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Wacker’s oxidation

In Leighton s total synthesis of dolabelide D, the Wacker-Tsuji oxidation diene 70 was achieved chemoselectively to produce methyl ketone 71.54 55 Furthermore, addition of (-)-sparteine as a ligand prevented olefin isomerization and led to selective formation of methyl ketone 71 from the terminal olefin in good yield.56... [Pg.320]

Wacker-type oxidation. S fected with H2O2 in the presence 1 Epoxidation. (Salen)Mn con dation." Usually an imidazole is ai these oxidations. " A great variet in this process, including oxygen organoiodine compounds. [Pg.184]

The single-stage process was developed by a research group of Hoechst AG (also see [36]). At the time, Hoechst AG owned 50% of the shares of Wacker Chemie. Via the board, they learned at an early time about Wacker s activity on ethylene oxidation and began research on this field. Later on, both companies cooperated and combined their results. [Pg.148]

The two-stage process has been developed by the research group of Wacker s Consortium fiir elektrochemische Industrie. While this group worked on the development of a single-stage process, Wacker had to realize that at the time and the site of the scheduled first commercial plant, oxygen was not available at a reasonable price. So, Wacker was forced to develop another version using air as the oxidant. [Pg.149]

Even with our modified definition of indifferent , we still require that the catalytic material should act indefinitely once introduced. This requirement is also fulfilled by a number of essential materials added to some catalytic processes, and often referred to as co-catalysts or promoters. For example, the copper (I)-copper (II) chloride redox system used in Wacker s palladium-catalysed oxidation of ethylene to acetaldehyde (section 11.7.7.3) behaves in a true catalytic manner in the single-reactor variant of the process (ethylene and O2 introduced into the same reaction vessel). [Pg.310]

It is most conveniently obtained by the Wacker-chemie s oxidation process. In this process ethylene is oxidised with oxygen in presence of the catalyst solution (Scheme 18). [Pg.248]

In 1979, Tsuji s group [51] reported an alternative approach to macrolactonization. Inspired by their previous success in the preparation of recifeiolide and 9-decanolide, the authors envisioned that the dimethyl ether of zearalenone (6) could be obtained via olefination using the co-iodoalkyl phenylthioacetate 7 (Scheme 7.2). The Michael addition of diethyl malonate (11) to 10 followed by decarboxylation afforded an ethyl ester, which was reduced to alcohol and converted into the tosylate 12. Wacker-Tsuji oxidation of the terminal olefin was then followed by reduction of the ketone and conversion of the tosylate into iodide to provide 9. This was... [Pg.279]

Another s)mthesis of muscone (compare Section 1.1) also starts with the nonadienoate (Equation 23). Wacker/Hoechst-oxidation of the terminal double bond and hydrogenation of the internal one yields a ketocarboxylic acid, which reacts in a Kolbe electrolysis to 2,15-hexadecanedione, the precursor of muscone [28]. [Pg.149]

As discussed above, on the basis of process considerations, the preferred mode of carrying out the hydroxylation of methane would be to utilize a Wacker type system using an air-recyclable oxidant. CH activation-based systems are quite amenable to such process considerations and both the Hg(II) and (bpym)Pt(II)/H2S04 are examples of such systems, where S(VI)/S(IV) redox cycle plays the role of the Wacker-type oxidant. A generalized scheme of this type of system is shown in Fig. 7.34 which emphasizes the possibility of avoiding the generation of free-radicals in the methane oxidation reactor by the use of singlef air-recyclable oxidants. Ox. [Pg.270]

METHOD 2 Without a doubt, this is the current world favorite for making P2Ps. This method is known as the Wacker oxidation and involves mixing safrole (or any other allylbenzene), palladium chloride, cuprous chloride and dimethylformamide in an oxygen atmosphere to get MD-P2P very quickly and in a totally clean manner [11, 12]. There s also a very nice review in ref. 13. [Pg.60]

Strike got the journal article for this recipe as literature citation used in the original Wacker oxidation Strike used for Method 2. In it both mercuric acetate, and to an extent, lead acetate produced ketones as described. Someone-Who-ls-Not-Strike also got a certain ketone. But maybe they were lucky or just plain wrong. Most people on Strike s site say this mercuric acetate thing... [Pg.89]

