Participants
| Role | Name | HCID | Charge |
|---|
| Reactant | Butanal | HCID 261 | — |
| Reactant | Formaldehyde | HCID 712 | — |
| Reactant | Triethylamine | HCID 8471 | — |
| Reactant | Triethylazanium;formate | HCID 10219518 | — |
| Product | Trimethylolpropane | HCID 6510 | 84% |
Reaction Steps
98.7 ml (0.71 mole)/hour of triethylamine, 42.9 ml (0.49 mole)/hour of n-butyraldehyde and 308.7 ml/hour of 15.2% strength formaldehyde solution (1.7 moles/hour of formaldehyde) are passed into a continuous reaction cascade which consists of three flasks connected in series, the reaction volume of each flask being 900 ml and the reaction temperature in each flask being 80° C. The reacted mixture from the cascade is fed to a continuous hydrogenation apparatus and is hydrogenated at 115° C. and under 60 bar, the catalyst consisting of 81.47% of NiO and 18.53% of Al2O3. Low boilers, and triethylammonium formate formed in the course of the reaction, are then separated off by distillation under reduced pressure (20 mbar). Fractional distillation of the residue under 3 mbar gives 125 g (84% yield) of trimethylolpropane per of hydrogenated mixture and 18 g (13% yield) of di-trimethylolpropane per of hydrogenated mixture, the stated % yields being based on n-butyraldehyde.
Provenance & Evidence
| DOI | 10.6084/m9.figshare.5104873.v1 |
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| Patent number | US04594461 |
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| Source dataset | uspto-grants-1986_06 |
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| ORD ID | ord-699c936dd83f4aea8e2e8e0340fb3b32 |
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| Source note | uspto-grants-1986_06 |
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