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TRANSCRIPT
Master Thesis
Synthesis of Ruthenium-based Water
Oxidation Catalysts and Mechanistic Study
February 2015
Motoki Yoshida
Division of Organic Chemistry, Department of Chemistry
School of Chemical Science and Engineering
KTH Royal Institute of Technology
Stockholm, Sweden
Abstract
Two series of new mononuclear ruthenium complexes with hydrophobic or hydrophilic
ligands [Ru(bda)L2] and [Ru(pdc)L3] (H2bda = 2,2’-bipyridine-6,6’-dicarboxylic acid;
H2pdc = 2,6-pyridinedicarboxylic acid; L = pyridyl ligands) were synthesized and their
electrochemical properties and catalytic activity toward water oxidation were examined.
It was revealed that the hydrophobic ligands introduced to [Ru(bda)L2] improved the
catalytic performance, almost twofold TON and TOF values were achieved compared to
the [Ru(bda)L2] catalyst with hydrophilic ligands. The cyclic voltammogram of
[Ru(bda)L2] exhibited marginal difference between the catalysts with hydrophobic
ligands and hydrophilic ones, implying that the hydrophobic ligands promoted the
catalytic activity by facilitating formation of a reaction intermediate dimer.
List of Abbreviations
CV cyclic voltammetry
dmso dimethyl sulfoxide
DPV differential pulse voltammetry
GC gas chromatography
H2bda 2,2’-bipyridine-6,6’-dicarboxylic acid
H2pdc 2,6-pyridinedicarboxylic acid
MS mass spectrometry
NHE normal hydrogen electrode
OEC oxygen evolving complex
pic 4-picoline
PCET proton-coupled electron transfer
TFE 2,2,2-trifluoroethanol
TMS tetramethylsilane
TOF turnover frequency
TON turnover number
WOC water oxidation catalyst
Table of Contents
1.1.1.1. Introduction ............................................................................................................. 1
1.1. Background ......................................................................................................... 1
1.2. Water Splitting .................................................................................................... 1
1.3. Water Oxidation Catalysts (WOCs) ................................................................... 3
1.4. Ruthenium-based WOCs .................................................................................... 4
1.5. Aim of Thesis ..................................................................................................... 5
2. Experimental Section .............................................................................................. 6
2.1. Synthesis and characterization............................................................................ 6
2.2. Electrochemistry ............................................................................................... 11
2.3. Water Oxidation ............................................................................................... 11
3. Results and Discussion .......................................................................................... 12
3.1. Cyclic Voltammetry ......................................................................................... 12
3.2. Pourbaix Diagram ............................................................................................. 15
3.3. Water oxidation ................................................................................................ 16
4. Conclusion .............................................................................................................. 17
Acknowledgements ....................................................................................................... 19
Reference ....................................................................................................................... 20
Supporting Information ............................................................................................... 24
1
1.1.1.1. Introduction
1.1. Background
Increasing concern about depletion of fossil fuels, air pollution and global
warming has driven scientists to explore the potential of hydrogen as a fuel of the
future.1 Since the only byproduct during the combustion of molecular hydrogen with
oxygen is water, hydrogen is sometimes considered as an environment-friendly energy
resource. However, hydrogen is a secondary form of energy, and it is promising as an
energy carrier. In other words, since molecular hydrogen scarcely occurs in nature, it is
necessary to produce hydrogen by using energy.2
There are numerous problems to tackle to realize the hydrogen economy, from
distribution and storage of hydrogen to cost and temperature problem of fuel cells.
Particularly, a key problem would be the means to produce hydrogen because most of
the hydrogen for industrial use is currently produced through transformations from
natural gas and oil.3 Although these methods are at present the least expensive processes
to produce hydrogen, adopting hydrogen produced from hydrocarbons as fuel cannot be
a substantial solution to the energy problems. A variety of methods to produce hydrogen
has been investigated, for example, gasification of coal, thermal or biological
conversion of biomass and water splitting using electricity, heat, or light.4 However,
these methods still have problems regarding, in particular, costs for large scale
production and further technical innovation is required.
