in situ-generated pvp-stabilized palladium(0) nanocluster catalyst in hydrogen generation from the...
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In situ-generated PVP-stabilized palladium(0) nanocluster catalyst
in hydrogen generation from the methanolysis of ammonia–borane
Huriye Erdogan, Onder Metin and Saim Ozkar*
Received 11th August 2009, Accepted 11th September 2009
First published as an Advance Article on the web 6th October 2009
DOI: 10.1039/b916459f
Herein, we report the in situ generation of poly(N-vinyl-2-pyrrolidone) (PVP)-stabilized
palladium(0) nanoclusters and their catalytic activity in hydrogen generation from the
methanolysis of ammonia–borane (AB). The PVP-stabilized palladium(0) nanoclusters with an
average particle size of 3.2 � 0.5 nm were formed from the reduction of palladium(II)
acetylacetonate during the methanolysis of AB in the presence of PVP at room temperature.
The palladium(0) nanoclusters are highly stable in solution for extended periods of time,
can be isolated as solid materials, are redispersible in methanol and show catalytic activity after
redispersion. The nanoclusters were characterized by TEM, XPS, FTIR, UV-Vis, XRD, and
SAED techniques. Mercury poisoning experiments indicate that PVP-stabilized palladium(0)
nanoclusters are heterogeneous catalysts in the methanolysis of ammonia–borane. The
PVP-stabilized palladium(0) nanoclusters are highly active and stable catalysts as they provide
23 000 turnovers in hydrogen generation from the methanolysis of AB over 27 h before
deactivation at room temperature. A kinetic study shows that the catalytic methanolysis
of AB is first order with respect to catalyst concentration and zero order with respect to substrate
concentration. The activation energy of the methanolysis of AB catalyzed by PVP-stabilized
palladium(0) nanoclusters was determined to be Ea = 35 � 2 kJ mol�1.
Introduction
Hydrogen is a globally accepted clean fuel which could
overcome the world energy problem and reduce the environ-
mental pollution caused by usage of fossil fuels as an energy
source.1 The main challenge for the widespread application
of hydrogen is its real-time production and its safe and
convenient storage because the low density of H2 makes it
difficult to store in compressed or liquid form.2 Metal
hydrides,3 metal organic frameworks,4 chemical hydrides,5
and hydrocarbons6 have been tested as solid hydrogen storage
materials. Although sodium borohydride has also been
considered as a solid hydrogen storage material,7 its use has
been restricted to portable fuel cell applications because of
its instability in solution without a base8 and inefficacy in
recycling the hydrolysis product.9 Recently, ammonia–borane
(AB) has attracted much attention due to its high hydrogen
capacity (19.6 wt%), high stability, and non-toxicity.10
Hydrogen can be generated from AB via thermal
decomposition,11 acid-catalyzed12 or transition-metal
catalyzed dehydrogenation,13–15 and hydrolysis.16
In contrast to NaBH4, ammonia–borane does not undergo
self hydrolysis in water and only generates hydrogen through
the hydrolysis reaction in the presence of a suitable catalyst.17
Our recent studies have shown that zeolite framework-
stabilized rhodium(0) nanoclusters and poly(N-vinyl-2-
pyrrolidone) (PVP)-stabilized cobalt(0) nanoclusters are
highly active catalysts for hydrogen generation from the
hydrolysis of ammonia–borane.18 However, liberation of
small quantities of ammonia at high AB concentrations and
inefficacy in recycling the hydrolysis product, metaborate, can
pose problems for hydrogen generation from hydrolysis of AB
in fuel cell applications. In this regard, methanolysis appears
to be advantageous for hydrogen generation from AB
(eqn (1)),19,20 as the methanolysis product can be regenerated
and no ammonia is liberated in the methanolysis—two
important requirements for fuel cell applications.10
H3NBH3 þ 4CH3OH�!catalyst NH4BðOCH3Þ4 þ 3H2 ð1Þ
Methanolysis of AB occurs only in the presence of a suitable
catalyst. Herein, we report the employment of in situ-generated,
polymer-stabilized palladium(0) nanoclusters as catalysts in
the methanolysis of AB. The catalyst systems used so far in the
methanolysis of AB are listed in Table 1.
