School of Engineering and Science - Jacobs University
School of Engineering and Science - Jacobs University
School of Engineering and Science - Jacobs University
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PVP stabilizer. In the work <strong>of</strong> Bönnemann [114, 115] , no such dependence was found<br />
(ee = 76% over 1.5 nm Pt cluster <strong>and</strong> 78 % over 3.9 nm, under 1 bar <strong>of</strong> H 2 pressure).<br />
In our opinion, one <strong>of</strong> the primary effects causing enhanced ee is a higher concentration<br />
<strong>of</strong> active chiral sites (“π-bonded” cinchonidine) on the catalyst surface. In the work <strong>of</strong><br />
Yang <strong>and</strong> co-authors cinchonidine adsorbs on the Pt surface from solution (optimum<br />
concentration <strong>of</strong> cinchonidine [80, 102, 180]) whereas high hydrogen pressure (40 bar)<br />
promotes a surface cleaning (from PVP, AcOH <strong>and</strong> etc.) for obtaining more space for<br />
flat adsorbed cinchonidine ( cinchonidine in any tilted mode needs, definitely, less free<br />
space for the adsorption). The catalyst prepared according to Bönnemann’s procedure<br />
(sample B) possesses adsorbed cinchonidine in flat <strong>and</strong> in two tilted modes as<br />
demonstrated in this manuscript <strong>and</strong> a high pressure <strong>of</strong> hydrogen was not applied.<br />
Moreover ee=94-95 % was obtained under high (100 bar) H 2 pressure with<br />
conventional 5R94 [180] <strong>and</strong> Engelhard 4759 [181]- Pt/Al 2 O 3 catalysts (average<br />
particles size 3.6 nm [182]) where the above mentioned size effect seems to be less<br />
probable.<br />
Based on these facts, we would like to conclude here, that it was found that the size <strong>of</strong><br />
Pt clusters (in range 1.4- ∞ nm) has no observed influence on the adsorption mode <strong>of</strong><br />
the cinchonidine (at least in case <strong>of</strong> sample B (1.4 nm), sample D (2.3 nm),<br />
conventional Pt/Al 2 O 3 (4 nm) <strong>and</strong> macroscopic samples from work <strong>of</strong> Zaera [77] <strong>and</strong><br />
Ferri [76]). This is important because it has been reported in the literature that cluster<br />
size does influence both catalytic activity <strong>and</strong> the observed ee [106].<br />
Thus, it was found that both ‘flat’ <strong>and</strong> ‘tilted’ modes <strong>of</strong> adsorbed cinchonidine are<br />
present on Pt nanoclusters <strong>and</strong> could be an explanation <strong>of</strong> the fact that this type <strong>of</strong><br />
catalyst does not provide the maximum possible enantiomeric excess (99 %).<br />
4.3.3 Investigation <strong>of</strong> catalytic behaviour <strong>of</strong> cinchonidine<br />
modified Pt nanoclusters<br />
Investigation <strong>of</strong> catalytic behavior <strong>of</strong> cinchonidine modified Pt nanoclusters was<br />
studied with B, D <strong>and</strong> conventional modified Pt/Al 2 O 3 in the hydrogenation <strong>of</strong> ethyl<br />
pyruvate.<br />
Initial transient period<br />
Under all reaction conditions, summarized in Table 4-4, enantiomeric excess was found<br />
to depend on the reaction time in a manner similar to that shown in the Fig. 4-13.<br />
During the first moments <strong>of</strong> hydrogenation (the period <strong>of</strong> time termed the initial<br />
transient period) enantiomeric excess increases to a maximum value (ee max ) <strong>and</strong> then<br />
decreases until the entire amount <strong>of</strong> ethyl pyruvate is converted in the reaction mixture.<br />
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