1.2. Water Splitting
The idea of using water, instead of fossil fuels, as a raw material for hydrogen
generation appears to be the best in terms of environmental burden since the molecules
2
involved in this reaction are very “clean” (Equation 1).
2H2O → 2H2 + O2 (1)
While water the demand of which is expected to grow is also a precious resource, the
amount of water for hydrogen generation to fulfill transportation needs in the U.S would
account for only about 1% of the domestic use of water.5 By applying water as the
source for hydrogen, many countries can reduce their dependence on foreign natural
resources and thus can strengthen their national energy security. Also, generated oxygen
can be utilized for various purposes including manufacture of nitric acid from ammonia,
metal fabrication and healthcare use.1
There are some different forms of energy that can be used for water splitting:
light, heat and electricity. Plants harness sunlight to split water into protons, electrons
and molecular oxygen in the process of photosynthesis. This reaction is catalyzed by the
oxygen evolving complex (OEC) and the core of OEC is proven to be a Mn4CaO5
cluster surrounded by some ligands.6 Considerable effort has been devoted to mimic this
light-driven water splitting system and there has been some progress in fundamental
science, but the conversion efficiency is still too low for practical applications.7 It is
also possible to produce hydrogen by thermal decomposition of water.8 However,
nuclear power plants required to achieve the high temperature for decomposition are
accompanied by dangerous radioactive wastes and a risk of accidents.
Electrolysis of water is potentially the most environment-friendly hydrogen
production method if the electricity is obtained from renewable energy. Nevertheless,
just 4% of hydrogen is industrially produced by electrolysis of water, only when
high-purity hydrogen is required.1 This is because the hydrogen produced by
electrolysis of water is costlier than the one produced from fossil fuels. A catalyst that
3
enables electrolysis of water with a low overpotential is thus highly demanded in order
to embrace the benefit of hydrogen produced by electrolysis.
1.3. Water Oxidation Catalysts (WOCs)
The water splitting process (Equation 1) is composed of two half reactions:
water oxidation (Equation 2) and proton reduction (Equation 3).
2H2O → O2 + 4H+ + 4e- (2)
2H+ + 2e- → H2 (3)
Because both reactions have a large activation barrier, a catalyst that lowers
overpotential and enhances reaction rate is required in order to perform water splitting.
For proton reduction reaction (3), platinum-based complexes have been reported to
show efficient catalytic ability,9 but the scarcity and high price associated with platinum
limit the applications in industrial scale. First-row transition metal catalysts, such as
iron, cobalt and nickel complexes, have also attracted much attention, aiming at
mimicking the functions of so-called hydrogenase enzymes which are responsible for
both oxidation of molecular hydrogen and reduction of protons.10
Meanwhile, the water oxidation reaction (2) is currently recognized as the
bottleneck for the development of the water splitting process.11 The reaction seems to be
simple at an initial glance, but it involves the transfer of four electrons, rearrangement
of multiple bonds and formation of the O-O bond. The search for novel WOCs that
minimize the overpotential, increase the reaction rate and have a high durability has
developed a variety of molecular WOCs consisted of different metal center(s), such as
ruthenium, iridium12 or first row transition metals (e.g. manganese,13 cobalt,14 iron,15 or
copper16).
