Participants
| Role | Name | HCID | Charge |
|---|
| Reactant | Butanal | HCID 261 | — |
| Reactant | 2-Ethyl-1,3-Hexanediol | HCID 7211 | — |
| Product | 2-Ethylhexanol | HCID 7720 | — |
| Product | 2-Ethylhex-2-Enal | HCID 12582 | — |
Reaction Steps
According to the present invention, 2-ethyl-1,3-hexane diol is thus prepared from n-butyraldehyde. 0.5-10% by weight, preferably 5-15% by weight, of a neutral phase-transfer catalyst is added to n-butyraldehyde, one such catalyst being, for example, polyethylene glycol (PEG 400), whereafter the mixture is cooled to 0°-20° C. The reaction may also be started from room temperature, but preferably so that the mixture is first cooled. Most preferably the reaction mixture is cooled to a temperature of 5°-15° C., and thereafter an aqueous solution of an alkali metal hydroxide or alkali earth metal hydroxide catalyst is added to the mixture drop by drop at such a rate that the reaction clearly starts, i.e. the temperature of the mixture clearly rises from its original value. The alkali metal hydroxide or alkali earth metal hydroxide is used in a proportion of 0.01-5% by weight, preferably 0.1-1% by weight, to n-butyraldehyde. The adding of the aqueous solution of the catalyst is discontinued when the temperature of the mixture has risen to the range 25°-45° C., preferably, however, to the range 30°-40° C. After the discontinuation of the adding of the catalyst, the mixture is further stirred for 0-5 h, preferably 0.2-3 h, whereafter the organic phase and the aqueous phase are separated from each other. Before the separation of the phases the reaction mixture may be neutralized with a mineral acid or an organic acid. The organic phase is recovered, and it is hydrogenated by catalytic hydrogenation at a temperature of 30°-200° C. and a pressure of 5-100 bar, preferably at a temperature of 60°-140° C. and a pressure of 10-60 bar. The hydrogenation may be carried out by using, for example, a Raney nickel catalyst. After the hydrogenation the product is vacuum distilled. The boiling point of 2-ethyl-1,3-hexane diol is 100° C./6 mbar, and a yield of up to more than 55% is obtained. When the process according to the invention is used, the worst byproduct, 2-ethyl hexanol via 2-ethyl hexenal, is formed at maximum at a rate of 2.6%. The rest of the reaction mixture is unreacted n-butyraldehyde which has become reduced to 1-butanol.
Provenance & Evidence
| DOI | 10.6084/m9.figshare.5104873.v1 |
|---|
| Patent number | US05663452 |
|---|
| Source dataset | uspto-grants-1997_09 |
|---|
| ORD ID | ord-0cfd7b986b624ab29a4e7a58d06f3558 |
|---|
| Source note | uspto-grants-1997_09 |
|---|