Participants
| Role | Name | HCID | Charge |
|---|
| Reactant | Heptanal | HCID 8130 | — |
| Reactant | Hex-2-ene | HCID 19966 | — |
| Reactant | HCID 178418361 | HCID 178418361 | — |
| Reactant | HCID 178418416 | HCID 178418416 | — |
| Catalyst | Rhodium | HCID 23948 | — |
| Solvent | Water | HCID 962 | — |
| Product | 1-Hexene | HCID 11597 | — |
| Product | Hex-2-ene | HCID 19966 | — |
Reaction Steps
20 parts by volume of the rhodium catalyst solution prepared as described in Example B are mixed with 800 parts by volume of polyethylene glycol 400 having a water content of 2% and are introduced into an autoclave whose gas space is then filled with an equimolar mixture of hydrogen and carbon monoxide under a total pressure of 80 bar. The solution is heated while stirring to 100° C., this temperature is held for another three hours while continuing to stir and while maintaining the pressure of 80 bar and 800 parts by volume of 2-hexene are then added while maintaining these reaction conditions, the reaction mixture is stirred for another two hours at 100° C. and 80 bar and, after cooling and venting the autoclave, the reaction mixture obtained is transferred to a phase separator in which the aldehyde phase having a heptanal content of 96% is separated off. As a result of the partial isomerization of 2-hexene to 1-hexene, this gives a mixture of 1-heptanal and 2-heptanal in a mixing ratio of 0.83. The yield of heptanal mixture is 96% of theory.
Provenance & Evidence
| DOI | 10.6084/m9.figshare.5104873.v1 |
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| Patent number | US06225508B1 |
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| Source dataset | uspto-grants-2001_05 |
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| ORD ID | ord-ac061a026fcb412383864096931b5cfb |
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| Source note | uspto-grants-2001_05 |
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