4
1.4. Ruthenium-based WOCs
Ruthenium-based WOCs are the most extensively studied WOCs since the
discovery of this class as the first homogeneous, non-protein WOCs in the early
1980s.17 While the high price of ruthenium metal is a drawback of ruthenium-based
WOCs, the molecular WOCs that exhibit the highest catalytic efficiency are to date
ruthenium-based. 18,19
[Ru(bda)(pic)2] and [Ru(pdc)(pic)3] (H2bda = 2,2’-bipyridine-6,6’-
dicarboxylic acid; H2pdc = 2,6-pyridinedicarboxylic acid; pic = 4-picoline; Figure 1) are
ruthenium-based WOCs that exhibit relatively high catalytic activity, both reported by
the author’s group.19,20 Both bda2- and pdc2- are strong electron-donating ligands, which
decrease the oxidation potentials of the catalysts and facilitate the electron transfer from
catalysts to an oxidizing equivalent.21 In the case of [Ru(bda)(pic)2], TON of 2000 and
TOF of 2500 min-1 were achieved using CeIV as oxidant.22 A kinetic study of the
catalyst showed that the consumption of CeIV is second order in the concentration of the
catalyst, implying a binuclear catalytic pathway.19 The involvement of a
seven-coordinate ruthenium dimer complex as an intermediate of the water oxidation
reaction was experimentally suggested and the seven-coordinated complex is
characterized by X-ray diffraction.23
Figure 1. Molecular structures of [Ru(bda)(pic)2] and [Ru(pdc)(pic)3]
5
On the other hand, a kinetic study of [Ru(pdc)(pic)3] proved that the catalytic reaction
is first order toward the catalyst, implying mononuclear catalytic pathway is most likely
involved.20 It was shown by NMR spectroscopy and MS analysis that the equatorial pic
is labile under acidic conditions and a solvent molecule alternatively coordinates to the
catalyst at RuIII state. It is proposed that [Ru(pdc)(pic)2(H2O)] is the real WOC. TON
of 550 and TOF of 13.8 min-1 were obtained using CeIV as oxidant.
Thirty years of research on ruthenium-based WOCs have led to significant
improvement in the catalytic efficiency. However, in order to develop WOCs which can
be utilized in industrial scale, further investigation regarding structure-activity
correlation and catalytic mechanism is of great need.24, 25
1.5. Aim of Thesis
In this thesis, four new ruthenium-bda-based or ruthenium-pdc-based WOCs
(A – D; Figure 2), to which hydrophobic or hydrophilic ligands are introduced, are
synthesized and their electrochemical properties and catalytic activity toward water
oxidation is explored.
Figure 2. Molecular structures of A - D
6
The main focus is on how the hydrophobic ligands contribute to enhance catalytic
activity. As previously explained, while ruthenium-bda-based WOCs are said to form a
dimer in the course of water oxidization, ruthenium-pdc-based WOCs are thought to
remain as a monomer during the reaction. Thus, it is anticipated that the introduced
hydrophobic ligands make the bda-based catalyst efficient because the hydrophobic
groups would aggregate in an aqueous solution and assist the formation of dimers. This
research is expected to present a new guideline regarding the design of novel WOCs.
2. Experimental Section
2.1. Synthesis and characterization
The synthesis of the WOCs A - D is shown in Scheme 1.
General: All chemicals and solvents were purchased from Sigma-Aldrich and used
without further purification unless otherwise stated. 1H-NMR spectra were recorded
with 500 MHz of Bruker Avance spectrometer with TMS as internal standard.
Rubda(dmso)2 3, [(η6-cymene)RuCl2]2 4 and phosphonate ligand 6 were prepared
following the literature methods.26–29 Complexations for complexes A - D were
performed on the basis of previous studies. 19,20
7
Scheme 1. The synthetic routes of catalysts A - D
8
Ru(bda)(4-propylpyridine)2 A. Ruthenium (III) chloride trihydrate 1 (6.50 g, 26.5
mmol) was dissolved in dmso (20 mL) with vigorous stirring under nitrogen atmosphere.
After addition of 2-propanol (70 mL), the mixture was heated to 85 oC for 24 h. At
room temperature, the precipitation was filtered off and washed with acetone and
diethyl ether to give 7.89 g of crude Ru-dmso complex 2 as yellowish powder, which
was used without further purification.
The crude product 2 (420 mg), H2bda (200 mg, 819 mmol) and methanol (20 mL) were
combined under nitrogen atmosphere and heated to 70 oC. After all the compounds were
dissolved, triethylamine (3.9 mL, 28 mmol) was added dropwise and the mixture was
heated to reflux for 4 h. After cooling down, the precipitation was filtered off and
washed with diethyl ether to afford 230 mg of Ru-bda complex 3 as brown powder,
which was used without further purification.
