Process for conversion of propane and apparatus
US-2015375196-A1 · Dec 31, 2015 · US
US9289759B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9289759-B2 |
| Application number | US-201213611089-A |
| Country | US |
| Kind code | B2 |
| Filing date | Sep 12, 2012 |
| Priority date | Sep 13, 2011 |
| Publication date | Mar 22, 2016 |
| Grant date | Mar 22, 2016 |
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Provided is a novel iridium catalyst complex which is useful in the dehydrogenation of alkanes. The iridium complex comprises the metal iridium atom complexed with a benzimidazolyl-containing ligand. The iridium atom can be coordinated with the nitrogen atoms in the benzimidazolyl-containing ligand to form an NCN pincer ligand complex. In another embodiment, the iridium catalyst is used, with or without a co-catalyst, in a dehydrogenation reaction converting alkanes to olefins. The reaction can be in a closed or open system, and can be run in a liquid or gaseous phase.
Opening claim text (preview).
That which is claimed is: 1. An iridium catalyst complex of the formula LMX(X′) n , where n =0, 1 or 2; X and X′ are moieties which can be eliminated from the metal center to generate a catalytically active LM fragment; M is iridium; and L is the ligand 2,2′-(1,3-phenylene) bis (1-propylbenzimidazol 2 yl). 2. A catalyst composition comprising the iridium catalyst complex of claim 1 and a co-catalyst. 3. A method of dehydrogenating alkanes which comprises contacting an alkane under dehydrogenation conditions in the presence of an iridium catalyst complex of the formula LMX(X′) n , where n =0, 1 or 2; X and X′ are moieties which can be eliminated from the metal center to generate a catalytically active LM fragment; M is iridium; and L is a ligand having the formula: wherein A and A′ are independently selected from the group consisting of: where R 1 , R 2 ,R 3 , and R* 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 and C 7 through C 17 aralkyl olefins; and Y is selected from the group consisting of C—H, C—C 1 , C—Br, C—I, N, P, C—OR 4 wherein R 4 is hydrogen, an optionally substituted acyl group, an optionally substituted alkylsulfonyl group or other leaving group; and p=0,1 or 2. 4. A method of dehydrogenating alkanes which comprises contacting an alkane under dehydrogenation conditions in the presence of the catalyst of claim 1 . 5. The method of claim 3 , wherein the reaction is run with a high boiling alkane having a boiling point of at least 200° C., in an open reactor. 6. The method of claim 5 , wherein the alkane is a C 12 or higher alkane. 7. The method of claim 3 , wherein the dehydrogenation reaction is run in the presence of oxygen. 8. The method of claim 3 , wherein the reaction is run in a closed system. 9. The method of claim 8 , wherein the reaction is run with an alkane which is lower than a C 12 alkane. 10. The method of claim 3 , wherein the alkane is a C 4 - C 20 alkane. 11. The method of claim 3 , wherein an olefin product is recovered. 12. The method of claim 7 , wherein the contacting is conducted in the gaseous phase. 13. The method of claim 4 , wherein a co-catalyst is used for the contacting.
with a hydrocarbon as an acceptor, e.g. hydrocarbon disproportionation, i.e. 2CnHp -> CnHp+q + CnHp-q · CPC title
Catalytic processes · CPC title
Alkadienes · CPC title
without a metal-carbon linkage · CPC title
Alkenes · CPC title
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