Participants
| Role | Name | HCID | Charge |
|---|
| Reactant | Acetic Acid | HCID 176 | — |
| Reactant | Carbon Dioxide | HCID 280 | — |
| Reactant | Cobalt | HCID 104730 | — |
| Solvent | Water | HCID 962 | — |
| Product | Cobalt diacetate | HCID 6277 | — |
| Product | Cobalt(1+), hydroxy- | HCID 6102352 | — |
Reaction Steps
The oxidation zone consisted of a vertical, glass tube oxidizer 60 inches (152.4 cm) in length and 2 inches (5.1 cm) in diameter having a capacity of 3.7L and equipped with inlets at the base for feeding air and the hydrolysis zone effluent. The top of the oxidizer was equipped with, in order, a heater exchanger for condensing acetic acid and water from the oxidizer vapor effluent, a vapor/liquid separator, a pressure-regulating valve, a trap cooled to -67° C. by dry ice (solid carbon dioxide) and a scrubber. The oxidizer is charged initially with an acetic acid solution containing 5 weight percent water and 0.3 weight percent cobalt, provided as cobalt hydrate or cobalt acetate. The oxidizer is heated to 130° C. by means of an electric heating cable and pressurized with air which was sparged to the bottom of the oxidation vessel while feeding either acetaldehyde or the EDA hydrolysis product.
Provenance & Evidence
| DOI | 10.6084/m9.figshare.5104873.v1 |
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| Patent number | US05175362 |
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| Source dataset | uspto-grants-1992_12 |
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| ORD ID | ord-182a87e3a74f41e78fca992239410b1a |
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| Source note | uspto-grants-1992_12 |
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