The crude product 3 (100 mg), 4-propylpyridine (0.13 mL, 1.00 mmol) and methanol
(20 mL) were combined under nitrogen atmosphere and heated to reflux for 20 h. After
cooling, the solvent was removed under reduced pressure and the crude solid was
purified twice by reprecipitation with methanol/diethyl ether to give brown solid A (88
mg, 0.15 mmol, three steps yield 26%). 1H NMR (500 MHz, Methanol-d4) δ 8.50 (d, J =
8.1 Hz, 2H), 7.94 (d, J = 7.6 Hz, 2H), 7.79 (t, J = 7.9 Hz, 2H), 7.58 (d, J = 5.8 Hz, 4H),
6.96 (d, J = 5.9 Hz, 4H), 2.41 (t, J = 7.7 Hz, 4H), 1.44 (q, J = 7.5 Hz, 4H), 0.76 (t, J =
7.3 Hz, 6H).
Ru(pdc)(4-propylpyridine)3 B. Ruthenium (III) chloride trihydrate 1 (3.70 g, 14.2
mmol), (R)-α-phellandrene (18.5 mL. 115 mmol) and ethanol (150 mL) were combined
under nitrogen atmosphere and heated to reflux for 4 h. After cooling, the solution was
filtered off to afford compound 4. The filtrate was reduced to the half-volume under
9
reduced pressure and the solution was kept in the fridge overnight. The generated
precipitation was filtered off to obtain additional product. In total 3.57 g of Ru-cymene
dimer 4 as dark red micro-crystalline was obtained and used without further
purification.
The crude product 4 (75.0 mg), H2pdc (41.0 mg, 0.245 mmol) and triethylamine (250
µL, 1.79 mmol) were dissolved in ethanol (8 mL) in a microwave tube under nitrogen
atmosphere. The mixture was heated to 140 oC in the microwave oven for 30 min. After
cooling, 4-propylpyridine (650 µL, 4.99 mmol) was added and the mixture under
nitrogen atmosphere was heated to 140 oC in microwave oven for 30 min. After cooling,
the solvent was removed under reduced pressure and the crude solid was dissolved in
dichloromethane (15 mL) and washed with water (10 mL) for three times. The organic
phase was dried over Na2SO4 and the solvent was removed under reduced pressure. The
crude product was purified by column chromatography on silica gel eluting with
dichloromethane/methanol (10:1, v/v). The obtained solid was further purified by
reprecipitation with dichloromethane/diethyl ether to give black solid B (108 mg, 0.172
mmol, three steps yield 57%). 1H NMR (500 MHz, Chloroform-d) δ 8.77 (d, J = 5.9 Hz,
2H), 8.13 (d, J = 5.8 Hz, 4H), 7.96 (d, J = 7.7 Hz, 2H), 7.55 (t, J = 7.7 Hz, 1H), 7.06 (d,
J = 5.8 Hz, 2H), 6.86 (d, J = 5.9 Hz, 4H), 2.58 (t, J = 7.8 Hz, 2H), 2.45 (t, J = 7.7 Hz,
4H), 1.66 (p, J = 7.5 Hz, 3H), 1.52 (p, J = 7.5 Hz, 7H), 0.93 (t, J = 7.3 Hz, 3H), 0.87 (t,
J = 7.4 Hz, 6H).
Diethyl [(4-pyridinyl)methyl] phosphonate 6. 4-Bromomethylpyridine hydrobromide
5 (1.50 g, 5.93 mmol) and chloroform (50 mL) were combined and treated with an
aqueous solution of K2CO3 (827 mg, 5.98 mmol) to quench the HBr. After phase
separation and drying over Na2SO4, triethyl phosphate (10.0 mL, 58.0 mmol) was added
10
and the solution was purged with nitrogen. The mixture was shielded from light and
heated to reflux for 10 h. After cooling, the solvent was evaporated under reduced
pressure and the resulting mixture was purified by column chromatography on silica gel
eluting with ethyl acetate/methanol (4:1, v/v) to give yellow oil 6 (922 mg, 4.02 mmol,
68%). 1H NMR (500 MHz, Chloroform-d) δ 8.54 (d, J = 5.2 Hz, 2H), 7.25 (dt, J = 4.2,
