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Electronic Material Properties - und Geowissenschaften ...

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Diffusion and reaction in micro- and mesopores<br />

Christoph Schüth<br />

Diffusion in micro- and mesopores is in many cases limiting for mass transfer and<br />

reaction rates in porous natural or synthetic materials. Accessibility and reactivity of<br />

micro- and meso-pore domains should be a function of the pore sizes as well as pore<br />

polarities. In natural po-rous media both parameters can be assumed to show a<br />

distribution, depending on the type of the porous material. Moreover, educts and<br />

products of a reaction may show different po-larities resulting in a distribution of<br />

diffusivities with an impact on overall reaction rates.<br />

The objective of this work is the synthesis and characterization of well-defined porous<br />

mate-rials with different pore sizes and polarities containing catalytically active sites,<br />

and study their accessibility with various methods. The catalytic hydrodehalogenation of<br />

chlorinated hydrocarbons (trichloroethylene (TCE) and chlorobenzene) and the<br />

hydrogenation of ben-zene serve as model reactions resulting in different product<br />

distributions in terms of polarity and molecular size. The use of well-characterized<br />

model solids should allow to relate diffu-sion rates and reactivities of the different<br />

materials to pore sizes and pore polarities.<br />

In the first step, the synthesis and first characterization of metal complexes will be<br />

performed. The selection of the metal complexes is predefined by the model reactions<br />

as described earlier. Pincer complexes (M-1a-c,2a-c) which are accessible by various<br />

procedures will be synthesized. In general a number of organic and organometallic<br />

transformations have to be performed to generate complexes M-1a-c,2a-c. Their special<br />

features are the different donor atoms which coordinate to the metal, the functional<br />

groups at the donor atoms and very important for this project the hydrolysable group at<br />

the end of the spacer. These features allow to adjust the metal complexes for a special<br />

application in catalysis.<br />

(R'O) 3Si<br />

X<br />

[M]<br />

X<br />

M-1a-c, M-2a-c<br />

Scheme 1<br />

X = SR (1), NR 2 (2)<br />

R = Me (a), Ph (b), Cy (c)<br />

[M] = Rh, Pd, Ni, Ru complex fragments<br />

R' = Me, Et<br />

Spacer e.g. C 6-alkane or short PEG chain<br />

It is planned to perform the dehalogenation reactions with the SCS-Pd complexes (Pd-<br />

1). Catalysts of this type are highly stable in air and water and are known to cleave<br />

carbon-chlorine bonds. This will be important for field applications planned at a later<br />

date of this project. To fine tune the active center with respect to electron density and<br />

steric hindrance R will be varied from methyl (Pd-1a), phenyl (Pd-1b) to cyclo-hexyl (Pd-<br />

1a). All complexes will be screened for their catalytic activity in dehalogenation and<br />

hydrogenation reactions.<br />

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