Ramachandran and Gagare have tested various transition-
metal salts such as RuCl3, RhCl3, PdCl2 and CoCl2 in the
methanolysis of AB and shown that RuCl3 is the catalyst of
choice (Table 1).10 Although RuCl3 provides high activity for
the methanolysis of AB, the report lacks information on the
lifetime of the catalyst; as in the other two papers,19,20 it has
not been reported for how long such a high TOF value would
be retained. Also, the issue of whether the catalysis starting
with the transition metal salts is homogeneous or hetero-
geneous has not been addressed.10 It is noteworthy that
the catalytic activities of two Pd catalysts, PdCl2 and
carbon-supported Pd, are very low.10 Similarly, Pd supported
on g-Al2O3 has been reported to have much lower activity in
Department of Chemistry, Middle East Technical University,06531 Ankara, Turkey. E-mail: [email protected];Fax: +90 312 210 3200; Tel: +90 312 210 3212
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the hydrolysis of AB compared to the other transition metals
such as Ru, Rh and Pt supported on g-Al2O3.21 Despite the
low catalytic activity of palladium in both the hydrolysis and
methanolysis of AB, we have shown that the PVP-stabilized
palladium(0) nanoclusters are highly active and long-lived
heterogeneous catalysts in the methanolysis of AB.
PVP-stabilized palladium nanoparticles have been prepared
via alcohol,22 polyol,23 microwave assisted24 and chemical
reduction methods.25 For catalytic applications, PVP-stabilized
nanoparticles prepared by using one of these methods must be
separated from the synthesis solution and redispersed in the
catalysis solvent . The separation processes generally result in
a significant loss of catalyst. In this regard, in situ generation
of nanoparticles in the medium of the catalytic reaction is
significant. Polymer-stabilized palladium(0) nanoclusters were
generated for the first time in situ by reduction of palladium(II)
acetylacetonate in the presence of PVP during the methano-
lysis of AB. PVP-stabilized palladium(0) nanoclusters are
highly active catalysts in the methanolysis of AB and stable
in solution. They could be isolated from the solution and
characterized by transmission electron microscopy (TEM),
X-ray photoelectron spectroscopy (XPS), Fourier transform
infra-red (FT-IR), X-ray diffraction (XRD), selected area
electron diffraction (SAED) and UV-Visible electronic absorption
spectroscopy. Mercury poisoning was used to determine
whether the in situ generated PVP-stabilized palladium(0)
nanoclusters are homogeneous or heterogeneous catalysts in
the methanolysis of ammonia–borane. The detailed kinetics
of the catalytic methanolysis of AB were also studied by
measuring the volume of hydrogen generated during the
reaction whilst varying the catalyst concentration, substrate
concentration and temperature.
Experimental
Materials
Palladium(II) acetylacetonate (99%), borane–ammonia
complex (497%), PVP-40 (average molecular weight
40 000), were purchased from Aldrich and used as received.
Methanol was purchased from Riedel-De Haen AG
Hannover, and it was distilled over metallic magnesium. All
methanolysis reactions were performed using the distilled
methanol under inert gas atmosphere unless otherwise
specified. Teflon-coated magnetic stir bars and all glassware
were cleaned with acetone and dried in an oven at 150 1C.
