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Weygand/Hilgetag Preparative Organic Chemistry

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326 Formation of carbon-oxygen bonds<br />

temperature. Above this is a fractionating apparatus, in which the aldehyde product is separated<br />

from unchanged alcohol; the latter is returned to the boiling flask, and the former passes<br />

to a condenser and thence to a receiver; the hydrogen escapes. Detailed dimensions are<br />

suited to the conditions. For instance, if the catalyst tube is 1 m long its diameter is 25-30 mm.<br />

The copper catalyst may be prepared, e.g., from a small roll of copper-wire net filled with a<br />

copper oxide paste to which 1 % of silver oxide has been added. This catalyst is placed in<br />

position in the apparatus, dried in a stream of hydrogen while the temperature is raised slowly,<br />

and the oxide is then reduced, also slowly, at 300°, the time required being 8-10 h. It is then<br />

allowed to cool without exposure to the air. Atmospheric pressure can be used if the boiling<br />

point of the aldehyde does not exceed 200°; if it does, diminished pressure must be used.<br />

The catalyst space must be heated to a temperature slightly higher than the boiling point<br />

of the aldehyde product.<br />

Geraniol is converted into oc- and /?-citral at atmospheric pressure; phenethyl<br />

alcohol gives phenylacetaldehyde; cinnamaldehyde is obtained from cinnamyl<br />

alcohol in good yield by use of a silver catalyst at 200°/20 mm. 429 Bremner<br />

et al. 430 describe a laboratory method for oxidation of tetrahydrofurfuryl<br />

alcohol by air on silver wool.<br />

The following is a generally applicable procedure, applied here to the<br />

conversion of 1-nonanol into nonanal: 431<br />

The success of the operation depends on careful preparation of the dehydrogenating<br />

catalyst. An aqueous solution of pure copper nitrate is treated with the calculated amount<br />

of pure sodium hydroxide solution, and the precipitated copper(n) hydroxide is washed by<br />

decantation with lukewarm water until completely neutral. The excess of water is then sucked<br />

off on a filter without allowing the hydroxide to become dry. This material may be stored as<br />

a paste in closed vessels. The copper hydroxide paste is spread in a thin layer on pieces of<br />

copper gauze 10 x 5 cm, which are then formed into a roll 10 cm long an4 placed in a<br />

copper tube 80 cm long into which thirty such rolls can be packed. The copper gauze should<br />

not have too fine a mesh, otherwise the catalytic effect is less. For reduction of the copper<br />

hydroxide the whole system is first washed through with hydrogen that has been washed with<br />

permanganate and dried by sulfuric acid. The catalyst tube is then heated electrically to<br />

300°, whereby the hydroxide is converted into spongy metallic copper; this reduction requires<br />

8 h; the product is allowed to cool in a stream of hydrogen unless it is to be used immediately.<br />

If the material is to be kept overnight a constant slow stream of hydrogen is led through the<br />

apparatus. Before the dehydrogenation is begun the temperature is raised again to 300°<br />

for 0.5 h and the whole is washed through with hydrogen. Then 1-nonanol is brought into<br />

the boiling flask, the hydrogen stream is throttled back, the apparatus is evacuated to 3 to<br />

5 mm, the temperature in the catalyst space is adjusted to 240°, and the alcohol is brought to<br />

the boiling point. The receiver is arranged for collection of various fractions in a vacuum;<br />

so, if the rate of distillation becomes temporarily too fast so that unchanged nonanol passes<br />

over (recognized by a rise in temperature at the column head), then that portion of the<br />

distillate is collected separately.<br />

When the operation is finished, the apparatus is filled with hydrogen and allowed to cool<br />

without entry of air; the catalyst then retains its activity. The yield of nonanal amounts to<br />

90%, the b.p. being 78°/3 mm.<br />

More than monohydric alcohols can be only incompletely dehydrogenated,<br />

and carbohydrate alcohols do not survive attempted dehydrogenation.<br />

High-boiling.alcohols are sometimes better dehydrogenated in the liquid<br />

phase in presence of a hydrogen-acceptor such as copper and nitrobenzene<br />

or ra-dinitrobenzene. The preparation of o-chlorobenzaldehyde in 86% yield<br />

from 2-chlorobenzyl alcohol at 205-210° may be cited as example. 432<br />

429 C. Moureu and G. Mignonac, C. R. Hebd. Seances Acad. Set, 111, 652 (1920)<br />

430 I. G. M. Bremner and co-workers, /. Chem. Soc, 1949, Suppl., 25.<br />

431 A. Lewisohn, Perfum. Essent. Oil Rec, 15, 13 (1924).<br />

432 F. Zetsche and P. Zala, Helv. Chim. Acta, 9, 288 (1926).

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