X being selected from X′ and OM, X′ being selected from the group consisting of F, Cl, Br, and I; and M being selected from the group consisting of H, an alkaline metal and NH 4 , and (P) comprises recurring units derived from tetrafluoroethylene (TFE) and a linear Sulfonyl Fluoride Vinyl Ether (SFVE). 13. The solid composition according to claim 12 , wherein the transition metal particles have a particle size below 10 nm. 14. The solid composition according to claim 12 , wherein the metal particles on the support (P) comprise at least one metal, in non-charged or ionic form, selected from ruthenium, rhodium, platinum, palladium, copper, nickel, iridium, cobalt, osmium, rhenium, iron, and combinations thereof. 15. The solid composition according to claim 12 , wherein the polymer (P) has an equivalent weight of 500 g/eq or higher in grams of fluorinated polymer per mole of —SO 3 H functional groups. 16. The solid composition according to claim 14 , wherein the metal particles on the support (P) consist of at least one metal, in non-charged or ionic form, selected from ruthenium, platinum, palladium and rhodium. 17. The solid composition according to claim 15 , wherein the polymer (P) has an equivalent weight of 380 g/eq or higher in grams of fluorinated polymer per mole of —SO 3 H functional groups. 18. The process according to claim 7 , wherein monomer (A) is selected from: sulfonyl halide fluoroolefins of formula: CF 2 ═CF(CF 2 ) p SO 2 X′ wherein p is equal to 2 or 3 and X′ is F; sulfonyl halide fluorovinylethers of formula: CF 2 ═CF—O—(CF 2 ) m SO 2 X′ wherein m equals 2 and X′ is F; sulfonyl halide fluoroalkoxyvinyl ethers of formula: CF 2 ═CF—(OCF 2 CF(R F1 )) w —O—CF 2 (CF(R F2 )) y SO 2 X′ where

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Classifications

  • of R2C=O or R2C=NR (R= C, H) · CPC title

  • C07C29/175Primary

    with simultaneous reduction of an oxo group · CPC title

  • The ring being saturated · CPC title

  • containing polymers {(organometallic polymers B01J31/123; polymer-bound organometallic complexes B01J31/165; coordination polymers B01J31/1691)} · CPC title

  • of the platinum group metals, iron group metals or copper · CPC title

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What does patent US9944571B2 cover?
The present invention relates to a process for the one-pot hydrogenation and dehydration or isomerization of an organic compound, and to a catalyst composition for this process comprising transition metal particles having particle size below 50 nm supported on a material comprising at least one fluorinated polymer (P), wherein polymer (P) bears —SO 2 X functional groups, X being selected from X…
Who is the assignee on this patent?
Solvay Specialty Polymers It
What technology area does this patent fall under?
Primary CPC classification C07C29/175. Mapped technology areas include Chemistry & Metallurgy.
When was this patent published?
Publication date Tue Apr 17 2018 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).