Heterogeneously Catalyzed Oxidation Reactions Using ... - CHEC
Heterogeneously Catalyzed Oxidation Reactions Using ... - CHEC
Heterogeneously Catalyzed Oxidation Reactions Using ... - CHEC
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6.4 Discussion<br />
CHAPTER 6<br />
The presented STA‐12(Co) catalyst effectively catalyzed the epoxidation of olefins in DMF media as it<br />
combines a high dispersion of well‐defined metal sites with a high metal content. Thereby the<br />
absolute amount of catalyst necessary for a reasonable conversion could be decreased by two orders<br />
of magnitude compared to reports in the literature on zeolite catalysts [22]. The conversion of<br />
styrene occurred quickly but with only a very low selectivity around 20 % and accompanied by<br />
formation of unknown (presumably oligomeric) side products as suggested by the incomplete mass<br />
balance. This is likely a general side reaction for styrene in DMF at elevated temperatures. Various<br />
examples in the literature on aerobic epoxidations in DMF with Co‐based solid catalysts (e.g. [20, 52])<br />
report styrene oxide selectivities of higher than 60 % which are, however, calculated on the basis of<br />
benzaldehyde and styrene oxide being the only products. <strong>Using</strong> the same estimation matrix for this<br />
study would also result in selectivities well above 60 %. Additionally, styrene was distilled prior to use<br />
in this study so that stabilizers were removed. On the contrary, the MOF catalyst converted (E)‐<br />
stilbene with a high selectivity between 80‐90 %. Average turn‐over frequencies were higher in the<br />
present study being around 20 h ‐1 compared to maximal 8 h ‐1 in [22] under similar conditions<br />
calculated based on the overall Co amount. Alongside the epoxidation reaction large amounts of<br />
byproducts not directly attributable to the olefin were formed in over‐ and near‐stoichiometric<br />
amounts, i.e. N‐formyl‐N‐methylformamide (FMF) as a solvent oxidation product and presumably<br />
free peroxides, both hinting at the complexity of the reaction mechanism.<br />
A side‐by‐side comparison of the MOF catalyst with the homogeneous catalysts employed<br />
here is difficult due to the different ligand sphere. Better homogeneous analogues of the MOF would<br />
bear a N,N'‐piperazinebis(methylenephosphonate) ligand but due to the pronounced Co network in<br />
the MOF would still not allow for conclusions by analogy. Differences show, however, that many<br />
effects seen for the MOF cannot be generalized for other Co catalysts. A major difference is the<br />
induction phase found only with the MOF. One reason for the induction phase could be traced back<br />
to the gradual formation of benzaldehyde which was found to be connected to the MOF catalytic<br />
activity and served as an explanation for the unexpected promoting role of another substrate,<br />
styrene, on the conversion of the investigated stilbene isomers. Other reasons for the induction<br />
phase were also investigated; e.g it seems unlikely that pore diffusion had an effect. The micropores<br />
of the MOF (ca. 1 nm) are similar in size to the stilbene isomers (ca. 1 nm) and therefore diffusion<br />
should influence the induction and reaction rate – if epoxidation takes place in the pores. Since<br />
benzaldehyde will hardly influence stilbene diffusion and MOF‐pretreatment with stilbene under N2<br />
did not shorten the induction phase, the MOF is likely active via its outer surface only. The efficacy of<br />
the MOF catalyst is therefore still limited by diffusion issues causing the inaccessibility of the MOF<br />
micropores. Opre et al. [23] suggest that epoxidation might occur via a DMF‐derived peroxide which<br />
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