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Ag grid induced photocurrent enhancement in WO3
photoanodes and their scale-up performance toward
photoelectrochemical H2 generation
Won Jae Lee*, Pravin S. Shinde, Guen Ho Go, Easwaramoorthi Ramasamy
Nanohybrid Energy Conversion Devices Research Center, Korea Electrotechnology Research Institute (KERI),
Changwon 641-120, Republic of Korea
article info
abstract
Article history:
The hydrogen generation from photoelectrochemical (PEC) water splitting under visible
Received 10 December 2010
light was investigated using large area tungsten oxide (WO3) photoanodes. The photo-
Accepted 3 February 2011
anodes for PEC hydrogen generation were prepared by screen printing WO3 films having
Available online 5 March 2011
typical active areas of 0.36, 4.8 and 130 cm2 onto the conducting fluorine-doped tin oxide
(FTO) substrates with and without embedded inter-connected Ag grid lines. TiO2 based
Keywords:
dye-sensitized solar cell was also fabricated to provide the required external bias to the
WO3
photoanodes for water splitting. The structural and morphological properties of the WO3
Scale-up
films were studied before scaling up the area of photoanodes. The screen printed WO3 film
PEC water splitting
sintered at 500 C for 30 min crystallized in a monoclinic crystal structure, which is the
Dye-sensitized solar cell
most useful phase for water splitting. Such WO3 film revealed nanocrystalline and porous
Solar-to-hydrogen
morphology with grain size of w70e90 nm. WO3 photoanode coated on Ag grid embedded
conversion efficiency
FTO substrate exhibited almost two-fold degree of photocurrent density enhancement
than that on bare FTO substrate under 1 SUN illumination in 0.5 M H2SO4 electrolyte. With
such enhancement, the calculated solar-to-hydrogen conversion efficiencies under 1 SUN
were 3.24% and w2% at 1.23 V for small (0.36 cm2) and large (4.8 cm2) area WO3 photoanodes, respectively. The rate of hydrogen generation for large area photoanode
(130.56 cm2) was 3 mL/min.
Copyright ª 2011, Hydrogen Energy Publications, LLC. Published by Elsevier Ltd. All rights
reserved.
1.
Introduction
Photoelectrochemical (PEC) hydrogen (H2) production
involving photovoltaic electrolysis of water under sunlight
illumination has been investigated as a potential means of
a clean, environmentally friendly, large scale fuel production
and lot of review articles and research papers can be found in
the literature [1e6]. The solar powered PEC H2 production
system is schematically illustrated in Fig. 1(a). It consists of
two components mainly a PEC cell for producing hydrogen at
counter electrode and oxygen at semiconductor electrode; and
a dye-sensitized solar cell (DSSC) bias power for supplying the
bias to the PEC cell. Fig. 1b shows the energetic of hydrogen
generation from PEC water splitting. More details on energetic
of semiconductor anode for H2 generation can be found in the
literature [7]. Some of the prime materials requirements for
efficient visible light water splitting are: i) the semiconductor
band gap should be in the range of 1.5e3.2 eV considering the
hydrogen generation potential to be 1.23 eV so that it could
absorb a significant portion of the visible part of the solar
* Corresponding author.
E-mail address: wjlee@keri.re.kr (W.J. Lee).
0360-3199/$ e see front matter Copyright ª 2011, Hydrogen Energy Publications, LLC. Published by Elsevier Ltd. All rights reserved.
doi:10.1016/j.ijhydene.2011.02.013
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Fig. 1 e (a) Schematic diagram for PEC H2 production system consisting of a semiconductor photoanode (where O2 is
produced), a counter electrode (where H2 is produced) and a DSSC for external bias; (b) Energy-level diagram for a PEC cell
with zero electrical bias. Two half-cell reactions occurring at the photoanode and cathode to generate O2 and H2 are shown.
