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Leached palladium

Figure 22.1. Schematic representation of use of insoluble poisons to selectively terminate catalysis from leached palladium species in couphng reactions. Figure 22.1. Schematic representation of use of insoluble poisons to selectively terminate catalysis from leached palladium species in couphng reactions.
Heterogenization of homogeneous metal complex catalysts represents one way to improve the total turnover number for expensive or toxic catalysts. Two case studies in catalyst immobilization are presented here. Immobilization of Pd(II) SCS and PCP pincer complexes for use in Heck coupling reactions does not lead to stable, recyclable catalysts, as all catalysis is shown to be associated with leached palladium species. In contrast, when immobilizing Co(II) salen complexes for kinetic resolutions of epoxides, immobilization can lead to enhanced catalytic properties, including improved reaction rates while still obtaining excellent enantioselectivity and catalyst recyclability. [Pg.3]

In addition to the evidence found from our group, a critical review of the available palladium literature for carbon-carbon coupling reactions was undertaken to attempt to further discern the nature of immobilized palladium catalysts [48]. This review indicates that the available data are consistent with a Pd(0)-Pd(II) catalytic cycle, and that there is no compelling evidence for a Pd(II)-Pd(IV) cycle. We have found that an array of techniques are needed to fuUy discern the nature of the catalytic species in Heck-type chemistries, and that, in general, complete and permanent immobilization of palladium catalysts for these reactions may be extremely difficult due to the lack of activity of solid palladium surfaces and the active nature of even a small amount of leached palladium. [Pg.453]

The catalytic activity, however, is generally associated with leaching of the metal into solution, the reaction being most likely catalyzed by soluble active Pd species. Palladium leaching is generally caused by oxidative attack of the aryl halide on the metal nanoparticles, giving catalyt-ically active aryl halide Pd(II) species in solution [30]. [Pg.443]

This allows for easy reuse of the catalyst in the reaction of allylation of secondary amines like piperidine or morpholine for several runs. The leaching of palladium was less than 0.001% of the initial amount. [Pg.465]

The supported aqueous phase methodology was applied to the system Pd(OAc)2/5 TPPTS, a catalytic precursor for the Trost-Tsuji reaction. The characterization of the solid by 31P MAS NMR confirms the presence of Pd°(TPPTS)3 as the main surface species. The catalytic properties of the solid were tested for the allylic substitution of E-cinnamylethylcarbonate by different nucleophiles such as ethyl acetoacetate, dimethyl malonate, morpholine, phenol, and 2-mercapto-pyridine. The absence of palladium leaching was demonstrated, and having solved the problem of water leaching from the solid to the organic phase, the SAP-Pd catalyst was successfully recycled several times without loss in its activity. It was used in a continuous flow experiment which... [Pg.465]

Further investigations using model compounds showed that the formation of PdCl2 by a reaction with the solvent, as suggested by Brinkmann el al. [30], was also not responsible for the observed rapid deactivation. Palladium leaching after formation of Pd(0) was also excluded by experiments. The authors concluded therefore that the presence of allyl acetate facilitated the decomposition. [Pg.84]

Some of the most remarkable achievements include microencapsulation in polystyrenes such as entrapped 0s04 for olefin hydroxylation (exploiting the interaction between n-electrons of benzene rings of the polystyrenes used as polymer backbones and the vacant orbitals of the catalysts) 5 polyurea-entrapped palladium (PdEnCat)6 for a multiplicity of C C forming reactions and the use of carboxylic acid-functionalized polymer (FibreCat).7 In general, however, metal leaching cannot be avoided. The PdEnCat catalyst, for instance, leaches some 4% of palladium per catalytic reaction run. [Pg.114]

Another example is the palladium catalyzed allylic substitution of 3-phenyl-2-propenyl-carbonic acid methyl ester to yield iV-(3-phenyl-2-propenyl)morpho-line reported by Reetz, Kragl and co-workers. This reaction was performed in the presence of phosphino-terminated amine dendrimers [17, 18] loaded with Pd11 cations as shown in Scheme 10. For this particular dendrimer with a molecular weight of 10 212 g/mol, a retention of 0.999 per residence time [35] was estimated in a membrane reactor with a SELRO MPF-50 membrane. It must be noted that a very high retention is a prerequisite for a continuous operating system, since a small leaching of the dendrimer leads to an exponential decrease in the amount... [Pg.508]

Bidentate chiral water-soluble ligands such as (S,S)-2,4-bis(diphenyl-sulfonatophosphino)butane BDPPTS (Fig. 2) or (R,R) 1,2-bis(diphenylsul-fonatophosphinomethyl)cyclobutane have been prepared [25]. Their palladium complexes catalyze the synthesis of chiral acids from various viny-larenes and an ee of 43% has been reached for p-methoxystyrene with the BDPPTS ligand. Furthermore, recycling of the aqueous phase has shown that the regio- and enantioselectivity are maintained and that no palladium leaches. [Pg.108]

The widespread use of platinum, palladium and other metals in automotive catalytic converters has been driven by environmental considerations and the increasing costs of the metals. This has not been matched by the development of clean reprocessing technologies for the catalysts themselves. The spent catalyst metals are oxidized to their cations via leaching into concentrated acids. [Pg.215]

Catalysis experiments were performed to investigate the telomerization of butadiene with ethylene glycol in selected TMS systems (e.g. si toluene DMF 1 5 4 or sl 2-octanol DMSO 1.35 3 5.2). With Pd/TPPTS as the catalyst a maximum yield of only 10% of the desired products could be achieved. With Pd/TPPMS the yield increased up to 43% in the TMS system si toluene isopropyl alcohol, but additional water had to be added to obtain a phase split after the reaction. The catalyst leaching is very high and 29% of the palladium used is lost to the product phase. [Pg.27]


See other pages where Leached palladium is mentioned: [Pg.195]    [Pg.197]    [Pg.103]    [Pg.332]    [Pg.335]    [Pg.218]    [Pg.201]    [Pg.195]    [Pg.197]    [Pg.103]    [Pg.332]    [Pg.335]    [Pg.218]    [Pg.201]    [Pg.160]    [Pg.629]    [Pg.218]    [Pg.221]    [Pg.227]    [Pg.227]    [Pg.228]    [Pg.229]    [Pg.444]    [Pg.193]    [Pg.193]    [Pg.195]    [Pg.197]    [Pg.197]    [Pg.197]    [Pg.200]    [Pg.104]    [Pg.188]    [Pg.14]    [Pg.464]    [Pg.379]    [Pg.83]    [Pg.161]    [Pg.162]    [Pg.164]    [Pg.165]    [Pg.484]    [Pg.509]    [Pg.143]    [Pg.148]    [Pg.216]   
See also in sourсe #XX -- [ Pg.452 , Pg.453 ]




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Palladium leaching

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