Participants
| Role | Name | HCID | Charge |
|---|
| Reactant | Phenol | HCID 996 | — |
| Reactant | Dimethyl Carbonate | HCID 12021 | — |
| Reactant | Carbonic acid, methyl phenyl ester | HCID 139482 | — |
| Solvent | Methanol | HCID 887 | — |
| Product | Diphenyl carbonate | HCID 7597 | — |
Reaction Steps
In a column apparatus as described in Example 15, in which, instead of the 10-tray sieve-plate column, a 10-tray bubble-cap tray column, isothermically thermostatted to 183° C., of length 72 cm and internal diameter 4.75 cm was used, there was reacted, under the conditions described there, a mixture of 150 g/h of methyl phenyl carbonate, 350 g/h of phenol and 6.25 g/h of octylstannonic acid. After establishment of constant conditions, at the head of the apparatus, 365 g/h of a mixture of 1.3% by weight of methanol, 8.5% by weight of dimethyl carbonate and 90.2% by weight of phenol was continuously withdrawn and, at the foot of the column, 135 g/h of a mixture of 6.2% by weight of phenol, 14.0% by weight of methyl phenyl carbonate and 79.8% by weight of diphenyl carbonate were continuously withdrawn. This represents a space-time yield for the formation of diphenyl carbonate of 0.085 g·ml-1· h-1, based on the reactor volume. 16.6% of the methyl phenyl carbonate used reacted with phenol with transesterification to form diphenyl carbonate. The selectivity of the formation of diphenyl carbonate was >99%, 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-0d22fd6d91324b59b2d427b7ea3f512c |
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| Source note | uspto-grants-1994_09 |
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