O2/H2O and H2/H2O are redox potentials for generation of O2 and H2. Vfb is the flat band potential and Uox is the built-in
oxygen over-potential. Conditions for efficient water splitting: Ec < Ered(H2O/H2) and Ev > Eox(O2/H2O).
spectrum (380e830 nm); ii) the conduction band edge (Ec)
position of semiconductor should be at a more negative
potential than the reduction potential of water (Ered) while the
valence band edge (Ev) position to be at a more positive
potential than the oxidation reaction (Eox) i.e. energetic of
semiconductor should meet the conditions: Ec < Ered(H2O/H2)
and Ev > Eox(O2/H2O); iii) the photocatalyst should have a
sufficiently negative flat band potential so as to have sufficient
over-potential to drive the water splitting reaction at a
reasonable rate; and finally iv) semiconductor should be stable
against photo-corrosion in aqueous environment [8,9].
Meeting these criteria, few photocatalysts such as TiO2,
Fe2O3, WO3, BiVO4 etc. have been investigated for water
splitting to produce H2 under light illumination [10e16].
Among these, Fe2O3 is a narrow band gap (w2.2 eV) material
capable of absorbing w40% of solar energy (up to 600 nm)
which is sufficiently enough for H2 production mostly in
aqueous solutions (pH>3). However, poor electron mobility
(0.01e0.1 cm2 V 1s 1) consequently leads to rapid electronhole recombination and a very low hole transport due to short
hole diffusion length (2e4 nm) [17]. In other words, it has
insufficient negative flat band potential. Despite having good
catalytic activity and stability over wide pH range, TiO2 is
generally limited by too large band gap (w3.2 eV), which fail to
absorb a significant fraction of visible light (below 385 nm),
resulting in poor conversion efficiencies under terrestrial
conditions. WO3 is again a wide band gap material with
slightly less band gap (2.7e2.8 eV) that can absorb reasonable
part of solar spectrum. WO3 with high hole diffusion length
(w150 nm) as compared with Fe2O3 (w2 nm) and TiO2
(w20 nm) can be a potential material for water splitting as
immediate recombination of electron-hole pairs could be
averted inside the semiconductor. It is stable in strong acidic
(pH<4) solutions (e.g. aq. H2SO4, H3PO4), however, shows low
chemical stability in alkaline solution (e.g. aq. NaOH, KOH).
The semiconductor based PEC water splitting system
involving a combination of photovoltaic cells and semiconductor liquid junctions (PV/SCLJ) approach is found to be
more efficient for H2 production [18]. In this approach, the
required input energy both for splitting of water and generation of external bias is provided by means of solar light. Swiss
research group [19] in an attempt proposed the tandem cell
system with a solar-to-hydrogen (STH) conversion efficiency
up to 7% using DSSC bias of w1.5 V. This so-called STH
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efficiency is sufficiently high in contrast to the theoretical
maximum STH efficiency for any material (only 20%) [20]; and
is therefore encouraging for further research. Thermodynamically, the STH conversion efficiency of WO3-based
devices remains less than 5% [20]. Arakawa et al. [21] reported
solar hydrogen production with STH efficiency of 2.8% from
a tandem cell system consisting of metal oxide semiconductor
films of area 1 1 cm2 and DSSC. A STH efficiency of 3.6% is
observed for 2.5 mm thick WO3 photoanode in 3 M H2SO4 and Pt
cathode using a PEC/PV ‘‘tandem cell’’ configuration [2]. The,
current PEC performance status of 4% STH has been achieved
in multijunction configurations using WO3 PEC interfaces [22].
However, all the previous attempts toward H2 production
using WO3 photoanode are limited only to small electrode
area (<1 cm2) at laboratory scale. There are no studies of
hydrogen production using large area photoanodes. Since,
photoanode is a key element in PEC water splitting system, it
is important to witness its scale-up performance in a development for full realization of hydrogen in the energy market.
Our group is mainly working on portable, scale-up processes
for energy harvesting nanocrystalline materials to meet the
energy requirements for their practical applications [23e25].
