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Weygand/Hilgetag Preparative Organic Chemistry

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Addition of hydrogen to C=C bonds and aromatic systems 23<br />

Formation of the alloy is accompanied by evolution of much heat. Because<br />

of the increase in temperature higher-melting alloys can often be obtained<br />

with a greater content of active metal. In the presence of atmospheric oxygen<br />

an aluminothermic reaction may lead to a further rise in temperature. Care<br />

is therefore necessary! The melt can be protected against attack by atmospheric<br />

oxygen by covering it with a layer of salt or by means of an inert<br />

gas.<br />

Alloys ready for use can now be obtained commercially.<br />

After decomposition of the aluminum alloys there is still residual aluminum<br />

in the metal, and this residue seems to be in part responsible for the activity of<br />

the catalyst. If this residue is largely removed by continued extraction, the<br />

catalyst becomes inactive. 157 Alloys containing more than 75% of nickel are<br />

only partly attacked by aqueous sodium hydroxide, or are not attacked at all;<br />

then decomposition has to be undertaken with very concentrated sodium<br />

hydroxide solution or by adding solid sodium hydroxide to the molten mass. 158<br />

Alloys containing between 30% and 50% of active metal are most suitable for<br />

preparation of active metal catalysts.<br />

The activity of Raney nickel can be increased by means of activators, for<br />

which purpose noble metals in the form of their chlorides, chloro acids, or<br />

salts of chloro acids are added after decomposition of the alloy or during the<br />

washing process. 159<br />

To increase the activity, Paul 160 added chromium, molybdenum, or cobalt<br />

in amounts of 3-10% (calculated on the amount of nickel) during preparation<br />

of the alloy. Hydrogenation in the presence of alkali or of organic bases is<br />

stated to effect a still further increase in activity.<br />

The efficiency of a Raney nickel catalyst for hydrogenation of carbonyl<br />

groups is much diminished if the catalyst is treated with 0.1% acetic acid or<br />

an amino acid, particularly dibasic amino acids or L-phenylalanine; but the<br />

efficiency for hydrogenation of C=C double bonds remains unaffected. Thus<br />

mesityl oxide was hydrogenated to isobutyl methyl ketone selectively and in<br />

good yield; but cinnamaldehyde could not be reduced in this way. 161 For<br />

asymmetric hydrogenation with Raney nickel modified by optically active<br />

2-hydroxy carboxylic acids see Tatsumi et al. 162<br />

Raney cobalt, 163 iron, 164 and copper catalysts 164 can be prepared in precisely<br />

analogous manner. They are, however, not so versatile in their application<br />

as Raney nickel.<br />

157 J. Aubry, Bull. Soc. Chim. France, [v], 5, 1333 (1938).<br />

158 Brit. Pat. 282,112 (1927) (I. G. Farbenindustrie); Chem. Abstr., 22, 3625 (1928).<br />

159 M.Delepine and A. Horeau, Bull. Soc. Chim. France, [v], 4, 31 (1937); E. Lieber,<br />

J. Amer. Chem. Soc, 72, 1190 (1950).<br />

160 R. Paul, Bull Soc. Chim. France, [v], 13, 208 (1946); see also J. Ishikawa, /. Chem.<br />

Soc. Japan, Pure Chem. Sect. [Nippon Kagaku Zasshi], 81, 1179 (1960) (cited from Chem.<br />

Zentralbl, 1963, 19,566).<br />

161 H. Fukawa, Y. Izumi, S. Komatsu, and S. Akabori, Bull. Chem. Soc. Japan, 35,<br />

1703 (1962) (cited from Chem. Zentralbl, 1964, 16-0821).<br />

162 S. Tatsumi, M. Imaida, Y. Fukuda, Y. Izumi, and S. Akabori, Bull Chem. Soc. Japan,<br />

37, 846 (1964) (cited from Chem. Zentralbl, 1966, 19-0820).<br />

163 U.S. Pat. 2,166,183 (1938); Chem. Abstr., 33, 8219 (1939); see also Brit. Pat. 628,407<br />

(1949); Chem. Abstr., 44, 2675e (1950).<br />

164 L. Faucounau, Bull. Soc. Chim. France, [v], 4, 58 (1937).

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