Participants
| Role | Name | HCID | Charge |
|---|
| Reactant | Methacrolein | HCID 6562 | — |
| Reactant | 1,4-Butanediol | HCID 8064 | — |
| Reactant | Allyl acetate | HCID 11584 | — |
| Reactant | Butanediol | HCID 165788 | — |
| Solvent | Acetic Acid | HCID 176 | — |
| Solvent | Water | HCID 962 | — |
| Product | 1,2-Butanediol | HCID 11429 | 13% |
| Product | Methylpropanediol | HCID 75103 | 5% |
Reaction Steps
The low boiling components of the hydrogenation mixture (principally water, acetic acid and hydrogenation products derived from methacrolein and allyl acetate) are distilled off under reduced pressure. The residue is subjected to the magnesia - promoted methanolysis in a manner similar to that described in Example II. It is passed continuously down through an 8 ft. × 1 in. diameter tube packed with one liter of the catalyst described in Example II and maintained at 130°C, against a countercurrent of methanol vapor (2000 grams per 800 gram charge per hour). Methyl acetate and the excess methanol are condensed from the top effluent, and a butanediol-rich trickle phase is taken into the boiler. Analysis of the latter (in a case using a single charge) by quantitative glpc shows the presence of 248 g of 1.4 - butanediol (69% yield in the conversion from allyl acetate), 17 grams of 2-methyl-1,3-propanediol (5% yield), and 47 grams of 1,2-butanediol (13% yield).
Provenance & Evidence
| DOI | 10.6084/m9.figshare.5104873.v1 |
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| Patent number | US03981931 |
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| Source dataset | uspto-grants-1976_09 |
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| ORD ID | ord-29375fc2b3c74f6daf204b96a6513d6f |
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| Source note | uspto-grants-1976_09 |
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