Transparent conducting oxides (TCOs) such as fluorinedoped tin oxide (FTO) are the commonly used substrates to
make photoanodes for PEC water splitting systems, solar cells
etc. However, relatively high sheet resistance (10e15 U/,) of
TCO substrates and its further increase upon high temperature
annealing [26] has delayed the entry of large area PEC cells into
the commercial market. PEC performance of scaled up electrodes is lower than that of tiny electrodes, since a carrier loss
occurs in resistive TCO substrate. Here we demonstrate a
simple method to reduce resistive loss and improve the
current collection of photogenerated charge carriers via strip
type semiconductor layers coated between inter-connected
metal grids embedded TCO substrates. Silver has been
a material of choice for grid line application in solar cells for
enhancing the current collection because of its high conductivity and low dark current [27]. To the best of authors’
knowledge, nobody has employed Ag grid embedded large area
TCO substrates for PEC water splitting to generate hydrogen.
In the present communication, we have successfully
demonstrated the scale-up process for WO3 photoanodes
prepared on Ag grid embedded FTO substrates by screen
printing method with remarkable improvement in photocurrent and hence hydrogen generation. PEC H2 generation has
been achieved by applying required external bias to the photoanodes using array of TiO2 based DSSC module. The novelty
of our work is that we have fabricated photoanodes with
photoactive area > 1 cm2 and have employed metal grids to
overcome the internal resistance in TCO substrates for efficient current collection in scaled up photoanodes.
2.
2.1.
were also used to fabricate electrodes for DSSC module. The
FTO substrates were cut into required dimension and
successively cleaned using acetone (for 10 min), ethanol (for
10 min) and deionized water (for 10 min) in ultrasonic cleaner.
FTO substrates of different sizes mainly 1 1.2, 1 10 and
15 15 cm2 were used after drying under nitrogen gas. Silver
current collector grid lines (dimension, width height:
0.6 mm 10 mm) were printed on FTO substrates of different
sizes using screen printable silver paste by a semi-automatic
screen printing machine (Automax). After drying at room
temperature for 30 min, Ag embedded FTO substrates were
heat treated at 180 C for 10 min. The distance between the Ag
metal grid lines was set to 8 mm (see Fig. 2). Two point
measurements show that after heat treatment at 180 C,
resistance of 5 cm length, silver grid line was around 1 U.
2.2.
Preparation of WO3 photoanodes
First, nanocrystalline WO3 powder was prepared by mixing
70% (21 g) polyethylene glycol (PEG) with a little water and
30 wt.% (9 g) ammonium metatungstate (AMT) powder. The
mixture was grinded using agate mortar for 1 h to make it
homogenous. This mixture was calcined at 500 C for 1 h to
remove the volatile components, yielding a yellow WO3
powder. After grinding smoothly, 30 wt.% of such WO3 powder
was slowly mixed with a blend of 65 wt.% a-terpinol and
5 wt.% ethyl cellulose to obtain a screen printable WO3 paste.
A 20 mm thick screen having 200 mesh per inch was used to
obtain approximately 5 mm thick WO3 film. Initially small size
Experimental
Substrates and silver metal grids
The conducting fluorine-doped tin oxide (FTO) coated glass
(TEC15, thickness: 2.3 mm, w80% transmittance, Rs 10 U sq 1)
substrates were used to make photoanodes. Such substrates
Fig. 2 e Schematic diagram of (a) small area 0.6 3 0.6 cm2;
scaled up (b) 0.6 3 8 cm2; and (c) 9.6 3 13.6 cm2 WO3
photoanodes with Ag grid embedded FTO as substrate; and
(d) schematic representation showing coating of WO3 on
Ag grid embedded FTO substrate and Ag capsulation using
epoxy.
