Hydrogenation cobalt-catalyzed

Rhodium- and cobalt-catalyzed hydrogenation of butadiene and 1-hexene [47, 48] and the Ru-catalyzed hydrogenation of aromatic compounds [49] and acrylonitrile-butadiene copolymers [50] have also been reported to be successful in ionic liquids. 

The flow-cell design was introduced by Stieg and Nieman [166] in 1978 for analytical uses of CL. Burguera and Townshend [167] used the CL emission produced by the oxidation of alkylamines by benzoyl peroxide to determine aliphatic secondary and tertiary amines in chloroform or acetone. They tested various coiled flow cells for monitoring the CL emission produced by the cobalt-catalyzed oxidation of luminol by hydrogen peroxide and the fluorescein-sensitized oxidation of sulfide by sodium hypochlorite [168], Rule and Seitz [169] reported one of the first applications of flow injection analysis (FTA) in the CL detection of peroxide with luminol in the presence of a copper ion catalyst. They... 

Interception of the reaction sequence at the alkylcobalt carbonyl stage before carbonyl insertion, and hydrogenation of this intermediate, produces an alkane. This undesired side reaction is only minor (1-3%) in cobalt-catalyzed hydroformylation of a nonfunctional olefin, but may become predominant with phenyl- or acyl-substituted olefins. Ethylbenzene has been obtained in >50% yield from styrene (37), and even more alkane was obtained from a-methylstyrene (35). 

The cobalt-catalyzed reaction was studied by isolation of the lactones formed by hydrogenation and lactonization at higher temperatures (73). The hydroformylation was conducted at 140°C and 300 atm, followed by hydrogenation and cyclization at 200°-240°C, Eq. (33). 

The first catalyst used in hydroformylation was cobalt. Under hydroformylation conditions at high pressure of carbon monoxide and hydrogen, a hydrido-cobalt-tetracarbonyl complex (HCo(CO)4) is formed from precursors like cobalt acetate (Fig. 4). This complex is commonly accepted as the catalytic active species in the cobalt-catalyzed hydroformylation entering the reaction cycle according to Heck and Breslow (1960) (Fig. 5) [20-23]. 

Raffinate-II typically consists of40 % 1-butene, 40 % 2-butene and 20 % butane isomers. [RhH(CO)(TPPTS)3] does not catalyze the hydroformylation of internal olefins, neither their isomerization to terminal alkenes. It follows, that in addition to the 20 % butane in the feed, the 2-butene content will not react either. Following separation of the aqueous catalyts phase and the organic phase of aldehydes, the latter is freed from dissolved 2-butene and butane with a counter flow of synthesis gas. The crude aldehyde mixture is fractionated to yield n-valeraldehyde (95 %) and isovaleraldehyde (5 %) which are then oxidized to valeric add. Esters of n-valeric acid are used as lubricants. Unreacted butenes (mostly 2-butene) are hydroformylated and hydrogenated in a high pressure cobalt-catalyzed process to a mixture of isomeric amyl alcohols, while the remaining unreactive components (mostly butane) are used for power generation. Production of valeraldehydes was 12.000 t in 1995 [8] and was expected to increase later. 

Morken and co-workers have reported the highly enantioselective version of this reaction, albeit with low efficacy in the aldol-type coupling [8d, e]. Unfortunately, we obtain low enantioselectivity ee 2-4%) using chiral rhodium complexes under our reaction conditions. An intramolecular adaptation has led to new opportunities in cobalt-catalyzed carbocyclizations, wherein the use of PhSiHs was essential for smooth ring formation (Eq. 4) [9]. The identical products were also formed by a combination of [Rh(COD)2]OTf/(p-CE3Ph)3P and molecular hydrogen [10]. 

Hydrogenation of acetic anhydride to acetaldehyde (equation 23) has been demonstrated utilizing cobalt carbonyl under one atmosphere of hydrogen. However, the cobalt complex is short lived. A more efficient cobalt catalyzed reaction with substantial catalyst longevity was realized at a temperature of 190 and 3000 psi pressure CO and hydrogen. The main products were equal amounts of EDA and acetic acid. Upon investigation, this reaction was found exceptionally efficient at a more reasonable 1500 psi pressure provided that the temperature was maintained... 

Commercial development of a range of cycloalkene-cobalt homogeneous catalysts has prompted their application in the synthesis of pyridine and 2-substituted pyridines. Thus, bis(cyclopentadienyl)cobalt catalyzes the reaction of acetylene with hydrogen cyanide, acetonitrile or acrylonitrile to yield pyridine, 2-methylpyridine and 2-vinylpyridine respectively (Scheme 4 R = H, Me or CH=CH2) (76S26, 78AG(E)505, 75BEP846350). The high cost of the catalyst has so far limited full commercial realization of this route. Acrylonitrile... 

