Participants
| Role | Name | HCID | Charge |
|---|
| Reactant | (-)-Menthol | HCID 16666 | — |
| Catalyst | Nickel | HCID 935 | — |
| Product | (-)-Isopulegol | HCID 170833 | — |
Reaction Steps
In the middle of the column at a height of 331 cm, 900 g/h of liquid L-menthol of synthetic origin were fed to the dividing wall column in the feed section of the dividing wall, which had been obtained by catalytic hydrogenation of L-isopulegol over a nickel catalyst, and comprised 99.39 GC area % L-menthol, 0.29 GC area % isopulegol, 0.25 GC area % neomenthol and 0.011 GC area % isomenthol, and also 0.044 GC area % neoisomenthol. The column was operated at top pressure 50 mbar and a return rate of 3.0 kg/h. A pressure drop of about 35 mbar (±1 mbar) was established. At the top of the column, a temperature of 120° C. was measured, and in the bottom a temperature of 135° C. (±0.5 K). The column was operated without a bottom draw and the distillate withdrawal was adjusted by means of a balance control system to 15 g/h (±1 g/h). The reflux ratio was thus about 200:1. The condenser of the column was at a temperature of 40° C. in order to prevent solids formation.
Provenance & Evidence
| DOI | 10.6084/m9.figshare.5104873.v1 |
|---|
| Patent number | US08414744B2 |
|---|
| Source dataset | uspto-grants-2013_04 |
|---|
| ORD ID | ord-0407f84b2793421ca1948d7b6f16da22 |
|---|
| Source note | uspto-grants-2013_04 |
|---|