In situ generation of PVP-stabilized palladium(0) nanoclusters
and the methanolysis of ammonia–borane
Both the in situ formation of PVP-stabilized palladium(0)
nanoclusters and the catalytic methanolysis of AB were
performed in the same medium. Before starting the
experiment, a jacketed reaction flask (50 mL) containing a
Teflon-coated stir bar was placed on a magnetic stirrer (IKA
RCT Basic) and thermostated to 25.0 � 0.5 1C by circulating
water through its jacket from a constant temperature bath
(Lauda RL6). Then, a graduated, glass cylinder tube filled
with water was connected to the Schlenk tube to measure the
volume of hydrogen gas evolved from the reaction. Next,
1.55 mg palladium(II) acetylacetonate (0.5 mM Pd) and
2.78 mg PVP-40 (2.5 mM) were dissolved in 5 mL methanol
in the Schlenk tube with a stir bar and stirred. Next, 64 mg
ammonia–borane (200 mM AB) was dissolved in 5 mL
methanol elsewhere and then transferred into the Schlenk tube
under argon atmosphere at 700 rpm with constant stirring.
The initial concentrations of AB and palladium were 200 mM
AB, and 0.5 mM Pd, respectively. A molar ratio of AB to
metal precursors greater than 100 was used to ensure complete
reduction of Pd2+ to its zero oxidation state and to observe
the catalytic hydrolysis of AB at the same time. The formation
of nanoclusters took less than 1 min and immediate evolution
of hydrogen gas took place, indicating that the nanoclusters
formed start to catalyze the methanolysis of AB. Catalytic
methanolysis was monitored by measuring the volume of
hydrogen gas evolved every 2 min at constant pressure by
determining the decrease in the water level of the glass tube
which was connected to the Schlenk tube. In a control experi-
ment, the stirring rate was varied in the range 0–800 rpm. It
was found that after 500 rpm, the stirring rate has no
significant effect on the catalytic activity. This indicates that
the system is in a non-MTL (mass transfer limitation) regime
at stirring rates 4500 rpm. In other words, there is no
diffusion problem due to the presence of the polymer in
concentrations of less than 5 mM.
Table 1 List of the catalysts used in hydrogen generation from the methanolysis of AB at 25 1C. The life time is given by the number of totalturnovers (TTO). Turnover frequency (TOF) values were estimated from the data given in respective references
Catalyst Amount of AB and catalyst TOF/min�1 TTO Ea/kJ mol�1 Ref.
1 RuCl3 2.9 mmol, 0.03 mol% 173 — — 102 RhCl3 2.9 mmol, 2 mol% 101 — — 103 CoCl2 2.9 mmol, 2 mol% 3.7 — — 104 NiCl2 2.9 mmol, 2 mol% 2.9 — — 105 RANEYs Ni 2.9 mmol, 2 mol% 3.6 — — 106 Pd/C 2.9 mmol, 2 mol% 2.0 — — 107 PdCl2 2.9 mmol, 2 mol% 1.6 — — 108 Cu NPs 1 mmol, 15 mol% 0.12 — — 199 Cu2O 1 mmol, 15 mol% 0.21 — — 1910 Cu–Cu2O 1 mmol, 15 mol% 0.26 — — 1911 Co–Co2B 10 mmol, 20 mol% 7.5 — — 2012 Ni–Ni3B 10 mmol, 20 mol% 5.0 — — 2013 Co–Ni–B 10 mmol, 20 mol% 10.0 — — 2014 Pd NCs 2 mmol, 0.5 mol % 22.3 23000 35 This work
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Self-methanolysis of ammonia–borane
64 mg AB were dissolved in 10 mL methanol in a jacketed
reaction flask (50 mL) containing a Teflon-coated stir bar. The
reaction flask was thermostated to a temperature in the range
15–35 1C by circulating water through its jacket from a
constant temperature bath. The experiment was started by
simultaneously closing the reaction flask and turning on the
stirrer at 700 rpm. Then the reaction was followed in the same
way as described above.
