Angewandte
Communications
Chemie
synthetic batch of PtSn@mSiO2, enhancement factors hexp
>
103 were observed, corresponding to f > 10%, setting a world
record for any heterogeneous NP catalyst. While our setup
did not permit these studies to be extended to higher pressure
and catalyst mass, the results clearly indicate that higher
conversions can likely be achieved. We hypothesize that the
slight differences in f and c between the two catalyst batches
are due to variations in uniformity of Pt and Sn surface atomic
distributions that exist despite the same 1:1 atomic ratio in
bulk. For the reactions at 3008C with 10 mg, the second batch
exhibited a higher f (10.4% vs. 7.5%) and a lower c (0.2% vs.
0.3%) than the first batch, consistent with anticorrelation of f
and c, and lower surface Pt/Sn ratio for the second synthetic
batch.
The dramatic increase in f, accompanied by a decrease in
c, is consistent with fewer three-fold Pt sites on the ordered
PtSn(110) surface compared to Pt(111) and Pt3Sn(111). A
Pt(111) surface consists of contiguous pure-Pt three-fold sites,
while Pt3Sn(111) bears isolated pure-Pt three-fold sites, and
Pt2Sn(111) is devoid of three-fold sites. Note that the mole
fraction of Sn in our PtSn@mSiO2 catalyst (Pt/Sn = 1:1) is
even higher than in the Sn/Pt2(111) surface alloy study. The
surface alloy studies on Pt, Pt3Sn, and Pt2Sn single crystal
surfaces have shown the three-fold Pt hollow sites to be
essential for dissociative adsorption of H2.[23–26] Chemisorp-
tion of H2 on the Sn/Pt2(111) surface alloys at room temper-
ature was found to be limited to only 2% of the saturation
coverage of hydrogen on clean Pt(111). In contrast, atomic
hydrogen readily adsorbs on the alloy surfaces at temper-
atures down to 150 K,[23] indicating that H2 chemisorption is
inhibited by kinetic rather than thermodynamic factors (high
H2 dissociation barrier).[6,7]
Due to the facile dissociative adsorption of H2 and high
rate of stepwise addition of H ad-atoms to the alkene in the
Horiuti–Polanyi mechanism, conversion by direct hydroge-
nation is extremely low for monometallic Pt NPs. The non-
linear dependence of f on Sn implicates the Pt three-fold
hollow sites in the catalysis by random addition. With
increasing Sn fraction, f also increases because of decreased
H2 dissociative chemisorption. There could also be a corre-
sponding increase in the number of sites that bind molecular
H2 and serve as active sites for direct hydrogenation.
Lastly, the efficacy of the Pt-Sn iNP catalysts in the
aqueous phase is demonstrated. Hydrogenation of 2-hydrox-
yethyl acrylate (HEA) in D2O was catalyzed by Pt3Sn@mSiO2
in the earthꢀs magnetic field. After bubbling p-H2 gas through
the slurry, the sample tube was immediately transferred into
the 400 MHz NMR magnet and the ALTADENA NMR
spectrum collected with a 908 pulse. As seen in Figures 4, S10
and S11, intense NMR signals of the methyl (c) and
methylene (d) groups of 2-hydroxyethyl propionate (HEP)
were obtained. Due to the continuous reaction in the slurry,
a reliable determination of the PHIP signal enhancement was
not possible in these experiments. Moreover, an estimated
factor of 10 in loss of polarization occurs during the ca. 10 s
transfer of the sample from low to high field.
Figure 3. A,B) Temperature dependence of pairwise selectivity, f, ALTA-
DENA signal enhancement factor, hexp, and PE-to-PA conversion, c, for
Pt@mSiO2, Pt3Sn@mSiO2 and PtSn@mSiO2 (10 mg, synthetic batch
1) at 100, 200, and 3008C (dark grey, grey, and light grey bars,
respectively). C) Linear dependence of conversion and pairwise selec-
tivity on H2 partial pressure for two PE reactant pressures (50 mg
PtSn@mSiO2, batch 2). D) Linear dependence of pairwise selectivity,
enhancement factor, and conversion on PtSn@mSiO2 catalyst mass
(batch 2).
3000-fold increase in signal enhancement relative to the
monometallic Pt@mSiO2 NPs (hexp = 0.20 ꢀ 0.07 and f =
0.0020 ꢀ 0.0007%) was observed (see Table S2). Meanwhile,
c decreases precipitously upon incorporation of Sn (Fig-
ure 3B and Table S3), following the order Pt@mSiO2 (19.5%)
> Pt3Sn@mSiO2 (17%) @ PtSn@mSiO2 (0.3%) at 3008C.
As seen in Figure 3B, conversion over Pt@mSiO2 slightly
decreased with increased temperature. This could be due to
coke formation on the pure Pt NPs where a high activity of
hydrogenation may induce local heating. Koel et al. reported
a 35% PE decomposition on Pt(111) during the TPD
experiment, ca. 5–7% decomposition on Pt3Sn, and no
decomposition on Pt2Sn as substrate temperature increased.
It was proposed that PE decomposition is also catalyzed on
contiguous pure-Pt three-fold hollow sites.[24] A slight reduc-
tion in c was observed over Pt@mSiO2 and Pt3Sn@mSiO2 in
the second run of the reaction, possibly due to the blocking of
some active sites by carbonaceous deposits.
The preceding results were obtained using only 10 mg of
PtSn@mSiO2 iNPs and 300 mbar H2. The low conversion
achieved for these conditions, attributed to the weak physi-
sorption of H2 for these iNPs, would be inadequate for most
applications. Therefore, additional experiments were per-
formed to investigate the scaling of f and c with catalyst mass
and H2 partial pressure. Figures 3C, S8 and S9 show a linear
dependence of c on pH with little change in f. Figures 3D and
2
S7 show that c also scales linearly with catalyst mass from 10
to 50 mg without significant loss of pairwise selectivity. In
these experiments, which were performed on a separate
To ensure that this hydrogenation occurs heterogeneously
on the iNPs and not homogeneously by leached metal ions, as
can occur in immobilized complexes,[41] PHIP experiments
Angew. Chem. Int. Ed. 2017, 56, 1 – 6
ꢀ 2017 Wiley-VCH Verlag GmbH & Co. KGaA, Weinheim
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