2.1 Hz, 2H), 4.13 – 3.99 (m, 4H), 3.14 (d, J = 22.3 Hz, 2H), 1.27 (t, J = 7.1 Hz, 6H).
Ru(bda){diethyl [(4-pyridinyl)methyl] phosphonate}2 C. The crude product 3 (40.0
mg), compound 6 (95.5 mg, 0.417 mmol) and methanol (25 mL) were combined under
nitrogen atmosphere and the mixture was heated to reflux for 12 h. After cooling down,
the solvent was removed under reduced pressure and the crude product was purified by
column chromatography on silica gel eluting with dichloromethane/methanol (10:1, v/v)
to afford black solid C (60.0 mg, 0.0748 mmol, yield 93%). 1H NMR (500 MHz,
Methanol-d4) δ 8.62 (d, J = 8.0 Hz, 2H), 8.04 (d, J = 7.7 Hz, 2H), 7.91 (t, J = 7.9 Hz,
2H), 7.77 (d, J = 6.0 Hz, 4H), 7.27 – 7.01 (m, 4H), 4.15 – 3.92 (m, 8H), 3.24 (d, J =
22.8 Hz, 4H), 1.18 (t, J = 7.0 Hz, 12H).
Ru(pdc){diethyl [(4-pyridinyl)methyl] phosphonate}2 D. The crude product 4 (50.0
mg), H2pdc (27.2 mg, 0.163 mmol) and triethylamine (160 µL, 1.15 mmol) were
dissolved in ethanol (8 mL) in a microwave tube under nitrogen atmosphere. The
mixture was heated to 140 oC in the microwave oven for 30 min. After cooling,
compound 6 (560 mg, 2.44 mmol) was added and the mixture under nitrogen
atmosphere was heated to 140 oC in microwave oven for 4.5 h. After cooling, the
solvent was removed under reduced pressure and the crude solid was purified by
column chromatography on silica gel eluting with dichloromethane/methanol (1:1, v/v)
to afford brown crystalline D (145 mg, 0.152 mmol, two steps yield 93%).1H NMR
11
(500 MHz, Chloroform-d) δ 8.82 (d, J = 5.7 Hz, 2H), 8.23 (d, J = 6.1 Hz, 4H), 7.98 (d, J =
7.7 Hz, 2H), 7.61 (t, J = 7.7 Hz, 1H), 7.23 – 7.13 (m, 2H), 7.06 – 6.89 (m, 4H), 4.01 (ddq,
J = 19.7, 8.4, 7.1 Hz, 12H), 3.11 (d, J = 22.6 Hz, 2H), 2.99 (d, J = 22.5 Hz, 4H), 1.19 (dt,
J = 14.0, 7.0 Hz, 18H).
2.2.Electrochemistry
Cyclic voltammetry (CV) and differential pulse voltammetry (DPV)
measurements were performed with an Autolab potentiostat with a GPES
electrochemical interface (Eco Chemie), using a pyrolytic graphite electrode (basal
plane, diameter 3 mm) (PGBE) as working electrode and a platinum column as counter
electrode and measured versus Ag/ AgCl reference electrode (3 M KCl aqueous
solution). All potentials measured herein were reported against the Ag/AgCl reference
electrode. The cyclic voltammograms were obtained in a phosphate buffer solution (0.1
M) or HNO3 aqueous solution (pH 1; trace metal grade, 70%, purified by redistillation,
99.999%; Fisher Scientific) containing a catalyst (1 mM) and TFE
(2,2,2-trifluoroethanol, >99%; 20 or 25 volume %). TFE was added to improve the
solubility of the catalysts to the solution.
2.3.Water Oxidation
The oxygen evolution was recorded with a pressure transducer (Omega
PX138-030A5 V) driven versus time by a power supply (TTi-PL601) at 8.00 V and
calibrated by gas chromatography (GC) (GC-2014 Shimadzu). First, (NH4)2[Ce(NO3)6]
(99.5%) was dissolved in HNO3 aqueous solution (initial pH 1.0) and the solution was
stirred in a 25 mL flask. Next, catalyst solution (HNO3 aqueous solution/TFE= 1/1, v/v)
12
was rapidly injected to the flask and started the measurement. Finally, the amount of
generated oxygen was calibrated by GC.