Instrumentation
The TEM and SAED images were obtained using a JEM-2010
(JEOL) TEM instrument operating at 200 kV. The samples
used for the TEM experiments were harvested from the
in situ-generated PVP-stabilized palladium(0) nanocluster
solution described above. The nanocluster solution was
centrifuged at 8000 rpm for 8 min. The separated nanoclusters
were washed with acetone to remove the excess PVP and other
residuals. Then, the nanocluster sample was redispersed in
5 mL methanol. One drop of the colloidal solution was
deposited on the silicon oxide coated copper grid and evaporated
under inert atmosphere. Samples were examined at magnifi-
cations between 100 and 400 K. The samples used for XPS
analysis were prepared by evaporating the methanol from the
nanocluster solution, as described above, by rotary evaporation
under vacuum. The resulting solid particles were washed with
acetone to remove the residuals from the solid sample under
N2 atmosphere. The X-ray photoelectron spectrum was taken
by using a SPECS spectrometer equipped with a hemispherical
analyzer and using monochromatic Al Ka radiation (1450 eV,
the X-ray tube working at 15 kV and 350 W) and a pass energy
of 48 eV. To better access the metal core in the sample, the
polymer matrix was scraped from surface of the sample via
bombardment by argon ions at 3000 eV for 3 min. The sample
prepared for the XPS analysis was also used for FT-IR
analysis. FT-IR spectra of neat PVP and PVP-stabilized
palladium(0) nanoclusters were taken from a KBr pellet on a
Bruker-Advance FTIR Spectrophotometer using Opus
software. To examine the final reaction product by11B-NMR, a certain amount of sample was taken directly
from the Schlenk tube into quartz NMR tube after the
stoichiometric hydrogen generation from the catalytic
methanolysis of AB finished. A few drops of CDCl3 solution
were added into the a quartz NMR tube. NMR spectra were
recorded on a Bruker Avance DPX 400 with an operating
frequency of 128.15 MHz for 11B-NMR. UV-Vis electronic
absorption spectra of palladium(II) acetylacetonate and
PVP-stabilized palladium(0) nanoclusters were recorded in
methanol solution on a Varian-Carry100 double beam
instrument. XRD patterns of PVP-stabilized palladium(0)
nanoclusters were recorded on a Rigaku Miniflex diffracto-
meter with Cu Ka (30 kV, 15 mA, l = 1.54051 A), over a 2yrange of 5 to 901 at room temperature.
Mercury-poisoning the methanolysis of ammonia–borane
catalyzed by PVP-stabilized palladium(0) nanoclusters.A standard
nanocluster formation and methanolysis experiment was
started with 200 mM AB, 1.0 mM palladium(II) acetylacetonate
and 5.0 mM PVP in 10 mL methanol at 25 � 0.1 1C. After
about 40% conversion of AB, elemental Hg (6.0 g, 3.0 mmol,
ca. 300 equiv.) was added to the solution under stirring.
The reaction was followed for a further 3 h.
Kinetics of the methanolysis of ammonia–borane catalyzed
by PVP-stabilized palladium(0) nanoclusters
In order to determine the rate law of the methanolysis of AB
catalyzed by PVP-stabilized palladium(0) nanoclusters, three
different sets of experiments were performed as described in
the ‘In situ generation of PVP-stabilized palladium(0) nano-
clusters in the methanolysis of ammonia–borane’ section.
Firstly, the AB concentration was kept constant at 200 mM
and the palladium concentration was varied (values of 0.5,
0.75, 1.0, 1.25, and 1.5 mM). In the second set of experiments,
the palladium concentration was kept constant at 0.5 mM and
the AB concentration was varied (values of 100, 150, 200, 250,
and 300 mM). In the third set, the methanolysis reaction was
performed at constant catalyst (1 mM Pd) and constant AB
(200 mM) concentration by varying the temperature in
the range of 15–35 1C to obtain the activation parameters;
activation energy (Ea), entalphy (DHa) and entropy (DSa).
