反応式
[CH3:1][C:2]([CH2:7][CH3:8])([CH2:5][OH:6])[CH:3]=[O:4].O>CO>[CH3:1][CH:2]([CH2:7][CH3:8])[CH2:3][OH:4].[CH3:1][C:2]([CH2:7][CH3:8])([CH2:5][OH:6])[CH:3]=[O:4].[CH3:1][C:2]([CH2:7][CH3:8])([CH2:5][OH:6])[CH2:3][OH:4]参加物
実験手順
Using the method described in Example 1(b), one part per hour of a 70 percent strength by weight aqueous solution of 2-methyl-2-ethyl-3-hydroxypropanal is hydrogenated, over the catalyst prepared as described in Example 1(a), at 130° C. and 30 bar, with a throughput of 0.35 part of 2-methyl-2-ethyl-3-hydroxypropanal per liter of catalyst per hour. The conversion is 99 percent. The hydrogenated material is fractionated through a packed column. After first runnings of water and small amounts of methanol, 2-methylbutanol and 2-methyl-2-ethyl-3-hydroxypropanal, 2-methyl-2-ethyl-propane-1,3-diol, of boiling point of 110°-112° C./12 mbar (melting point 44°-46° C.), is obtained in an amount corresponding to 0.6850 part per hour. This is equivalent to a yield of 96.2% of theory, based on starting material.
後処理
- customprepared
- customas described in Example 1(a), at 130° C.
出典と根拠
- ORDレコード
- ord-1acb37bf5d674bf8a1917b6ec8183b56
- 出典データセット
- uspto-grants-1983_07
- 特許番号
- US04393251
関連ノート
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