Participants
| Role | Name | HCID | Charge |
|---|
| Reactant | Butanal | HCID 261 | — |
| Reactant | HCID 178418361 | HCID 178418361 | — |
| Solvent | 1-Butanol | HCID 263 | — |
| Product | Butyl butyrate | HCID 7983 | — |
Reaction Steps
Further n-butyraldehyde is supplied to nozzle 123 in second vaporiser 122 by way of line 124. Reference numeral 125 indicates a distribution tray. A hot vaporous mixture comprising unreacted hydrogen from first catalytic stage 116, product n-butanol, inerts, and a minor amount of by-products, e.g. n-butyl n-butyrate, also formed in first catalytic stage 116, exits vaporiser 122 overhead in line 126 at a temperature of 105° C. After passage through a heater 127, supplied with a suitable heating medium, e.g. steam, in line 128, the mixture passes on in line 129 at a temperature of 125° C. to second catalytic stage 130. The aldehyde is quantitatively hydrogenated, n-butanol being the major product, under adiabatic conditions. The temperature of the vaporous reaction mixture exiting second catalytic stage 130 in line 131 is 195° C. After heat recovery in heat exchanger 132 by indirect heat exchange with a cooling medium, e.g. boiler feed water, supplied in line 133, the reaction mixture, now at 150° C. passes on in line 109 to heat exchanger 108.
Provenance & Evidence
| DOI | 10.6084/m9.figshare.5104873.v1 |
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| Patent number | US04451677 |
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| Source dataset | uspto-grants-1984_05 |
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| ORD ID | ord-9978d5afff7b41c2a7748850c7ec09bd |
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| Source note | uspto-grants-1984_05 |
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