Determination of the catalytic lifetime of PVP-stabilized
palladium(0) nanoclusters in the methanolysis of
ammonia–borane
The catalytic lifetime of PVP-stabilized palladium(0) nano-
clusters in the methanolysis of AB was determined by measuring
the total turnover number (TTON). This experiment was
started with a 20 mL solution containing 0.5 mM palladium(II)
acetylacetonate and 500 mM AB (320 mg) at 25 � 0.5 1C.
After conversion of all the added H3NBH3, checked by
stoichiometric H2 gas evolution (3.0 mol H2/mol H3NBH3),
a new batch of 320 mg ammonia–borane was added and the
reaction was kept going in this way until no hydrogen gas
evolution was observed. The ammonia generation during the
TTO experiments was checked before addition of new batch of
AB by using an acid/base indicator.
Results and discussion
Preparation, characterization and heterogeneity
of PVP-stabilized palladium(0) nanoclusters
PVP-stabilized palladium(0) nanoclusters were formed in situ
from the reduction of palladium(II) acetylacetonate in the
presence of PVP during the methanolysis of AB. In a typical
experiment, polymer and metal precursor were first mixed well
in methanol by stirring at 700 rpm and then AB was added to
the reaction solution in order to form palladium(0) nano-
clusters. As with other amine–boranes,13,18 AB acts as
reducing agent and provides two electrons for the reduction
of Pd(II) to Pd(0). Then, the Pd(0) nanoclusters are formed by
the nucleation and autocatalytic growth mechanism.26 The
abrupt colour change from pale yellow to dark brown after
addition of the AB solution into the mixture of metal
precursor and PVP indicates the formation of palladium(0)
nanoclusters. Concomitantly, hydrogen evolution starts after
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the colour change indicating that the nanoclusters are the
active catalyst in the methanolysis of AB.
The conversion of palladium(II) acetylacetonate to
palladium(0) nanoclusters can be followed in the UV-visible
electronic absorption spectra taken during the reaction
(Fig. 1). The adsorption bands of palladium(II) acetyl-
acetonate at 330, 260 and 225 nm gradually disappear upon
addition of AB into the solution with the concurrent growth of
a new absorption band at 295 nm, attributable to Pd(0)
nanoclusters.27 This spectroscopic observation indicates that
the reduction of palladium(II) to palladium(0) is complete
within less than 5 min.
Survey experiments performed by varying the polymer to
metal ratio showed that the highest stability and catalytic
activity of the PVP-stabilized palladium(0) nanoclusters is
obtained when a five-fold molar excess of polymer is used in
the methanolysis of AB. It is most likely that the complete
dissolution of PVP in methanol achieved by prolonged
vigorous stirring is required to obtain stable palladium(0)
nanoclusters. The PVP-stabilized palladium(0) nanoclusters
are highly stable in solution, even for months, and they can
be isolated from the solution as solid materials by removing
the volatiles in vacuum. The solid palladium(0) nanoclusters
isolated are also stable for months under inert atmosphere and
readily redispersible in methanol. Moreover, when redispersed
in methanol, the palladium(0) nanoclusters still show catalytic
activity in the methanolysis of AB.
The morphology and particle size of the PVP-stabilized
palladium(0) nanoclusters were studied by using TEM
(Fig. 2a). Palladium(0) nanoclusters with average particle size
of 3.2 � 0.5 nm are obtained as shown in the histogram
(Fig. 2b). The AB reduction of palladium(II) acetylacetonate
in the presence of PVP yields nearly-spherical nanoclusters
with no agglomeration. Compared to the size of PVP-stabilized
palladium nanoparticles prepared by using the well-known
alcohol reduction method (3–8 nm depending on the PVP/Pd
ratio),22 the use of mild reducing agent AB and low
temperature leads to the formation of palladium nanoclusters
in smaller particle size and narrower size distribution. In
particular, it is noteworthy that the PVP-stabilized Pd(0)
nanoclusters prepared by AB reduction are stable in solution
against agglomeration while the nanoparticles previously used
as catalysts in the methanolysis of AB20 have been shown to
undergo rapid agglomeration. This is key in obtaining higher
catalytic activity (see later).
