Process for regenerating a catalyst for the hydroformylation of olefins in the gas phase
US-2022379294-A1 · Dec 1, 2022 · US
US11033890B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-11033890-B2 |
| Application number | US-201816638420-A |
| Country | US |
| Kind code | B2 |
| Filing date | Nov 2, 2018 |
| Priority date | Nov 13, 2017 |
| Publication date | Jun 15, 2021 |
| Grant date | Jun 15, 2021 |
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Some embodiments of the present invention relate to processes to recover rhodium from a hydroformylation process. In some embodiments, the process to recover rhodium from the hydroformylation process comprises (a) treating a catalyst-containing stream from the hydroformylation process with 2.5 to 20 weight percent, based on the total weight of the stream, of a water-soluble organic amine of the following structure: wherein R 32 , R 33 , and R 34 are each independently alkyls and ethoxylates, and wherein no more than one of R 32 , R 33 , and R 34 is alkyl; (b) heating the resulting solution in the presence of syngas to a temperature of at least 65° C. to generate a rhodium-rich phase and a supernatant; and (c) removing the supernatant to recover the rhodium-rich phase.
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What is claimed is: 1. A process to recover rhodium from a hydroformylation process that comprises producing at least one aldehyde in a reaction zone, the reaction zone comprising a C 7 to C 22 olefin, hydrogen and carbon monoxide in the presence of a catalyst, wherein the catalyst comprises rhodium and an organophosphorus ligand, wherein the process comprises: (a) treating a catalyst-containing stream from the hydroformylation process with 2.5 to 20 weight percent, based on the total weight of the stream, of a water-soluble organic amine of the following structure: wherein R 32 , R 33 , and R 34 are each independently alkyls and ethoxylates, and wherein no more than one of R 32 , R 33 , and R 34 is alkyl; (b) heating the resulting solution in the presence of syngas to a temperature of at least 65° C. to generate a rhodium-rich phase and a supernatant; and (c) removing the supernatant to recover the rhodium-rich phase. 2. The process of claim 1 , wherein the ligand is an organomonophosphite. 3. The process of claim 1 , wherein R 32 , R 33 , and R 34 are each ethoxylates. 4. The process of claim 1 , wherein the water-soluble organic amine is triethanolamine. 5. The process of claim 1 , further comprising returning the rhodium-rich phase to the reaction zone. 6. The process of claim 1 , further comprising treating the rhodium-rich phase with an organic solvent, and returning the treated rhodium-rich phase to the reaction zone. 7. The process of claim 1 , further comprising separating the rhodium from the rhodium-rich phase by acidifying the rhodium-rich phase to a pH less than 6 in the presence of water and a water-immiscible organic solvent, and optionally in the presence of an organophosphorus ligand, and returning the rhodium-containing organic solvent to the reaction zone. 8. The process of claim 1 , wherein the syngas is provided in step (b) at atmospheric pressure or higher. 9. The process of claim 1 , wherein the catalyst-containing stream is a liquid purge stream from the hydroformylation process. 10. The process of claim 1 , wherein at least 50 weight percent of the rhodium from the catalyst-containing stream is present in the rhodium-rich phase. 11. The process of claim 1 , further comprising: (d) treating the supernatant from step (c) with 2.5 to 20 weight percent of the water-soluble organic amine; and (e) heating the treated supernatant in the presence of syngas to a temperature of at least 65° C. to generate a second rhodium-rich phase and a second supernatant.
Hydroformylation, metalformylation, carbonylation or hydroaminomethylation · CPC title
containing rhodium · CPC title
Recycling of unreacted starting or intermediate materials · CPC title
Recycling of catalysts · CPC title
Heat treatment · CPC title
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