Checked by R. L. Shriner and Philip R. Ruby.
1. Procedure
In a
1-l. round-bottomed flask, fitted with a heated
reflux condenser maintained at 100–110° (Note
1), are placed
44 g. of stearic acid (Note
2) and
20 g. (0.5 mole) of magnesium oxide (Note
3). The flask is immersed in a
Wood's metal bath heated at 335–340° (Note
4). After the reaction has proceeded for 1 hour, 10-g. portions of melted stearic are added down the condenser at 15-minute intervals until an additional 240 g. (284 g., 1 mole total) has been added (Note
5). The heating is continued until the total reaction time is 10 hours.
The reaction flask is removed from the metal bath and allowed to cool to about 100°, and the liquid contents are poured with stirring into
1 l. of 4N sulfuric acid in a
3-l. beaker. This mixture is boiled with vigorous mechanical stirring until the frothing ceases (Note
6) and the upper layer is clear (about 2 hours). The lower aqueous layer is then siphoned off, and the upper layer is boiled for 1 hour with 1 l. of water. The water layer is separated, and the upper layer is boiled with
1 l. of a 5% sodium hydroxide solution for 1 hour with vigorous stirring. The ketone layer is then separated and boiled for 1 hour each with three successive 1 l. portions of hot water (Note
7) with good stirring.
The crude
stearone is allowed to solidify and is then broken up and dried by pressing between filter paper. The crude yield is
230–240 g. (
91–95%). The product melts at
84–86° and has an acid value of zero. It is purified by dissolving in
1.2 l. of a 2:1 mixture of benzene and absolute ethanol, filtering hot, and allowing to crystallize (Note
8). After a second crystallization from the same mixed solvents, the
stearone is obtained as glistening white flakes, melting clear at
89–89.5° (shrinks at 87–88°). The yield is
204–220 g. (
81–87%) (Note
9).
2. Notes
1. The condenser, attached to the flask by a ground-glass joint, is a Pyrex tube 50 cm. long and 20 mm. in internal diameter, wound with No. 26 Nichrome wire covered with asbestos paper. It is connected to a variable transformer and adjusted so as to maintain a temperature of 100–110°. A
copper Liebig condenser heated by steam is also suitable provided that the inner tube has a diameter of about 20 mm.
2. The purity and melting point of the final product are dependent on the purity of the
stearic acid. If
Armour's Neo-Fat 1-65, m.p. 64–67° (90–95% stearic acid) is recrystallized first from
95% ethanol and then from acetone, a
stearic acid melting from
67° to 68° results which yields a
stearone with a melting point of
88–89° (shrinks at 86–88°).
In order to obtain
stearone with the highest melting point, the checkers found it necessary to purify the above recrystallized
stearic acid by converting it to the methyl ester and fractionating this ester under reduced pressure, using a
30-in. electrically heated packed fractionating column. The fraction boiling at
180–182°/4 mm.,
n40D 1.4364, is collected. The
methyl stearate solidifies on cooling and melts at
38–39°. Saponification and acidification yielded white crystals of
stearic acid melting clear at
69–69.3° (cor.).
Commercial "stearone" (Armour) is made from
Neo-Fat 1-60 (which is approximately 75% stearic and 25% palmitic acid) and melts at
80–84°.
3.
Merck's reagent-grade magnesium oxide is suitable. The submitters recommend 10 g. of catalyst, but this amount gave a
stearone with m.p.
87–88°. The larger amount, 20 g., gave a product melting clear at
89–89.5°.
4. The temperature of the bath should not be allowed to rise above 345°. Decomposition products are formed which lower the melting point of the final product.
5. With the rate of addition of
stearic acid given, the decomposition of
magnesium stearate maintains an excess of
magnesium oxide in the reaction mixture. Each addition of
stearic acid should take 1 to 2 minutes. Thus frothing of the reaction mixture is held under control; a brisk evolution of steam with a little entrained
stearic acid follows each addition but quickly subsides and is followed by a steady effervescence due to the liberation of
carbon dioxide.
6. A little unchanged
magnesium stearate may cause frothing at this stage, which may be controlled by the addition of a few drops of
2-octanol and by vigorous stirring, which hastens decomposition of the soap.
7. The removal of fatty acids from neutral higher aliphatic compounds requires vigorous stirring of the hot aqueous and organic phases.
8. The solubility of
stearone falls rapidly with temperature; a hot jacketed funnel is used with gentle suction.
9. This is a general method for the preparation of higher aliphatic ketones. It has been found suitable for the preparation of ketones from fatty acids containing 12 to 20 carbon atoms.
3. Discussion
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