The XPS spectrum of PVP-stabilized palladium(0) nano-
clusters given in Fig. 3 shows two well-resolved peaks at
335.8 and 341.4 eV, which are readily assigned to Pd(0) 3d5/2and Pd(0) 3d3/2, respectively, by comparison with the values of
metallic palladium.28 That no higher oxidation peak for
palladium is observed in the XPS spectrum might be due to
the protection of palladium(0) against oxidation by the surface-
adsorbed PVP during the sample preparation. Also,
comparison of the FT-IR spectra of the PVP-stabilized
palladium(0) nanoclusters and neat PVP, both taken from a
KBr pellet, shows the existence of PVP in the nanoclusters
sample, most probably adsorbed on the surface of the nano-
clusters, since the free PVP molecules should have been
removed while washing with excess acetone.
Fig. 4a shows the powder XRD patterns for the
PVP-stabilized palladium(0) nanoclusters sample. The peak
broadening is characteristic of materials having a nanometer
particle size.29 Four reflections are observed in the XRD
pattern at 2y of 39.5, 45, 59 and 66.51 that could be attributed
to 111, 200, 220 and 311 peaks of elemental palladium,30 but
another peak observed at 21.51 most probably belongs to the
residual ammonium tetramethoxyborate species remaining on
the surface of the nanoclusters. These four reflections are also
Fig. 1 UV-Visible electron absorption spectra taken during the
reaction of palladium(II) acetylacetonate with ammonia–borane in
the presence of PVP in methanol solution.
Fig. 2 (a) TEM image and (b) associated histogram for PVP-stabilized
palladium(0) nanoclusters formed from the reduction of palladium(II)
acetylacetonate (0.5 mM) by ammonia–borane (200 mM) in the
presence of PVP (2.5 mM).
Fig. 3 X-Ray photoelectron spectrum of PVP-stabilized palladium(0)
nanoclusters isolated from the reduction of palladium(II) acetyl
acetonate (0.5 mM) by ammonia–borane (200 mM) in the presence
of PVP (2.5 mM).
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seen from the SAED image shown in Fig. 4b indicating the
presence of palladium in cubic structure.11B-NMR spectra taken from the reaction solution after the
complete methanolysis of AB catalyzed by PVP-stabilized
palladium(0) nanoclusters show a single intense peak at
d E 8.6 ppm which is readily assigned to the tetramethoxy-
borate [B(OCH3)4]� anion.10
Kinetics of the methanolysis of ammonia–borane catalyzed
by in situ-generated PVP-stabilized palladium(0) nanoclusters
As the first control test before starting the kinetic studies, the
methanolysis of AB was performed in the absence of catalyst.
In these test experiments, performed at various temperature in
the range of 15–35 1C, no detectable hydrogen gas evolution
was observed from the self-methanolysis of AB over a period
of 24 h. The in situ-generated PVP-stabilized palladium(0)
nanoclusters are found to be highly active catalysts for the
methanolysis of AB at low concentrations and room temperature.
Fig. 5 shows the plots of the volume of hydrogen generated
versus time during the catalytic methanolysis of 200 mM
H3NBH3 solution in the presence of palladium(0) nanoclusters
in different Pd concentrations (0.50, 0.75, 1.00, 1.25, and
1.50 mM) at 25 � 0.5 1C. The hydrogen generation rate was
determined from the linear portion of the plot for each
experiment. The plot of hydrogen generation rate versus
palladium concentration, both in logarithmic scale (the inset
in Fig. 5), gives a straight line with a slope of 1.17 E 1,
indicating that the methanolysis reaction is first order with
respect to the catalyst concentration.
