Participants
| Role | Name | HCID | Charge |
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| Reactant | Acetic Acid | HCID 176 | — |
| Reactant | Water | HCID 962 | — |
| Reactant | Toluene | HCID 1140 | — |
| Catalyst | Palladium | HCID 23938 | — |
| Product | Benzyl acetate | HCID 8785 | — |
Reaction Steps
A mixture of 70.7 wt. % acetic acid, 23.2 wt. % toluene and 6.1 wt. % water was first, at the rate of 0.198 gm./min., vaporized and then fed into a 3/8" I.D. stainless-steel tubular reactor packed with about 4.7 gm. of palladium on alumina support, at 160°-170° C. and about 30 psig. The palladium content contained in the supported catalyst was about 2% by weight. After about two hours of continuously running the reaction, the gaseous reaction product was directly sent to an on-line G.C. analyzer. The G.C. analysis showed that about 15% of toluene was converted; and that no product other than benzyl acetate was formed from the vapor phase reaction. A check based on the feed/product material balance indicated that the yield of benzyl acetate was over 90 mole % of toluene reacted.
Provenance & Evidence
| DOI | 10.6084/m9.figshare.5104873.v1 |
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| Patent number | US04350825 |
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| Source dataset | uspto-grants-1982_09 |
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| ORD ID | ord-57afbbebac13498da4f1afac79eab392 |
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| Source note | uspto-grants-1982_09 |
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