Participants
| Role | Name | HCID | Charge |
|---|
| Reactant | Butanal | HCID 261 | — |
| Reactant | 2-Heptanone | HCID 8051 | — |
| Product | Butanal | HCID 261 | — |
| Product | 2-Ethylhexanal | HCID 31241 | — |
Reaction Steps
The processes according to the invention may be carried out by passing the aldehyde and ketone reactant mixture, and the aldol catalyst solution, through a stationary bed of pelleted or supported hydrogenation catalysts, enclosed in a tubular reactor. This is typical of continuous fixed-bed plug-flow reactor processes, where the reactants are continually consumed as they flow down the length of the reactor. However, as seen in Example 2 (Comparative), when this continuous plug-flow fixed-bed concept is applied to the cross-aldol condensation of acetone and n-butyraldehyde, the selectivity of n-butyraldehyde to methyl amyl ketone is very low, only 38%. The main-by-product, 2-ethylhexaldehyde, the result of the self-aldol condensation of n-butyraldehyde, cannot be easily separated from the methyl amyl ketone by distillation.
Provenance & Evidence
| DOI | 10.6084/m9.figshare.5104873.v1 |
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| Patent number | US06979751B2 |
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| Source dataset | uspto-grants-2005_12 |
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| ORD ID | ord-80ad2cf836a94048a19d0b8a9d3e81d3 |
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| Source note | uspto-grants-2005_12 |
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