The effect of AB concentration on the hydrogen generation
rate was also studied by performing a series of experiments
starting with various initial concentrations of H3NBH3 while
keeping the catalyst concentration constant at 0.5 mM Pd.
Fig. 6 shows plots of the volume of hydrogen generated versus
time during the catalytic methanolysis of AB at various AB
concentrations. The hydrogen generation rate in units of mL
H2 min�1 was determined from the linear portion of the plot
for each ammonia–borane concentration and used for
constructing the plot of hydrogen generation rate versus AB
concentration, both in logarithmic scale (the inset in Fig. 6).
The slope of the line given in the inset of Fig. 6 is 0.09 E 0,
indicating that the methanolysis reaction is zero order with
respect to the ammonia–borane concentration. Consequently,
the rate law for the catalytic methanolysis of AB catalyzed by
in situ generated PVP-stabilized palladium(0) nanoclusters can
be given as in eqn (2).
�3d H3NBH3½ �dt
¼ d H2½ �dt¼ k½Pd� ð2Þ
Fig. 4 (a) Powder XRD pattern. (b) Selected area electron diffraction
image of PVP-stabilized palladium(0) nanoclusters.
Fig. 5 The volume of hydrogen versus time plot for the methanolysis
of ammonia–borane catalyzed by PVP-stabilized palladium(0) nano-
clusters depending on the palladium concentration. The inset shows
the plot of hydrogen generation rate versus the concentration of
palladium (both in logarithmic scale) at 25 � 0.5 1C.
Fig. 6 Volume of hydrogen versus time plots depending on the
substrate concentrations at constant catalyst concentration (0.5mM).
The inset shows the plot of hydrogen generation rate versus the
substrate concentration (both in logarithmic scale) at 25 � 0.5 1C.
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Observation of the first order kinetics for the catalytic
methanolysis of AB starting with a known Pd(0)n nanocluster
source is a compelling evidence that Pd(0) nanoclusters are the
true catalyst.
Methanolysis of AB catalyzed by PVP-stabilized palladium(0)
nanoclusters was carried out at different temperatures in the
range 15–35 1C, starting with an initial substrate concentration
of 200 mM H3NBH3 and a catalyst concentration of 1.0 mM
Pd, in order to determine the activation parameters of the
reaction. The values of rate constants, k (Table 2), for the
methanolysis of AB catalyzed by PVP-stabilized palladium(0)
nanoclusters were calculated from the slope of the linear part
of each plot in Fig. 7 and used to calculate the activation
parameters (Arrhenius plot is shown in the inset): Arrhenius
activation energy, Ea = 35 � 2 kJ mol�1; activation enthalpy,
DHa = 33 � 2 kJ mol�1; activation entropy, DSa = �150 �3 J K�1 mol�1.
A catalyst lifetime experiment was performed starting with a
20 mL solution of PVP-stabilized palladium(0) nanoclusters
containing 0.5 mM Pd and 0.5 M H3NBH3 plus 5 equiv. PVP
at 25.0 � 0.5 1C. The in situ-generated PVP-stabilized
palladium(0) nanoclusters provide 23 000 turnovers in the
methanolysis of ammonia–borane over 27 h before deactivation,
which makes them long-lived nanocatalysts. It is noteworthy
that this is the first total turnover number reported for the
catalytic methanolysis of AB.
Mercury poisoning
The ability of Hg(0) to poison heterogeneous metal(0)
catalysts,31 by amalgamating the metal catalyst or being
adsorbed on its surface, has been known for a long time.
The Hg(0) poisoning experiment is easy to perform, but it is
not definitive by itself, nor universally applicable.32 The
suppression of catalysis by Hg(0) is considered as evidence
for heterogeneous catalysis. After about 40% of conversion in
a typical methanolysis experiment at 25.0 � 0.5 1C,
300 equivalents of mercury per palladium was added into
the reaction solution and the progress of reaction was followed
by monitoring the H2 volume, as shown in Fig. 8. The
complete cessation of the catalytic methanolysis of AB upon
mercury addition is additional evidence that Pd(0) nanoclus-
ters are the real catalyst in the methanolysis of AB.
