Participants
| Role | Name | HCID | Charge |
|---|
| Reactant | Acetic Acid | HCID 176 | — |
| Reactant | Nitrogen | HCID 947 | — |
| Reactant | Oxygen | HCID 977 | — |
| Reactant | Cyclohexane | HCID 8078 | — |
| Catalyst | Cobalt(II) acetate tetrahydrate | HCID 61372 | — |
| Product | Cyclohexanol | HCID 7966 | 70.3% |
| Product | Cyclohexanone | HCID 7967 | 28.2% |
| Product | Cyclohexyl acetate | HCID 12146 | 1.5% |
Reaction Steps
In a 316 stainless steel reactor having an internal volume of 300 ml, 26 g (309 mmol) of cyclohexane, 14 g of acetic acid, 179 mg (0.617 mmol) of bis(acetylacetonato)manganese(II) dihydrate, and 15.4 mg (0.0617 mmol) of cobalt(II) acetate tetrahydrate were placed, and the reactor was sealed and was pressurized to 50 Kg/cm2 (4.9 MPa) with a gaseous mixture comprising 50% of O2 and 50% of N2. The liquid temperature was raised on an oil bath and was held at 110° C. Immediately after the liquid temperature reached 110° C., absorption of the gas began. The reaction was terminated by cooling 60 minutes later. A reaction mixture was diluted with 60 g of acetic acid to thereby dissolve all of solid matters. The resulting solution was analyzed to find that a conversion from cyclohexane was 0.11% and adipic acid was not produced. In addition, cyclohexanone (selectivity: 28.2%), cyclohexanol (selectivity: 70.3%), and cyclohexyl acetate (selectivity: 1.5%) were produced.
Provenance & Evidence
| DOI | 10.6084/m9.figshare.5104873.v1 |
|---|
| Patent number | US07015356B2 |
|---|
| Source dataset | uspto-grants-2006_03 |
|---|
| ORD ID | ord-8ef503da2f5f426e81b729e65bcfc2fe |
|---|
| Source note | uspto-grants-2006_03 |
|---|