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Nickel catalysts, for hydrogenation

Neopentyl alcohol, 40, 76 Nickel catalyst for hydrogenation of resorcinol, 41, 56, 57 Nitramines from amines and acetone cyanohydrin nitrate, 43, 84 Nitration, of amines to nitramines by acetone cyanohydrin nitrate, 43, 83... [Pg.118]

Table 5.2 Effect of Promoters on the Activity of Skeletal Nickel Catalysts for Hydrogenation of Different Functional Groups... Table 5.2 Effect of Promoters on the Activity of Skeletal Nickel Catalysts for Hydrogenation of Different Functional Groups...
Riesz and Weber compared the selectivities of commercial platinum, palladium, rhodium, and nickel catalysts for hydrogenation of linolenic components in soybean oil.110 Representative results are summarized in Table 3.8. Certain platinum metal catalysts showed higher selectivities than nickel catalysts, as indicated by the values of SL (A in Scheme 3.13) = 2.4-2.7. Generally, nickel catalysts showed selectivities... [Pg.89]

NyseL [M THaishaw] Nickel catalyst for hydrogenation of oils. [Pg.260]

The efficiency of a Raney nickel catalyst for hydrogenation of carbonyl groups is much diminished if the catalyst is treated with 0.1% acetic acid or an amino acid, particularly dibasic amino acids or L-phenylalanine but the efficiency for hydrogenation of C=C double bonds remains unaffected. Thus mesityl oxide was hydrogenated to isobutyl methyl ketone selectively and in good yield but cinnamaldehyde could not be reduced in this way.161 For asymmetric hydrogenation with Raney nickel modified by optically active 2-hydroxy carboxylic acids see Tatsumi et al.162... [Pg.23]

Kenjo T. Chromium-doped Raney nickel catalyst for hydrogen electrodes in alkatine fuel cells. J Electrochem Soc 1985 132(2) 383-6. [Pg.164]

Zirconium tetrafluoride [7783-64-4] is used in some fluoride-based glasses. These glasses are the first chemically and mechanically stable bulk glasses to have continuous high transparency from the near uv to the mid-k (0.3—6 -lm) (117—118). Zirconium oxide and tetrachloride have use as catalysts (119), and zirconium sulfate is used in preparing a nickel catalyst for the hydrogenation of vegetable oil. Zirconium 2-ethyIhexanoate [22464-99-9] is used with cobalt driers to replace lead compounds as driers in oil-based and alkyd paints (see Driers and metallic soaps). [Pg.433]

Pure piperitone was subjected to the action of purified hydrogen, in the presence of a nickel catalyst, for six hours, the temperature ranging between 175° to 180° C. The double bond in piperitone was readily opened out with the formation of menthone, but further action of the hydrogen under these conditions did not reduce the carbonyl group, even after continued treatment for two days. Under correct conditions, however, the reduction to menthol should take place. The ease with which menthone is formed in this way is of special interest, not only in connection with the production of this ketone, but also as a stage in the manufacture of menthol. [Pg.240]

A variety of catalysts including copper, nickel, cobalt, and the platinum metals group have been used successfully in carbonyl reduction. Palladium, an excellent catalyst for hydrogenation of aromatic carbonyls is relatively ineffective for aliphatic carbonyls this latter group has a low strength of adsorption on palladium relative to other metals (72,91). Nonetheless, palladium can be used very well with aliphatic carbonyls with sufficient patience, as illustrated by the difficult-to-reduce vinylogous amide I to 2 (9). [Pg.66]

Raney nickel is a useful catalyst for hydrogenations at mild conditions. It is, however, sensitive to poisoning and not very stable at high temperatures. Another disadvantage is that regeneration is not always possible in many cases the catalyst must be melted with aluminium until the right Al-Ni alloy is formed. Then the preparation procedure has to be repeated again. Moreover, the preparation procedure is not very reproducible. [Pg.70]

The most commonly used catalysts for hydrogenation (finely divided platinum, nickel, palladium, rhodium, and ruthenium) apparently serve to adsorb hydrogen molecules on their surface. [Pg.307]

Campbell, C. T., and Goodman, D. W. 1982. A surface science investigation of the role of potassium promoters in nickel catalysts for carbon monoxide hydrogenation. Surf. Sci. 123 413-26. [Pg.80]

The Treatment of Activated Nickel Catalysts for the Selective Hydrogenation... [Pg.536]

Similarly, we can ask what would be the best catalyst for hydrogenating an olefin such as ethylene. Since olefins (alkenes) are more strongly chemisorbed than hydrogen, we choose a metal that just barely chemisorbs H2—this means Co, Rh, Ir, Ni, Pd, or Pt. In practice, nickel is the least expensive choice. Again, it should be finely divided (maximum surface area) for greatest catalytic efficiency and be dispersed on the internal surfaces of a porous support such as alumina with surface area on the order of 200 m2 g 1.8... [Pg.120]

Specific activities of silica-supported nickel catalysts for benzene hydrogenation (ftH) and exchange (ftE) at 298 K [39,282]... [Pg.105]

It is clear that the influence of surface geometry upon catalytic activity is extremely complex and many more studies are required before any definitive relationship between catalytic activity and metal particle size can be established. Such studies will require to take cognisance of such factors as the perturbation of surface structure due to the formation of carbidic residues, as noted by Boudart [289] and by Thomson and Webb [95], and by the modification of catalytic properties on adsorption, as noted by Izumi et al. [296—298] and by Groenewegen and Sachtler [299] in studies of the modification of nickel catalysts for enantioselective hydrogenation. Possible effects of the support, as will be discussed in Sect. 6.3, must also be taken into account. [Pg.106]

There is evidence of a promoting action of chromium on nickel catalysts for the reaction of hydrogenation of valeronitrile in our conditions. Introduction of chromium increased the initial specific activity and the selectivity. The promoting effect of chromium on activity could be correlated to the increase of the metallic surface. Another explanation could be that the Cr+ segregated at the surface of the catalyst may play the role of a Lewis acid center and may be responsible for a better chemisorption of valeronitrile on the catalysts, through nitrogen lone pair electrons or the n orbital of the CN bond. However, further examination of the results obtained (see Fig. 3)... [Pg.119]

Alkenes can also be produced effectively by die reduction of alkynes. The reduction can be carried out stereospecifically to give either cis or trails olefins as desired. This is a very useful method because of the stereocontrol. The P-2 nickel catalyst for the cis hydrogenation is produced in situ by the reduction... [Pg.206]

A mixture of 680 grams of 2-methyl-9-phenyl-2,3-dihydrol-pyridindene hydrobromide, 6,000 cc of water and about 100 grams of Raney-nickel catalyst is hydrogenated at room temperature and at about 1,000 lb pressure for a period of three hours. The catalyst is filtered. The clear filtrate is treated with a solution of 240 grams potassium thiocyanate in 400 cc of water. A heavy solid precipitates from which the supernatant liquid is decanted. [Pg.2705]


See other pages where Nickel catalysts, for hydrogenation is mentioned: [Pg.502]    [Pg.200]    [Pg.88]    [Pg.88]    [Pg.117]    [Pg.7]    [Pg.502]    [Pg.200]    [Pg.88]    [Pg.88]    [Pg.117]    [Pg.7]    [Pg.68]    [Pg.610]    [Pg.1204]    [Pg.407]    [Pg.47]    [Pg.130]    [Pg.110]    [Pg.94]    [Pg.102]    [Pg.43]    [Pg.734]    [Pg.348]    [Pg.928]    [Pg.228]   
See also in sourсe #XX -- [ Pg.1003 ]




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