(NH4)2[Ce(NO3)6] (CeIV) is a strong one-electron transfer oxidant (E ≈ 1.72 V
vs NHE) which is soluble in water, and used as a sacrificial electron acceptor (Equation
4).
WOC
4CeIV + 2H2O O2 + 4H+ + 4CeIII (4)
The conditions used in the measurements were as follows:
A and C for TOF: HNO3 pH 1 aqueous solution (3.4 mL) containing CeIV (0.346 M)
and catalyst (1.14 × 10-4 M) and TFE (0.1 mL).
A and C for TON: HNO3 pH 1 aqueous solution (3.475 mL) containing CeIV (0.346 M)
and catalyst (2.86 × 10-5 M) and TFE (25 µL).
B and D: HNO3 pH 1 aqueous solution (2.85 mL) containing CeIV (8.33 × 10-2 M),
catalyst (6.67 × 10-5 M) and TFE (0.15 mL).
3. Results and Discussion
3.1. Cyclic Voltammetry
Figure 3 displays the cyclic voltammograms (CVs) of Ru-bda based complexes
A and C under pH 1 nitric acid condition (upper) or pH 7 phosphate buffer condition
(lower), and Figure 4 displays the CVs of Ru-pdc based complexes B and D under the
same conditions. In Table 1 the oxidation potentials, onset potential for catalytic current
acquired from DPV spectrum and catalytic current at 1.5 V acquired from CV spectrum
are summarized.
13
Figure 3. CV data of complex A at pH 1 (upper left), C at pH 1 (upper right), A at pH 7
(lower left) and C at pH 7 (lower right). [(NH4)2[Ce(NO3)6]]= 0.1 mM.
Figure 4. CV data of complex B at pH 1 (upper left), D at pH 1 (upper right), B at pH 7
(lower left) and D at pH 7 (lower right). [(NH4)2[Ce(NO3)6]]= 0.1 mM.
14
Table 1. DPV and CV data of complexes A - D
complex Eox III/ II (V) Eox IV/ III (V) Eox V/IV (V) Eonset (V) I (µA)a
A (pH=1) 0.43 0.92 -- 1.10 10.0
B (pH=1) 0.29 1.04 1.20 1.23 9.1
C (pH=1) 0.46 0.98 -- 1.18 6.8
D (pH=1) 0.31 0.70 -- 1.23 7.9
A (pH=7) 0.40 0.78 -- 1.14 61.9
B (pH=7) 0.28 0.78 1.28 1.39 42.7
C (pH=7) 0.39 0.82 -- 0.95 38.2
D (pH=7) -- 0.62 -- 1.27 17.4
a catalytic current at 1.5 V
Catalytic current was observed for all the complexes A – D at both pH 1 and pH 7. The
difference of corresponding oxidation potential between A and C were small (the
differences were smaller than 0.1 V), implying that the hydrophobic/hydrophilic part of
the ligands have little effects on electrochemical properties of the complexes.
The observed catalytic current was larger at high pH than low pH. This is
explained from Nernst equation (Equation 5):
� = ��+
��
��
��
� (5)
(where � is a cell potential, �� is a standard cell potential, �is the gas constant, �
is absolute temperature, is number of moles of electrons transferred in the cell
reaction, � is the Faraday constant, �� is chemical activity for oxidants, �� is
chemical activity for reductants.)
For the water oxidation reaction (2), E0 = 1.02 V vs Ag/ AgCl (3M KCl), so the
15
equation (5) is expressed as below:
E = (1.02-0.059 pH) V vs Ag/ AgCl (3M KCl) (6)
It is clear from the equation (6) that voltage required for water oxidation is lowered
under high pH condition and this is why the catalytic current is larger at high pH.
3.2. Pourbaix Diagram
The DPVs of complex A and C at various pH values were recorded and the
Pourbaix diagram was drown (Figure 5).
