HuagongsheHuagongshe Chemistry Print Report · For research reference only
Phenol → Cumene
Participants
| Role | Name | HCID | Charge |
|---|---|---|---|
| Reactant | Phenol | HCID 996 | — |
| Reactant | Carbonyl cyanide (m-chlorophenyl)hydrazone | HCID 2603 | — |
| Product | Phenol | HCID 996 | 4% |
| Product | Cumene | HCID 7406 | 10% |
Reaction Steps
According to A.C. CCCP 1235860 (1986) before decomposition, the phenol tar is diluted by high-molecular weight aromatic compounds such as Baltic shale oil (grade kerogen -70) weight ratio of tar to shale oil 1.3/2.5. Process conditions are: pressure 3-7 MP, temperature 400°-430 ° C., time 5-20 min. Liquid products obtained are separated by distillation. This process takes place under relatively severe conditions and gives a poor yield of phenol (4-5% ) and cumene (10-15% ). In addition it requires the addition of shale oil.
Provenance & Evidence
| DOI | 10.6084/m9.figshare.5104873.v1 |
|---|---|
| Patent number | US05504251 |
| Source dataset | uspto-grants-1996_04 |
| ORD ID | ord-2856fd1ce6664b169d97f4556107c5eb |
| Source note | uspto-grants-1996_04 |