Stable long-term method for producing C5-aldehydes
US-9272973-B2 · Mar 1, 2016 · US
US11840506B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-11840506-B2 |
| Application number | US-202318310975-A |
| Country | US |
| Kind code | B2 |
| Filing date | May 2, 2023 |
| Priority date | May 3, 2022 |
| Publication date | Dec 12, 2023 |
| Grant date | Dec 12, 2023 |
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A process for preparing C 5 aldehydes involves hydroformylation of butenes with synthesis gas in the presence of a homogeneous catalyst system and a solvent. It is a feature of the process that the aldehyde concentration in the reaction mixture is limited.
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The invention claimed is: 1. A process for preparing C 5 aldehydes by hydroformylation of butenes, the process comprising: reacting the butenes with synthesis gas in at least one reaction zone of a reactor, in the presence of a homogeneous catalyst system and of a solvent, wherein a cycle gas containing at least a portion of product aldehydes, unconverted butenes, and butanes is removed from the at least one reaction zone, and wherein an aldehyde concentration in a liquid reaction mixture in the reactor is kept below 15% by mass by the cycle gas. 2. The process according to claim 1 , wherein the cycle gas removed from the at least one reaction zone is first directed to an aerosol separator. 3. The process according to claim 2 , wherein the cycle gas downstream of the aerosol separator is directed to a condenser, wherein the product aldehydes present in the cycle gas, the unconverted butenes, and the solvent are condensed out. 4. The process according to claim 3 , wherein a condensed liquid phase and a gas phase are separated from one another in a phase separator. 5. The process according to claim 4 , wherein the gas phase is recycled to the at least one reaction zone via a cycle gas compressor. 6. The process according to claim 4 , wherein the condensed liquid phase is directed to a C 4 /C 5 separation consisting of one or more distillation columns. 7. The process according to claim 6 , wherein previously removed product aldehydes and the solvent are separated from one another in a solvent removal, and the solvent is recycled to the reactor. 8. The process according to claim 1 , wherein the solvent has a higher boiling point than the product aldehydes. 9. The process according to claim 1 , wherein the solvent is isononyl benzoate (INB) or diisononyl cyclohexane-1,2-dicarboxylate (DINCH). 10. The process according to claim 1 , wherein the hydroformylation in the at least one reaction zone additionally takes place in the presence of a stabilizer. 11. The process according to claim 10 , wherein the stabilizer is an organic amine compound containing at least one 2,2,8,8-tetramethylpiperidine unit of formula (I): 12. The process according to claim 1 , wherein the homogeneous catalyst system comprises a metal from group 8 or 9 of the Periodic Table of the Elements, and at least one organic phosphorus-containing ligand. 13. The process according to claim 12 , wherein the metal is iron, ruthenium, iridium, cobalt, or rhodium. 14. The process according to claim 1 , wherein the homogeneous catalyst system comprises rhodium and a ligand having the structure of formula (1): 15. A liquid mixture, comprising: an aldehyde, cobalt or rhodium, an organic phosphorus-containing ligand, and a solvent, wherein an aldehyde concentration in the liquid mixture is below 15% by mass. 16. The process according to claim 12 , wherein the at least one organic phosphorus-containing ligand is a mono- or biphosphate ligand. 17. The process according to claim 13 , wherein the metal is cobalt or rhodium.
Asymmetric hydroformylation · CPC title
Phosphites ((RO)3P) , their isomeric phosphonates (R(RO)2P=O) and RO-substitution derivatives thereof · CPC title
by extractive distillation · CPC title
by oxo-reactions · CPC title
by distillation · CPC title
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