Participants
| Role | Name | HCID | Charge |
|---|
| Reactant | Ammonia | HCID 222 | — |
| Reactant | 2,6-Dimethylphenol | HCID 11335 | — |
| Reactant | Praseodymium oxide | HCID 165911 | — |
| Reactant | Alumina | HCID 9989226 | — |
| Catalyst | Palladium | HCID 23938 | — |
| Solvent | HCID 178418361 | HCID 178418361 | — |
| Product | 2,6-Dimethylcyclohexylamine | HCID 110932 | 96% |
Reaction Steps
A catalyst consisting of 1.0% by weight of palladium and 0.5% by weight of praseodymium oxide, the remainder being aluminum oxide, in extrudate form is introduced into a 1 l cylindrical reaction tube and is heated to 200° C. A mixture of 60 g of 2,6-dimethylphenol and 360 g of liquid ammonia per hour is passed over this catalyst bed. At the same time, 100 liters (S.T.P.) of hydrogen are passed in co-current through the reaction tube under a pressure of 200 bar. The reaction product which leaves the tube is cooled under superatmospheric pressure and is then let down. About 62 g of crude product, which gives 60 g of pure 2,6-dimethylcyclohexylamine (corresponding to a yield of 96%) on distillation, are thereby obtained per hour.
Provenance & Evidence
| DOI | 10.6084/m9.figshare.5104873.v1 |
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| Patent number | US04429155 |
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| Source dataset | uspto-grants-1984_01 |
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| ORD ID | ord-69e1b3a758594fbfa3369f462d571be0 |
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| Source note | uspto-grants-1984_01 |
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