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(square type) WO3 having an active area of 0.6 0.6 cm2 was
coated on 1 1.2 cm2 size FTO substrate. One time screen
printing of WO3 paste on to the FTO substrate and subsequent
sintering at 500 C for 30 min resulted in w5 mm thick mesoporous layer of WO3. By repeating the screen printing and
drying steps 5 times, an optimal film thickness of 25 mm (5
screen printed layers) was accomplished gradually. The optimization was based on the photocurrent performance of the
different photoanodes and is described in the results and
discussion section. Screen printing was performed in a cleanroom environment to avoid any sources of contamination on
fresh films. We had however difficulty in coating multiple
layers of WO3 between Ag grid lines embedded on FTO
substrates using screen printing. Therefore, to have a good
understanding and comparison of the results on PEC
hydrogen generation, the scale-up of WO3 electrodes on Ag
grid embedded FTO substrates was carried out with 5 mm thick
WO3 films. The 5 mm thick WO3 layers with active area of
0.6 0.8 cm2 and 9.6 13.6 cm2 were coated on FTO substrates
of size 1 10 cm2 and 15 15 cm2, respectively. In case of
15 15 cm2 photoanode, there are 12 stripe type 5 mm WO3
layers of dimension 0.6 13.6 cm2 between Ag grid lines
embedded on FTO substrates giving rise a total active area of
130.56 cm2. Note that the WO3 films are not touching the Ag
grid lines. Ag current collecting grids were further encapsulated using non-conductive and non-corrosive epoxy resin in
order to protect them from the electrolyte. Providing adequate
protection to the Ag grid is an important issue considering the
mass production and long-term stability of the water splitting
system. A scheme of the grid design and dimensions of WO3
photoanodes toward their scale-up process is shown in Fig. 2
(aed). In addition, a platinum wire (0.1 cm thick, w8 cm long)
was used as a counter electrode for the hydrogen production.
A calibrated cylindrical tube from a syringe (of 3 mL capacity)
surrounding the Pt wire was used to quantify the collected
hydrogen gas.
2.3.
3.
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Results and discussion
Fig. 3 shows the X-ray diffraction pattern of screen printed
WO3 film sintered at 500 C for 30 min. XRD analysis of characteristic diffraction peaks of WO3 using standard diffraction
data (JCPDS 01-072-0677) reveals the polycrystalline nature of
tungsten trioxide (WO3, a-phase) with monoclinic crystal
structure. Such structure closely resembles to that of prototype structure of ReO3 consisting of WO6 octahedra linked
together at the corners to produce a highly symmetrical threedimensional network with cubic symmetry [28]. The two
characteristic triplets of WO3 consisting (002), (020), (200) and
(022), ( 202), (202) reflections are seen in the diffraction angle
range of 22.5e24.7 and 33e34.5 , respectively. The faces (200),
(020), and (002) in the monoclinic phase of WO3 are proven
experimentally to give best results for photo-oxidation of
water [29,30]. Also, the crystallized monoclinic phase of WO3
is advantageous for the H2 production since it is more useful to
oxidize the water and organic species under visible light
[31e33] and is quite stable at room temperature. Using a wellknown Scherrer equation, average crystallite size of WO3 is
calculated to be 10e15 nm suggesting the nanocrystalline
nature of the formed material.
Fig. 4 shows FESEM images of thick WO3 film coated on FTO
substrate. The image reveals nanocrystalline and porous
morphology and size of nanocrystalline grains is in the range
of 70e90 nm. Inset of Fig. 4 shows the cross-sectional FESEM
image of WO3 photoanode at low magnification (1,000X) estimating a film thickness of w25 mm. Number of voids interconnecting the WO3 nanoparticles, ranging in size from 1 to
4 mm, can be seen in the FESEM image. This suggests the
presence of highly porous network in WO3. Binding such
Characterization and PEC H2 production system
The photelectrodes were characterized by using X-ray
diffractometer (Phillips, Model 3234) and field emission scanning electron microscopy (FESEM, Hitachi S4800) for structural
and surface morphological features of WO3. The solar light
PEC water splitting system for H2 production consisted of
a WO3 photoanode placed inside a glass container filled with
0.5 M of aqueous H2SO4 electrolyte. Pt wire (0.1 m thick, 8 cm
long) assembled within a calibrated cylindrical syringe, served
as hydrogen evolving cathode (counter electrode). The saturated calomel electrode (SCE) and/or a Ag/AgCl (saturated with
3 M KCl) electrode were used as reference electrodes. Required
external bias voltage for splitting of water was provided by
means of a DSSC module. The details about preparation of
DSSC module are given elsewhere [24]. The currentevoltage
(IeV) characteristics of the PEC cell and DSSC were respectively measured using Perkin Elmer Potentiostat/Galvanostat
(Model 2273) and Keithley digital source meter (Model 2400) in
both dark and light illumination. Abet Technologies Sun 2000
solar simulator (1000 W Xe source) was used as the source of
illumination and the intensity of incident light was fixed to 1
SUN (AM 1.5G, 100 mW cm 2) using a reference solar cell
(PVM-259).
