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Rhodium, aromatic hydrogenation catalyst

Advances continue to be made in the synthesis and use of polymer-supported homogeneous catalysts. A rhodium(i) hydrogenation catalyst, prepared as outlined in Scheme 1, is much more versatile than most homogeneous rhodium catalysts. This catalyst will not only reduce a variety of olefinic and aromatic hydrocarbons under mild conditions but also carbonyl, nitrile, and nitro-groups. The catalyst is air stable, but its lifetime appears to be less than those of other polymer-supported catalysts. [Pg.197]

Aldehydes, both aliphatic and aromatic, can be decarbonylated by heating with chlorotris(triphenylphosphine)rhodium or other catalysts such as palladium. The compound RhCl(Ph3P)3 is often called Wilkinson s catalyst.In an older reaction, aliphatic (but not aromatic) aldehydes are decarbonylated by heating with di-tert-peroxide or other peroxides, usually in a solution containing a hydrogen donor, such as a thiol. The reaction has also been initiated with light, and thermally (without an initiator) by heating at 500°C. [Pg.944]

Rhodium(II) acetate catalyzes C—H insertion, olefin addition, heteroatom-H insertion, and ylide formation of a-diazocarbonyls via a rhodium carbenoid species (144—147). Intramolecular cyclopentane formation via C—H insertion occurs with retention of stereochemistry (143). Chiral rhodium (TT) carboxamides catalyze enantioselective cyclopropanation and intramolecular C—N insertions of CC-diazoketones (148). Other reactions catalyzed by rhodium complexes include double-bond migration (140), hydrogenation of aromatic aldehydes and ketones to hydrocarbons (150), homologation of esters (151), carbonylation of formaldehyde (152) and amines (140), reductive carbonylation of dimethyl ether or methyl acetate to 1,1-diacetoxy ethane (153), decarbonylation of aldehydes (140), water gas shift reaction (69,154), C—C skeletal rearrangements (132,140), oxidation of olefins to ketones (155) and aldehydes (156), and oxidation of substituted anthracenes to anthraquinones (157). Rhodium-catalyzed hydrosilation of olefins, alkynes, carbonyls, alcohols, and imines is facile and may also be accomplished enantioselectively (140). Rhodium complexes are moderately active alkene and alkyne polymerization catalysts (140). In some cases polymer-supported versions of homogeneous rhodium catalysts have improved activity, compared to their homogenous counterparts. This is the case for the conversion of alkenes direcdy to alcohols under oxo conditions by rhodium—amine polymer catalysts... [Pg.181]

The direct reduction of gallic acid described here illustrates the virtue of the rhodium-on-alumina catalyst to achieve the perhydrogenation of polyhydroxylated aromatic compounds with minimal attendant hydrogenolysis. A closely related hydrogenation, that of pyrogallol, to yield a dihydro intermediate, and also the direct reduction of pyrogallol with palladium-on-stron-tium carbonate to afford the all ci5-pyrogallitol (1,2,3-cyclohex-anetriol) have been reported. ... [Pg.66]

Raney nickel and platinum, palladium, and rhodium catalysts have been used to accomplish the hydrogenation of polycyclic aromatics. Hydrogenation of fused polycyclic arenes leads to the cis- or fran -substituted cyclohexane derivatives. The cis product is usually obtained again this can be understood in terms of the mechanism proposed for aromatic hydrogenation (vide supra). [Pg.409]

T. Harada, S. Ikeda, Y. Hau Ng, T. Sakata, H. Mori, T. Torimoto, M. Matsumura, Rhodium nanoparticle encapsulated in a porous carbon sheU as an active heterogeneous catalyst for aromatic hydrogenation, Adv. Funct. Mater. 18 (2008) 2190-2196. [Pg.408]