Conclusions
PVP-stabilized palladium(0) nanoclusters were easily generated
in situ during the methanolysis of ammonia–borane from
the reduction of a commercially available precursor. The
reduction of palladium(II) acetylacetonate by ammonia–
borane in the presence of PVP yields nearly spherical
palladium(0) nanoclusters with no agglomeration. The PVP
stabilizer can provide enough stabilization for the
palladium(0) nanoclusters so that they are very stable in
solution under inert atmosphere and yet highly active catalysts
for hydrogen generation from the methanolysis of ammonia–
borane at room temperature. PVP-stabilized palladium(0)
nanoclusters could be isolated as stable solid materials and
well characterized. PVP appears to be a strongly stabilizing
ligand for the palladium(0) nanoclusters, providing relatively
small size and narrow size distribution (3.2 � 0.5 nm).
Although a strong stabilizer such as PVP would sturdily
control the nanocluster formation, the particle size is also
expected to be affected by the experimental conditions such as
temperature and concentration (of substrate, precursor, and
stabilizer). Such a study was considered beyond the scope this
paper. PVP-stabilized palladium(0) nanoclusters are isolable
and re-dispersible. More importantly, when re-dispersed in
methanol, they retain their catalytic activity in the methano-
lysis of ammonia–borane. The kinetics of methanolysis of AB
were reported for the first time on the reaction catalyzed
by PVP-stabilized palladium(0) nanoclusters. Their activity
Fig. 7 The volume of hydrogen versus time plots at different
temperatures for the methanolysis of ammonia–borane catalyzed by
PVP-stabilized palladium(0) nanoclusters in the temperature range
15–35 1C. The inset shows an Arrhenius plot (ln k versus the reciprocal
absolute temperature, 1/T (K�1)).
Table 2 The values of the rate constant, k, for the catalytic methano-lysis of AB starting with a solution of 200 mM H3NBH3 and in situ-generated PVP-stabilized palladium(0) nanoclusters (1.0 mM Pd) atdifferent temperatures calculated from hydrogen volume versus time
T/1C Rate constant, k/mol H2 (mol Pd)�1 s�1
15 0.19520 0.26125 0.32630 0.41935 0.516
Fig. 8 The volume of hydrogen versus time plots for catalytic
methanolysis of 200 mM AB with and without addition of 300 equiv.
Hg(0) at 25 � 0.1 1C.
10524 | Phys. Chem. Chem. Phys., 2009, 11, 10519–10525 This journal is �c the Owner Societies 2009
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measured in TOF compares well with those of the catalysts
used previously for the methanolysis of AB (Table 1). With the
exception of expensive ruthenium and rhodium catalysts, they
provide the fastest reaction. Furthermore, PVP-stabilized
palladium(0) nanoclusters are long-lived catalysts in the
methanolysis of AB, providing 23 000 turnovers over 27 h
before deactivation at room temperature. Easy preparation,
high stability, and the high catalytic performance make the
in situ-generated PVP-stabilized palladium(0) nanoclusters
promising catalytic candidates to be employed in developing
highly efficient portable hydrogen generation systems using
AB as a solid hydrogen storage material. Although palladium
metal is more expensive than the first row metals, the
in situ-generated PVP-stabilized palladium(0) nanoclusters
are highly active catalysts in hydrogen generation from the
methanolysis of AB, even in low catalyst concentrations at
room temperature. This makes palladium(0) nanoclusters
attractive as catalysts.
Acknowledgements
Partial support of this work by Turkish Academy of Sciences,
TUBITAK (Project No: 108T840). O.M. thanks the
METU-DPT-OYP Program on behalf of Ataturk University.
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