Figure 5. Plots of voltage versus pH (Pourbaix diagram) for complex A (left) and
complex C (right)
The diagram shows the thermodynamically most stable species at certain pH and
voltage. Slopes in the diagram (-0.059, which can be calculated in the same way as
equation 6 from Nernst equation) indicate that the equilibrium potential between two
species is dependent on pH value of the solution i.e. proton coupled electron transfer
(PCET) is involved. On the other hand, horizontal lines indicate that the equilibrium
potential is independent of pH value i.e. neither protons nor hydroxides are involved in
A C
16
the reaction. From this diagram, it is suggested that Ru(V)=O is involved in water
oxidation process. The voltage required for the reaction is depicted in the equation (6).
3.3.Water oxidation
Chemical water oxidation was demonstrated by using CeIV as a sacrificial
oxidant in an aqueous solution at pH 1. A typical oxygen evolving trace by using A - D
as a catalyst was depicted in Figure 6. TON and TOF were calculated as an average
value of three measurements.
Figure 6. Oxygen evolving trace by catalysts A and C (left) and B and D (right)
Table 2. Catalytic data of complexes A - D
complex TON TOFinitial (s-1)
A 1929 32
B 219a 3 × 10-2
C 1044 18
D 85a 9 × 10-3
a after 8 hours
17
As expected, bda-based complex with hydrophobic ligands A showed superior
catalytic activity compared to bda-based complex with hydrophilic ligands C. The
lifetime of these two complexes approximately appeared to be the same, but the TON
and TOF of A increased almost twofold compared to C. This is possibly because the
formation of intermediate dimers is promoted by the hydrophobic ligands in aqueous
solution, considering that the CV measurement revealed the ligands have little influence
on the electrochemical properties of the catalysts.
Meanwhile, the pdc-based complex with hydrophobic ligands B also exhibited
better catalytic performance compared to the other pdc-based complex with hydrophilic
ligands D. This result was not anticipated since the hydrophobic ligands were not
supposed to enhance the catalytic activity of the pdc-based complex that works as a
monomer catalyst. Further investigation is required to clarify the influence of
hydrophobic ligands on catalytic performance of pdc-based catalysts.
4. Conclusion
Catalysts A – D were successfully synthesized and their electrochemical properties and
catalytic activities were revealed. All the catalysts exhibited catalytic activities toward
the water oxidation reaction. It was shown that the bda-catalyst with hydrophobic
ligands A exhibited better catalytic performance compared to the one with hydrophilic
ligands C. There was marginal difference in the CV diagrams of A and C, suggesting
that the hydrophobic ligands help form an intermediate dimer and this could be why the
catalytic activity improved. However, pdc-catalyst with hydrophobic ligands B also
unexpectedly showed better catalytic performance compared to the one with
18
hydrophobic ligands D. Further research on the effect of hydrophobicity of WOCs is
underway.
19
Acknowledgements
First of all, I would like to express my sincere gratitude to Professor Licheng
Sun for giving me the opportunity to perform my degree project as a member of his
research group at KTH. It was truly great experience for me to conduct research at his
renowned laboratory in the field of artificial photosynthesis. He always provided me
with incisive comments that led me to the right direction.
I would also like to express my deepest appreciation to my supervisor, Quentin
Daniel, who had supported me throughout my work by giving me detailed instructions
and proper advice. This project would not have completed without his assistance and
encouragement. One could not wish for a better supervisor than him.
I am grateful to all the other members in the laboratory and in Department of
Organic Chemistry as well, particularly Doctor Lele Duan, Lei Wang and Fusheng Li,
for giving me useful advice and kindly explaining me instructions for laboratory
equipment. Whole my stay in the lab became fruitful thanks to these people.
Last but not least, I thank the love and patience of my family. I would like to
dedicate this thesis to my grandmother, Haruko, who always cheered me up during my
stay in Sweden by writing letters to me, but passed away three days after I returned to
Japan.
20
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Supporting Information
Figure S1. 1H NMR spectrum of A
Figure S2. 1H NMR spectrum of B
25
Figure S3. 1H NMR spectrum of C
Figure S4. 1H NMR spectrum of D
NRu
N
N
N
OO
OO
P
P
O
O
O
OO
O
26
Figure S5. DPV data of complex A and C
Figure S6. DPV data of complex B and D
27
Figure S7. Oxygen evolving trace by catalysts A and C for TOF