Participants
| Role | Name | HCID | Charge |
|---|
| Reactant | Acetone | HCID 180 | — |
| Reactant | Phenol | HCID 996 | — |
| Reactant | Cumen hydroperoxide | HCID 53627471 | — |
| Product | Phenol | HCID 996 | — |
| Product | Dicumyl peroxide | HCID 6641 | — |
Reaction Steps
In another embodiment, a method for the production of phenol and acetone from a cumene hydroperoxide mixture comprises: a first stage and a second stage and at least two serially connected reactors, wherein the first stage comprises decomposition of a cumene hydroperoxide in the presence of a catalyst mixture to form phenol, acetone, and dicumyl peroxide mixture, and the second stage comprises formation of a phenol and acetone mixture from decomposition of the remainder of the cumene hydroperoxide and dicumyl peroxide formed in the first stage, wherein, the first stage further comprises: a) forming the catalyst mixture in a catalyst formation reactor by combining sulfuric acid and phenol in a weight ratio of from 2:1 to 1:1000, wherein the sulfuric acid is an aqueous sulfuric acid solution comprising at least 75 wt. % sulfuric acid; b) holding the catalyst mixture in the catalyst formation reactor at a temperature of about 35 to 45° C. for about 60 to 300 minutes; and c) adding the catalyst mixture to the cumene hydroperoxide mixture to form the phenol and acetone mixture, wherein the phenol and acetone mixture formed has a reduced level of hydroxyacetone as compared to a phenol and acetone mixture formed using a catalyst that is only sulfuric acid.
Provenance & Evidence
| DOI | 10.6084/m9.figshare.5104873.v1 |
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| Patent number | US07485758B2 |
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| Source dataset | uspto-grants-2009_02 |
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| ORD ID | ord-05ceaca6fe2844c1a0cb9b27cbce3ac6 |
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| Source note | uspto-grants-2009_02 |
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