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Heterogeneously Catalyzed Oxidation Reactions Using ... - CHEC

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CHAPTER 6<br />

Intensity (a.u.)<br />

Figure 6‐5: Comparison of fresh and used STA‐12(Co) catalyst. (a) SEM image of fresh catalyst; (b) SEM image<br />

of used catalyst; (c) XRD of fresh and used catalyst.<br />

6.3.3 Heterogeneous vs. homogeneous catalysis<br />

A key in MOF catalysis is to assess whether catalysis proceeds mainly homogeneously or<br />

heterogeneously [24, 45] since dissolvable impurities or MOF degradation might also account for any<br />

observed catalytic activities. Thus, the catalyst was removed by filtration after the induction phase<br />

(Figure 6‐6). As can be seen, the reaction proceeds after catalyst removal, but with a significantly<br />

lower reaction rate. AAS analysis of the reaction mixture indeed showed some Co leaching of 0.40<br />

ppm amounting to ca. 3 % of the employed Co. Subsequent dissipation of the MOF during reaction as<br />

a cause for the catalytic activity and the induction phase can, however, be excluded: addition of (E)‐<br />

stilbene to an oxygen‐pretreated mixture of the Co‐MOF and DMF (100 °C over 12 h) did not result in<br />

a higher reaction rate. In fact, the induction took even longer due to catalyst deactivation. Similar<br />

leaching was found (0.44 ppm). Overall this indicates that the main catalytic route is heterogeneous<br />

in nature though minor homogeneous contributions cannot be excluded. Homogeneously dissolved<br />

Co salts (cobalt(III) acetyl acetonate and cobalt(II) acetate) indeed showed considerable activity.<br />

<strong>Using</strong> the same amount of Co as in the heterogeneous experiments, both (E)‐ and (Z)‐stilbene were<br />

converted faster (Figure 6‐7) exhibiting no induction phase. The conversion of<br />

162<br />

500<br />

450<br />

400<br />

350<br />

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250<br />

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150<br />

100<br />

50<br />

0<br />

-50<br />

10 20 30 40 50<br />

2θ/°<br />

(c)<br />

used<br />

fresh

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