Participants
| Role | Name | HCID | Charge |
|---|
| Reactant | Phenol | HCID 996 | — |
| Reactant | Carbonic acid, methyl phenyl ester | HCID 139482 | — |
| Product | Diphenyl carbonate | HCID 7597 | — |
Reaction Steps
A mixture of 75 g/h of methyl phenyl carbonate, 175 g/h of phenol and 3 g/h of octylstannonic acid was continuously fed into this reactor at the feeding point above the sieve-point column. At the same time, a gentle nitrogen stream of 2 [1.h-1 ] from the spiral tube evaporator was passed in the opposite direction to this starting material stream. After establishment of constant conditions, at the head of the apparatus, 195 g/h of a mixture of 2.2% by weight of methanol, 13.7% by weight of dimethyl carbonate and 84.1% by weight of phenol were continuously withdrawn, and at the foot of the column, 61 g/h of a mixture of 1.5% by weight of phenol, 0.9% by weight of methyl phenyl carbonate and 97.6% by weight of diphenyl carbonate were continuously withdrawn. This represented a space-time yield for the formation of diphenyl carbonate of 0.06 g/mlh, based on the reactor volume. 18.6% 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-46b44cdee47b48f0a4fdfce24648e0f7 |
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| Source note | uspto-grants-1994_09 |
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