Acetaldehyde, first used extensively during World War I as a starting material for making acetone [67-64-1] from acetic acid [64-19-7] is currendy an important intermediate in the production of acetic acid, acetic anhydride [108-24-7] ethyl acetate [141-78-6] peracetic acid [79-21 -0] pentaerythritol [115-77-5] chloral [302-17-0], glyoxal [107-22-2], aLkylamines, and pyridines. Commercial processes for acetaldehyde production include the oxidation or dehydrogenation of ethanol, the addition of water to acetylene, the partial oxidation of hydrocarbons, and the direct oxidation of ethylene [74-85-1]. In 1989, it was estimated that 28 companies having more than 98% of the wodd s 2.5 megaton per year plant capacity used the Wacker-Hoechst processes for the direct oxidation of ethylene. [Pg.48]

Oxidative addition consumes one equivalent of expensive Pd(OAc)2 in most cases. However, progress has been made towards the catalytic oxidative addition pathway. Knolker s group described one of the first oxidative cyclizations using catalytic Pd(OAc)2 in the synthesis of indoles [19]. They reoxidized Pd(0) to Pd(II) with cupric acetate similar to the Wacker reaction, making the reaction catalytic with respect to palladium [20]. [Pg.3]

The phenolic oxygen on 2-allyl-4-bromophenol (7) readily underwent oxypalladation using a catalytic amount of PdCl2 and three equivalents of Cu(OAc)2, to give the corresponding benzofuran 8. This process, akin to the Wacker oxidation, was catalytic in terms of palladium, and Cu(OAc)2 served as oxidant [17]. Benzofuran 10, a key intermediate in Kishi s total synthesis of aklavinone [18], was synthesized via the oxidative cyclization of phenol 9 using stoichiometric amounts of a Pd(II) salt. [Pg.270]

The more expedient, direct catalytic oxidation route to acetone was developed in Germany in the 1960s. If you had been in charge of building the acetone business from scratch, you d probably not have built any IPA-to-acetone plants if you had known about the Wacker process. It s a catalytic oxidation of propylene at 200—250°F and 125—200 psi over palladium chloride with a cupric (copper) chloride promoter. The yields are 91-94%. The hardware for the Wacker process is probably less than for the combined IPA/acetone plants. But once the latter plants were built, the economies of the Wacker process were not sufficient to shut them down and start all over. So the new technology never took hold in the United States. [Pg.243]

In contrast to the usual Wacker-conditions, optimum rates and catalyst stability in the Pd/batophenanthroHne-catalyzed olefin oxidations was observed in the presence of NaOAc (pH s 11.5). Under such conditions, the catalyst-containing aqueous phase could be recycled with about 2-3 % loss of activity in each cycle. In the absence of NaOAc precipitation ofPd-black was observed after the second and third cycles. Nevertheless, kinetic data refer to the role of a hidroxo-bridged dimer (Scheme 8.1) rather than the so-called giant palladium clusters which could easily aggregate to metallic palladium. [Pg.212]

The impressive activity achieved by Teles catalyst was improved some years later by the use of CO as an additive [92]. In this study, Hayashi and Tanaka reported a TOF of 15600h 1, at least two orders of magnitude higher than [as-PtCl2(tppts)2], for the hydration of alkynes, providing an alternative synthetic route to the Wacker oxidation. Although several solvents were tested, the best results were obtained with aqueous methanol, and sulfuric acid or HTfO as acidic promoters. Unlike Utimoto s observation, in this case terminal propargylic alcohols partially (17-20%) delivered anti-Markovnikov product, in addition to the Markovnikov species. Some years before, Wakatsuki et al. had already reported the anti-Markovnikov hydration of terminal alkynes catalyzed by ruthenium(II) [93]. [Pg.450]

Wacker oxidation. Tsuji et al.s have developed two procedures for oxidation of 1-alkenes to methyl ketones with oxygen that are catalyzed by PdCl2 (7, 278 9, 327). The solvent in both cases is aqueous DMF. One method uses PdCl2-CuCl (molar ratio 1 10) the other uses PdCl2 and p-benzoquinone (molar ratio 1 100). Both procedures are about equivalent for oxidation of simple l-alkenes to methyl ketones, but the former method is usually more effective for oxidation of more complex 1-alkenes. [Pg.302]


See other pages where Wacker’s oxidation is mentioned: [Pg.59]    [Pg.40]    [Pg.59]    [Pg.40]    [Pg.271]    [Pg.100]    [Pg.309]    [Pg.120]    [Pg.715]    [Pg.235]    [Pg.108]    [Pg.1062]    [Pg.123]    [Pg.168]    [Pg.1538]    [Pg.61]    [Pg.681]    [Pg.1009]    [Pg.7]    [Pg.141]    [Pg.827]    [Pg.256]    [Pg.1197]   
See also in sourсe #XX -- [ Pg.40 ]

See also in sourсe #XX -- [ Pg.40 ]




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