Methods for making linear internal olefins from mixtures of linear and branched olefins
US-2024051900-A1 · Feb 15, 2024 · US
US9828310B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9828310-B2 |
| Application number | US-201715412523-A |
| Country | US |
| Kind code | B2 |
| Filing date | Jan 23, 2017 |
| Priority date | Sep 10, 2013 |
| Publication date | Nov 28, 2017 |
| Grant date | Nov 28, 2017 |
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Provided is a Group 9 novel metal catalyst complex further comprising a ketone-containing cocatalyst. The metal catalyst complex is useful in generating olefins from alkanes with great efficiency. In one embodiment, provided is an iridium catalyst complex useful in the dehydrogenation of alkanes comprising a ketone-containing cocatalyst and iridium complexed with a tridentate ligand. Also provided is a novel dehydrogenation method which utilizes the catalyst composition. In other embodiments, a novel process for preparing oligomers from alkanes utilizing the catalyst composition is provided.
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That which is claimed is: 1. A method of dehydrogenating alkanes which comprises contacting an alkane under dehydrogenation conditions in the presence of a catalyst composition comprising a ketone containing cocatalyst and a Group 9 metal complex, wherein the metal complex is a composition of the formula LMX(X′) n , where n=0, 1 or 2; X and X′ are moieties into which a monomer can insert or which can be eliminated from the metal center to generate a fragment LM; M is a Group 9 metal; and L is a tridentate ligand with L having the formula: wherein A and A′ are independently selected from the group consisting of: R 1 , R 2 , R 3 and R* are independently selected from the group consisting of halide, hydride, triflate, acetate, borate, C 1 through C 12 alky, C 1 through C 12 alkoxy, C 3 through C 12 cycloalkyl, C 3 through C 12 cycloalkoxy, C 6 through C 14 aryl, C 7 through C 17 aralkyl and olefins; and Y is selected from the group consisting of C—H, C—Cl, C—Br, C—I, N, P, C—OR 4 , wherein R 4 is hydrogen, an optionally substituted acyl group, a substituted or unsubstituted alkylsulfonyl group, or other leaving group; and p=0, 1 or 2. 2. The method of claim 1 wherein the ligand is 2, 6-bis (di-iso-propylphosphino) phenyl-1. 3. The method of claim 1 , wherein the reaction is run with a high boiling alkane having a boiling point of at least 200° C., in an open reactor. 4. The method of claim 3 , wherein the alkane is a C 12 or higher alkane. 5. The method of claim 1 , wherein the dehydrogenation reaction is run in the presence of oxygen. 6. The method of claim 1 , wherein the reaction is run in a closed system. 7. The method of claim 6 , wherein the reaction is run with an alkane which is lower than a C 12 alkane. 8. The method of claim 1 , wherein an olefin product is recovered. 9. The method of claim 5 , wherein the contacting is conducted in the gaseous phase. 10. The method of claim 5 , wherein an olefin product is further reacted within the reactor system. 11. A process for preparing oligomers from an alkane, comprising (a) contacting an alkane under dehydrogenation conditions in accordance with the method of claim 1 to form olefins, (b) contacting the olefins prepared in step (a) under oligomerization conditions with an oligomerization catalyst to prepare oligomers of the olefins, and (c) hydrogenating the olefin oligomers, with all reactions occurring in a single reactor. 12. The process of claim 11 , wherein the oligomerization catalyst of step (b) comprises a nickel, platinum or palladium metal catalyst complex comprising the metal complexed with a nitrogen containing bi- or tridentate ligand. 13. The process of claim 12 , wherein the metal catalyst complex of step (b) is of the formula LMX(X′) n , where n=0, 1 or 2; X and X′ are moieties into which a monomer can insert; M is selected from the group consisting of nickel, platinum and palladium; and L is a nitrogen containing bi- or tridentate ligand. 14. The process of claim 13 , wherein L is a benzimidazolyl based ligand. 15. The process of claim 13 , wherein X and X′ are independently selected from the group consisting of halides, hydride, triflate, acetates, borates, C 1 through C 12 alky, C 1 through C 12 alkoxy, C 3 through C 12 cycloalkyl, C 3 through C 12 cycloalkoxy, C 6 through C 14 aryl, C7 through C17 aralkyl and olefins. 16. The process of claim 13 , wherein L has the formula wherein A and A′ are independently selected from the group consisting of: R 1 , R 2 , R 3 and R* are independently selected from the group consisting of halide, hydride, triflate, acetate, borate, C 1 through C 12 alky, C 1 through C 12 alkoxy, C 3 through C 12 cycloalkyl, C 3 through C 12 cycloalkoxy, C 6 through C 14 aryl, C 7 through C 17 aralkyl and olefins; and Y is selected from the group consisting of C—H, C—Cl, C—Br, C—I, N, P, C—OR 4 , wherein R 4 is hydrogen, an optionally substituted acyl group, a substituted or unsubstituted alkylsulfonyl group, or other leaving group; and p=0, 1 or 2. 17. The process of claim 13 , wherein the olefins of step (b) are contacted with a combination of the metal catalyst complex and a co-catalyst. 18. The process of claim 11 , wherein said alkane is selected from the group consisting of straight chain alkanes, branched chain alkanes and cycloalkanes. 19. The process of claim 18 , wherein said alkane is a straight chain or branched chain alkane. 20. The process of claim 11 , wherein the oligomerization catalyst is a nickel, platinum or palladium metal catalyst complex, and the ligands are the same as in the Group 9 metal catalyst complex. 21. The method of claim 1 , wherein the Group 9 metal is iridium. 22. The method of claim 1 , wherein the ketone cocatalyst comprises benzophenone.
Phosphines · CPC title
with more than one complexing nitrogen atom, e.g. phenanthroline · CPC title
Catalytic processes · CPC title
containing organic compounds or metal hydrides · CPC title
with oxygen as an acceptor · CPC title
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