An initial report by Rathke and Feder of Argonne National Laboratory on cobalt-catalyzed hydrogenation of CO (35) has been followed by extensive study of this chemistry by the same workers (36-38). Reaction conditions adopted for these investigations (pressures below 375 atm and temperatures below 230°C) are much less severe than those employed in the earlier work... 

Fig. 1. Produci distribution as a function of reaction time in cobalt-catalyzed CO hydrogenation. (Reprinted from Ref. 38, by courtesy of Marcel Dekker, Inc.) Reaction conditions 26.5 atm H2, 340 atm CO, 182 C, 1,4-dioxane solvent. Y = J 0[HCo(CO)4]dt cobalt concentration changes throughout reaction because of sampling. Average HCo(CO)4 concentration is 0.051 M.

Rales to Primary Products in Cobalt-Catalyzed CO Hydrogenation at I82°C ... 

Product Selectivity and Rate as a Function of Pressure for Cobalt-Catalyzed CO Hydrogenation° b... 

Rates oj Cobalt-Catalyzed CO Hydrogenation in Different Solvents at 200°Ca... 

Product Distribution in Cobalt-Catalyzed CO Hydrogenation in Various Solvents b... 

The kinetics of hydroformylation by phosphine- or phosphite-modified complexes is even more complex than that of the cobalt-catalyzed reaction. Depending on the reaction conditions, either alkene complexation (Scheme 7.1, 6 to 7) or oxidative addition of hydrogen (Scheme 7.1, 9 to 10) may be rate-determining. 

Addition of modifying ligands such as tributyl phosphine affords a one-step, cobalt-catalyzed synthesis of alcohols (at lower pressure), but accompanying olefin hydrogenation reduces yields (3). With amine ligands, the effects are varied. Accelerated hydroformylation rates are possible with weak bases such as pyridine, but stronger bases (piperidine or triethylamine, for example) retard or completely inhibit the reaction (4,5). 

Godard, C., S. B. Duckett, S. Polas, R. Tooze, and A.C. Whitwood. 2005. Detection of intermediates in cobalt-catalyzed hydroformylation using para-hydrogen-induced polarization. J. Am. Chem. Soc. 127 4994-4995. 

Such a scheme by itself is insufficient to explain the accelerating effect of hydrogen bromide on cobalt-catalyzed autoxidations since optimum rates are achieved only in the presence of both hydrogen bromide and cobalt. One of the functions of the Co(II) is to maintain the concentration of hydrogen bro-... 

One of the mechanistic steps most often encountered and inferred from kinetic data is ligand dissociation, which leads to the generation of a catalytically active intermediate. If ligand is added to such a catalytic system, the rate of the reaction decreases. Examples of this in homogeneous catalytic reactions are many CO dissociation in cobalt-catalyzed hydroformylation, phosphine dissociation in RhCl(PPh3)3-catalyzed hydrogenation, Cl dissociation in the Wacker process, etc. The actual rate expressions of most of these processes are described in subsequent chapters. 

Hydroformylation of linear olefins in a conventional cobalt oxo process (see Section 5.3) produces increasing linear-to-branched aldehyde ratios as the carbon monoxide ratio in the gas stream is increased up to 5 MPa (50 atm), but there is little further effect if the reaction mixture is saturated with carbon monoxide. An increasing partial pressure of hydrogen also increases this ratio up to a hydrogen pressure of 10 MPa. As the reaction temperature is increased, the linear-to-branched aldehyde ratios decreases. Solvents in conventional cobalt-catalyzed hydroformylation affect the isomer distribution. In propylene... 

In the Shell process (SHOP) phosphine-modified cobalt-catalyzed hydrofor-mylation is one of the steps in the synthesis of linear alcohols with 12-15 carbon atoms (see Section 7.4.1). Two important characteristics of this reaction should be noted. First, the phosphine-modified precatalyst HCo(CO)3(PBu3) is less active for hydroformylation than HCo(CO)4 but more active for the subsequent hydrogenation of the aldehyde. In this catalytic system both hydroformylation and hydrogenation of the aldehyde are catalyzed by the same catalytic species. Second, the phosphorus ligand-substituted derivatives are more stable than their carbonyl analogues at higher temperatures and lower pressures (see Table 5.1). 

As early as 1938, Roelen discovered the cobalt-catalyzed hydroformylation of olefins, then known as the oxo reaction, which allowed the synthesis of aldehydes by addition of carbon monoxide and hydrogen to alkenes. Not long after this discovery it was found that cobalt, rhodium, ruthenium and platinum are also suitable as catalysts. However, because of the considerable price advantage for large scale applications in industry, cobalt catalysts are mostly used. Rhodium complexes, however, are... 

The cobalt-catalyzed reaction of olefins with CO and hydrogen to give aldehydes (Equation 2) was discovered by Roelen at Ruhrchemie in 1938, and is now known as hydroformylation (or, sometimes, as the 0x0 synthesis, Section 4.6) and is the basis of another major industrial process. 

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