Participants
| Role | Name | HCID | Charge |
|---|
| Reactant | Water | HCID 962 | — |
| Reactant | 2-Methyl-2-phenylpropane-1,3-diol | HCID 90603 | — |
| Reactant | HCID 10535020 | HCID 10535020 | — |
| Reactant | Methanol--water (1/1) | HCID 22242641 | — |
| Solvent | Methanol | HCID 887 | — |
| Product | 2-Phenyl-1-propanol | HCID 14295 | — |
| Product | 2-Methyl-2-phenylpropane-1,3-diol | HCID 90603 | — |
| Product | HCID 10535020 | HCID 10535020 | — |
Reaction Steps
Using the method described in Example 1(b), 1.2 parts per hour of a 50 percent strength by weight solution of 2-methyl-2-phenyl-3-hydroxypropanal in a 1:1 water-methanol mixture are hydrogenated, over the catalyst prepared as described in Example 1(a), at 130° C. and 30 bar, with a throughput of 0.3 part of 2-methyl-2-phenyl-3-hydroxypropanol per liter of catalyst per hour. The conversion is over 99 percent. The hydrogenated material is fractionated through a packed column. After first runnings of water, methanol, 2-phenylpropanol and 2-methyl-2-phenyl-3-hydroxypropanal, 2-methyl-2-phenyl-propane-1,3-diol, of boiling point 143°-145° C./1 mbar (melting point 80°-82° C.), is obtained in an amount corresponding to 0.5405 part per hour. This is equivalent to a yield of 89% of theory, based on starting material.
Provenance & Evidence
| DOI | 10.6084/m9.figshare.5104873.v1 |
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| Patent number | US04393251 |
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| Source dataset | uspto-grants-1983_07 |
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| ORD ID | ord-c2e746feab4d4dafa2f931534b0d3e60 |
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| Source note | uspto-grants-1983_07 |
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