Iron oxide supported rhodium catalyst for nitroarene reduction
US-11452992-B2 · Sep 27, 2022 · US
US11712680B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-11712680-B2 |
| Application number | US-202217820111-A |
| Country | US |
| Kind code | B2 |
| Filing date | Aug 16, 2022 |
| Priority date | Mar 20, 2019 |
| Publication date | Aug 1, 2023 |
| Grant date | Aug 1, 2023 |
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A supported catalyst having rhodium particles with an average diameter of less than 1 nm disposed on a support material containing magnetic iron oxide (e.g. Fe 3 O 4 ). A method of producing the supported catalyst and a process of reducing nitroarenes to corresponding aromatic amines employing the supported catalyst with a high product yield are also described. The supported catalyst may be recovered with ease using an external magnet and reused.
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The invention claimed is: 1. A process of reducing an aromatic nitro compound to an aromatic amine compound, the method comprising: mixing the aromatic nitro compound with a hydrogen transfer reagent in the presence of a supported catalyst and a solvent to form a reaction mixture; and heating the reaction mixture thereby forming the aromatic amine compound; wherein the supported catalyst comprises: a support material comprising Fe 3 O 4 ; and a catalytic material comprising rhodium disposed on the support material; wherein the catalytic material is in the form of subnanoparticles having an average particle size of 0.2-0.99 nm; the rhodium is present in an amount of 1-20 wt % relative to a total weight of the supported catalyst; and the support material is devoid of Al 2 O 3 . 2. The method of claim 1 , wherein the Fe 3 O 4 in the supported catalyst is in the form of nanospheres. 3. The method of claim 2 , wherein the nanospheres have an average particle size of 5-25 nm. 4. The method of claim 1 , wherein the rhodium in the supported catalyst is present in an amount of 4-10 wt % relative to a total weight of the supported catalyst. 5. The method of claim 1 , wherein the supported catalyst has a BET surface area in a range of 100-180 m 2 /g. 6. The method of claim 1 , wherein the supported catalyst has a saturation magnetization value in a range of 50-75 emu/g. 7. The process of claim 1 , wherein the hydrogen transfer reagent is tetrahydroxydiboron. 8. The process of claim 1 , wherein the supported catalyst is present in an amount of 1-50 g/mol relative to a molar amount of the aromatic nitro compound. 9. The process of claim 1 , wherein the reaction mixture is heated at a temperature of 30-80° C. 10. The process of claim 1 , wherein the reaction mixture is heated for 0.5-300 minutes. 11. The process of claim 1 , wherein the solvent is water. 12. The process of claim 1 , wherein the aromatic nitro compound is at least one selected from the group consisting of nitrobenzene, 2-nitrotoluene, 3-nitrotoluene, 4-nitrotoluene, 3-nitroaniline, 4-nitroanisole, 1,3-dimethyl-2-nitrobenzene, 2-nitrophenol, 4-nitrophenol, and 1-chloro-4-nitrobenzene. 13. The process of claim 1 , wherein the aromatic amine compound is at least one selected from the group consisting of aniline, 2-methylaniline, 3-methylaniline, 4-methylaniline, 1,3-diaminobenzene, 4-methoxyaniline, 2,6-dimethylaniline, 2-aminophenol, 4-aminophenol, and 4-chloroaniline. 14. The process of claim 1 , which has an aromatic amine compound yield of 35-99.9 mole % relative to a molar amount of the aromatic nitro compound. 15. The process of claim 1 , further comprising: separating the supported catalyst from the aromatic amine compound; and reusing the supported catalyst.
characterised by their crystalline properties, e.g. semi-crystalline (catalysts comprising carbon B01J21/18; molecular sieves B01J29/00) · CPC title
Nanoparticles · CPC title
Scanning electron microscopy; Transmission electron microscopy · CPC title
Metal or metal oxide crystallite size · CPC title
Indexing scheme associated with group B01J35/00, related to the analysis techniques used to determine the catalysts form or properties · CPC title
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