Participants
| Role | Name | HCID | Charge |
|---|
| Reactant | Benzene | HCID 241 | — |
| Reactant | HCID 178418361 | HCID 178418361 | — |
| Reactant | HCID 178418416 | HCID 178418416 | — |
| Catalyst | Palladium | HCID 23938 | — |
| Product | Cyclohexylbenzene | HCID 13229 | — |
Reaction Steps
In addition, U.S. Pat. No. 5,146,024 discloses that benzene can be reacted with hydrogen in the presence of carbon monoxide and a palladium-containing zeolite X or Y to produce cyclohexylbenzene, which can then be converted in high yield to phenol and cyclohexanone by autooxidation with subsequent acid treatment. The hydroalkylation reaction is carried out at a liquid hourly space velocity (LHSV) of the benzene feed of about 1 to about 100 hr−1, a total reaction pressure of about 345 to about 10,350 kPa, a molar ratio of H2 to benzene of about 0.1:1 to about 10:1, a molar ratio of carbon monoxide to H2 of about 0.01:1 to about 0.3:1, and a temperature of about 100 to about 250° C. Preferred operating conditions are said to include a LHSV of the benzene feed of about 5 to about 30 hr−1, a total reaction pressure of about 1,380 to about 4,830 kPa, a molar ratio of H2 to benzene of about 0.2:1 to about 1:1, a molar ratio of CO to H2 of about 0.02:1 to about 0.1:1, and a reaction temperature of about 140 to about 200° C.
Provenance & Evidence
| DOI | 10.6084/m9.figshare.5104873.v1 |
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| Patent number | US08084648B2 |
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| Source dataset | uspto-grants-2011_12 |
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| ORD ID | ord-9bfff245f58b4befb42cd2c12114a91e |
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| Source note | uspto-grants-2011_12 |
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