Participants
| Role | Name | HCID | Charge |
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| Reactant | Phenol | HCID 996 | — |
| Reactant | Carbonic acid, methyl phenyl ester | HCID 139482 | — |
| Product | Diphenyl carbonate | HCID 7597 | — |
Reaction Steps
In the column apparatus described in Example 15, under the conditions described there, was reacted a mixture of 50 g/h of methyl phenyl carbonate, 200 g/h of phenol and 3.25 g/h of octylstannonic acid. After establishment of constant conditions, at the head of the apparatus, 210 g/h of a mixture of 1.0% by weight of methanol, 5.4% by weight of dimethyl carbonate and 93.6% by weight of phenol were continuously withdrawal and, at the foot of the column, 48 g/h of a mixture of 9.4% by weight of phenol, 1.9% by weight of methyl phenyl carbonate and 88.7% by weight of diphenyl carbonate were continuously withdrawn. This represented a space-time yield for the formation of diphenyl carbonate of 0.048 g·ml-1· h-1, based on the reactor volume. 20.5% of the methyl phenyl carbonate used reacted with phenol, transesterifying to form diphenyl carbonate. The selectivity of the formation of diphenyl carbonate was >99.9%, that is no by-products could be detected.
Provenance & Evidence
| DOI | 10.6084/m9.figshare.5104873.v1 |
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| Patent number | US05344954 |
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| Source dataset | uspto-grants-1994_09 |
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| ORD ID | ord-d749d2c44d064148a31bb1fea244dc47 |
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| Source note | uspto-grants-1994_09 |
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