Chemistry - A European Journal
10.1002/chem.201901698
COMMUNICATION
catalyst was lower than that of the Au28(SC
6
H
11
)
20 catalyst
synthesized for further comparison (note that the corresponding
UV-vis spectra and the atomic structures were shown in Figure
(
Figure 2C).
S7). Although the Au18(SC
same ligand (SC 11) with Au28(SC
product selectivity from Au28(SC
6
H
11
)
14 catalyst was protected by the
20, it exhibited different
20 for CO hydrogenation
A
B
6
H
6 11
H )
6
H
11
)
2
under identical reaction conditions, as shown in Figure 2F. As
much, the Au44(SPh-Bu)28 catalyst with same thiolate ligand
(
SPh-Bu) with Au28(SPh-Bu)20 showed different catalytic
performance for CO hydrogenation: the products such as
2
ethanol, methanol, formic acid and methane can be obtained
over the former, while methanol and methane were produced on
the latter (Figure 2F). These results clearly ruled out the ligand
effects of the two Au28(SR)20 catalysts on the performance of
C
D
CO
2
hydrogenation. The catalytic properties are mainly
determined by the atomic structure of gold atoms rather than
thiolate ligands.
Attenuated total reflection infrared (ATR-IR) spectroscopy
was conducted to detect the potential intermediates adsorbed
over the two isomers in the hydrogenation reaction of CO
Figure S8 shows ATR-IR spectra obtained from exposure of the
isomers to a mixture gas of CO and H . The bands at 2962 and
960 cm-1 can be assigned to asymmetric CH stretches of
methoxy groups produced by the reaction of methanol with
2
.
2
2
2
E
F
-1
catalysts, whereas the apparent bands at 2887 and 2886 cm
[
6]
were associated with formate. A set of peaks at 1383, 1239,
-
1
[7]
and 1056 cm , corresponding to methoxy species, were
observed for Au28(SPh-Bu)20, and the corresponding peaks were
-1
observed at 1383, 1241, and 1053 cm for Au28(SC
results imply that the methoxy is the major intermediate in the
hydrogenation of CO catalyzed by the two isomers.
6 11
H )20. The
2
The difference in the catalytic selectivity toward methanol
for the two isomers is understood by the chemical desorption
capacity of methanol onto the two isomeric catalysts. The
methanol-temperature-programmed desorption was carried out
and the temperature was ramped to 300 oC (note that higher
Figure 2. Catalytic performance of CO
Au28(SR)18 catalysts: (A) Au28(SPh-Bu)20 and (B) Au28(SC
Corresponding Arrhenius plots. (D) Comparison experiments with differnet
reaction gas. (E) Comparison of catalytic properties of Au28(SR)20 catalysts
with different pretreatments. (F) Catalytic results of Au18(SC
2
hydrogenation over isomeric
20. (C)
6 11
H )
6
H
11
)14 and
temperatures were not allowed because it might lead to
decomposition and aggregation of nanoclusters following the
ligands desorption which can be deduced from Figure S6). As
shown in Figure S9, the peaks of methanol desorption were
Au44(SPh-Bu)28 for CO
2
hydrogenation. Reaction conditions: 2 MPa CO /H
2 2
o
(1:3), 130 C, 24 h. Au28T: Au28(SPh-Bu)20 and Au28C: Au28(SC
6
H
11 20
) .
The two isomers showed an excellent durability and the
conversion and product selectivity in the cycles of the
o
o
CO
2
located at 197
Au28(SC 20, suggesting that Au28(SPh-Bu)20 favors the leave
of methanol from the active sites. In particular, the asymmetric
C
for Au28(SPh-Bu)20 and 210
C for
reused catalysts were comparable with the first run results
Figure S3). We compared the UV-vis spectroscopic fingerprints
6 11
H )
(
of the fresh and used catalysts and no obvious spectral change
was observed (Figure S4). The retention of characteristic optical
spectra after reactions ruled out the possibility for Au28(SR)20
decomposition under the reaction conditions. Transmission
electron microscopy studies showed that the two nanoclusters
had no obvious aggregation throughout the reactions (Figure
S5). Considering isomers themselves containing carbon sources
shape of the desorption peak of methanol over Au28(SPh-Bu)20
,
which implies a first order desorption kinetics,[ indicates that
the adsorption of methanol over the Au28(SPh-Bu)20 is non-
dissociative. In contrast, the symmetric methanol desorption
8]
peak over Au28(SC
order desorption kinetics, implies that the adsorption of
11
methanol over Au28(SC H )20 is dissociative. It is proposed that
6 11
H )20, which is associated with the second
[
9]
6
(
ligands), the comparison experiments were carried out; when
no reaction gas was introduced, no product was obtained; with
either CO or H being introduced, no product was detected
Figure 2D), indicating that the products derive from the reaction
the differences in the desorption capacity of methanol onto the
isomeric Au28(SR)20 may partially account for the different
selectivity of methanol on the two catalysts.
2
2
(
D/H and H/D exchange studies are shown in Figure S10.
During the first run of D/H exchange (black and red curves; note
2 2
of CO and H rather than organic ligands. To study the effect of
the thiolate ligands on the catalytic performance, the catalysts
were pretreated at 400 C (above ligand desorption temperature,
o
that the two isomers were pretreated in the Ar at 150 C for 1h
o
2
and then D was introduced to exchange with H species), H
Figure S6) to remove all the thiolate ligands, leaving exposed
Au(0) atoms on the surface of particles. From Figure 2E, the
reactivity of the bare gold catalysts decreased and the major
species associated with the two Au28 catalysts are identical and
assigned to the H of organic ligands. Immediately after the
exchange of D
catalysts under a D
second run of H/D exchange. The new peaks (blue and pink
curves) were observed (284 oC for Au28(SC 20 and 371 o
for Au28(SPh-Bu)20), which are tentatively ascribed to the
2
with H species of ligands and the cooling of
product was CH
may have been changed. Moreover, the Au18(SC
nanoclusters (where C 11 = cyclohexyl) and the Au44(SPh-Bu)28
nanoclusters (where Ph-Bu 4-tert-butylphenyl) were
4
, suggesting that underlying reaction pathway
2
stream, H was introduced to perform the
2
6
11 14
H )
6
H
6
H
11
)
C
=
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