Participants
| Role | Name | HCID | Charge |
|---|
| Reactant | Alumina | HCID 9989226 | — |
| Reactant | Monoepoxycyclododecadiene | HCID 54352584 | — |
| Reactant | HCID 178418361 | HCID 178418361 | — |
| Catalyst | Palladium | HCID 23938 | — |
| Product | Cyclododecanol | HCID 15595 | 20% |
Reaction Steps
Also, it is known that epoxidized cycloalkanes and/or epoxidized cycloalkenes can be produced by epoxidizing corresponding cycloalkenes with a high yield. If the epoxidized compounds can be converted to corresponding cycloalkanones and cycloalkanols with a high efficiency, the cycloalkanones and the cycloalkanols can be expected to be obtained at a high yield. However, only a small number of reports can be found on methods of converting an epoxidized cycloalkane and/or an epoxidized cycloalkene to a mixture of cycloalkanone with cycloalkanol. For example, J. Mol. Catal., Vol. 69, pages 69 to 103 (1991) discloses a method of hydrogenating a monoepoxycyclododecadiene with hydrogen in the presence of a catalyst comprising palladium carried on a carrier consisting of γ-alumina, under a hydrogen gas pressure of 1.3 MPa at a temperature of 90° C. In this method, cyclododecanol was produced with a yield of 20% or less and no cyclododecanone was produced. When a catalyst comprising palladium carried on a carrier consisting of titania or silica was used in place of the above-mentioned palladium catalyst carried on γ-alumina, the yield of cyclododecanol was low and unsatisfactory.
Provenance & Evidence
| DOI | 10.6084/m9.figshare.5104873.v1 |
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| Patent number | US06335472B1 |
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| Source dataset | uspto-grants-2002_01 |
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| ORD ID | ord-8965c465e8af40daa8c2bb28687f2b49 |
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| Source note | uspto-grants-2002_01 |
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