Cost. The catalytically active component(s) in many supported catalysts are expensive metals. By using a catalyst in which the active component is but a very small fraction of the weight of the total catalyst, lower costs can be achieved. As an example, hydrogenation of an aromatic nucleus requires the use of rhenium, rhodium, or mthenium. This can be accomplished with as fittie as 0.5 wt % of the metal finely dispersed on alumina or activated carbon. Furthermore, it is almost always easier to recover the metal from a spent supported catalyst bed than to attempt to separate a finely divided metal from a liquid product stream. If recovery is efficient, the actual cost of the catalyst is the time value of the cost of the metal less processing expenses, assuming a nondeclining market value for the metal. Precious metals used in catalytic processes are often leased. [Pg.193]

Ruthenium is excellent for hydrogenation of aliphatic carbonyl compounds (92), and it, as well as nickel, is used industrially for conversion of glucose to sorbitol (14,15,29,75,100). Nickel usually requires vigorous conditions unless large amounts of catalyst are used (11,20,27,37,60), or the catalyst is very active, such as W-6 Raney nickel (6). Copper chromite is always used at elevated temperatures and pressures and may be useful if aromatic-ring saturation is to be avoided. Rhodium has given excellent results under mild conditions when other catalysts have failed (4,5,66). It is useful in reduction of aliphatic carbonyls in molecules susceptible to hydrogenolysis. [Pg.67]

The above generalities apply particularly to palladium. Hydrogenation over platinum or rhodium are far less sensitive to the influence of steric crowding. Reduction of 1-t-butylnaphthalene over platinum, rhodium, and palladium resulted in values of /ci//c2 of 0.42, 0.71, and 0.024, respectively. Also, unlike mononuclear aromatics, palladium reduces substituted naphthalenes at substantially higher rates than does either platinum or rhodium. For example, the rate constants, k x 10 in mol sec" g catalyst", in acetic acid at 50 C and 1 atm, were (for 1,8-diisopropylnaphthalene) Pd (142), Pt(l8.4), and Rh(7.1)(25). [Pg.120]

To hydrogenate an aromatic ring, it s necessary either to use a platinum catalyst with hydrogen gas at several hundred atmospheres pressure or to use a more effective catalyst such as rhodium on carbon. Under these conditions, aromatic rings are converted into cyclohexanes. For example, o-xylene yields 1,2-dimethylcvclohexane, and 4-terf-butylphenol gives 4-terf-butyl-cyclohexanol. [Pg.579]

The benzylic position of an alkylbcnzene can be brominated by reaction with jV-bromosuccinimide, and the entire side chain can be degraded to a carboxyl group by oxidation with aqueous KMnCfy Although aromatic rings are less reactive than isolated alkene double bonds, they can be reduced to cyclohexanes by hydrogenation over a platinum or rhodium catalyst. In addition, aryl alkyl ketones are reduced to alkylbenzenes by hydrogenation over a platinum catalyst. [Pg.587]


See other pages where Rhodium, aromatic hydrogenation catalyst is mentioned: [Pg.1314]    [Pg.1314]    [Pg.181]    [Pg.200]    [Pg.151]    [Pg.1564]    [Pg.211]    [Pg.441]    [Pg.73]    [Pg.206]    [Pg.1234]    [Pg.620]    [Pg.633]    [Pg.134]    [Pg.271]    [Pg.282]    [Pg.29]    [Pg.61]    [Pg.335]    [Pg.461]    [Pg.215]    [Pg.460]    [Pg.116]    [Pg.34]    [Pg.727]    [Pg.733]    [Pg.735]    [Pg.192]    [Pg.4]    [Pg.345]    [Pg.321]    [Pg.200]    [Pg.200]    [Pg.15]    [Pg.97]    [Pg.119]    [Pg.1003]   
See also in sourсe #XX -- [ Pg.579 ]

See also in sourсe #XX -- [ Pg.579 ]

See also in sourсe #XX -- [ Pg.599 ]




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Aromatic hydrogen

Aromatic hydrogenation

Aromatic hydrogenation catalysts

Aromatics hydrogenation

Catalysts aromatization

Hydrogen aromaticity

Hydrogenated aromatics

Rhodium aromatics

Rhodium catalysts catalyst

Rhodium catalysts hydrogen

Rhodium hydrogenation catalyst

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