Participants
| Role | Name | HCID | Charge |
|---|
| Reactant | Acetaldehyde | HCID 177 | — |
| Reactant | Oxygen | HCID 977 | — |
| Reactant | Acetic Anhydride | HCID 7918 | — |
| Catalyst | Copper | HCID 23978 | — |
| Catalyst | Cobalt | HCID 104730 | — |
| Solvent | Acetic Acid | HCID 176 | — |
| Product | AcOH AcOAc | HCID 21895370 | — |
Reaction Steps
A process for the continuous production of acetic acid and acetic anhydride by reacting acetaldehyde by oxidizing it with gaseous oxygen in liquid phase in the presence of copper acylate and cobalt acylate as a catalyst and in the presence of an aliphatic carboxylic acid ester as a diluent in a reaction zone, which comprises: effecting the reaction at temperatures of 62° to 90° C. over a period of less than 20 minutes with the use of the diluent and acetaldehyde in a quantitative ratio of 60:40 to 40:60; delivering the resulting reaction products to a distilling zone; distilling overhead the carboxylic acid ester and water; separating the carboxylic acid ester phase from the water phase and recycling the organic phase with a reflux ratio of at least 1:1 to the distilling zone; delivering base product accumulating in the distilling zone to an evaporating zone and evaporating it therein so as to obtain 2 to 12 parts by weight of an acetic acid/acetic anhydride-mixture as distillate per part by weight of catalyst solution as base product.
Provenance & Evidence
| DOI | 10.6084/m9.figshare.5104873.v1 |
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| Patent number | US04252983 |
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| Source dataset | uspto-grants-1981_02 |
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| ORD ID | ord-513780b30f224327b20cfe0df78750cb |
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| Source note | uspto-grants-1981_02 |
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