Fig. 3 e X-ray diffraction pattern of screen printed WO3 film
deposited on FTO substrate and sintered at 500 C for
30 min. XRD reveals monoclinic crystal structure as
evidenced from comparison with standard diffraction data
# 01-072-0677.
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Fig. 4 e FESEM images of thick WO3 film coated on FTO
substrate exhibiting nanocrystalline and porous
morphology (Magnification 50,000X). Inset shows the
cross-sectional view of WO3 photoanode estimating a film
thickness of 25 mm (Magnification 10003).
porous morphology with the crystalline structure induces
some strain of the dislocation that could enhance the chemical reactivity [34]. The rate of water splitting reaction on the
WO3 surface can be closely connected with the density of
spaceecharge-separated electron-hole pairs. This can be
increased by enhancing electron-trapping active sites on the
WO3 surfaces by engineering the microstructure of the WO3.
The morphology, surface area, surface acidity, and defect
structure are the important factors affecting the water splitting [35]. Upon illumination, the photogenerated minority
carriers (holes) in case of compact thin films have a short
traversing distance to reach the water/WO3 interface. On the
other hand, with increasing film thickness for such films raises majority carrier (e ) diffusion path length to the back
contact (TCO) causing recombination of carriers and hence
decreasing the photocurrent. Nevertheless, the high photocurrent observed in our case for film thicknesses up to 25 mm
result from the large surface area of the inter-linked nanoporous geometry of WO3. The large, well connected voids in
WO3 film allow the electrolyte to diffuse freely. Similar kind of
behavior is shown by highly porous 22 mm thick TiO2 films [36].
Fig. 5 shows the photocurrent density curves as a function
of applied potential for various WO3 photoanodes under
simulated 1 SUN illumination in 0.5 M H2SO4 electrolyte using
a conventional three-electrode configuration. Fig. 5a shows
the J-V curves vs. SCE reference electrode under dark and light
illumination recorded for WO3 photoanodes (active area
0.6 0.6 cm2) of different thicknesses. The dark current
remained low until the redox potential was reached for
oxygen evolution in 0.5 M H2SO4 solution (1.5 V vs. SCE). For
5 mm thick WO3 (Fig. 5a), the onset of photocurrent starts after
0.35 V, which increases slowly and attains a saturation level of
2.28 mA/cm2 at 1.4 V. The plateau photocurrent region
(average of 2.28 mA/cm2) extends up to 1.8 V. Photocurrent
shoots up gradually to infinity beyond applied voltage of 1.8 V.
With increase in film thickness (increasing screen printing
layers), the plateau photocurrent increases slightly to
2.42 mA/cm2; however appearing at lower applied potentials
(1.2 V) than that in case of 5 mm thick WO3 films. A shoulder
appears near the photocurrent onset potential at around
0.25 V vs. SCE. A similar kind of behavior is reported by others
[37] in which appearance of such shoulder has been attributed
to the tendency of formic acid molecules to be specifically
adsorbed on the WO3. Although there is not much increase in
plateau photocurrent with increase in film thickness, the
onset potential shifts toward lower applied potential. This is
advantageous since PEC water splitting to generate hydrogen
can be achieved at much lower applied potentials using such
WO3. Inset of Fig. 5a shows the variation of photocurrent
densities measured at 1.23 V vs. SCE as a function of film
thickness (different screen printed layers) for various WO3
photoanodes (0.36 0.36 cm2). It is seen that the photocurrent
saturates gradually for 25 mm WO3 films. A similar photocurrent increment was also noticed in thick nanoporous TiO2
with increasing film thickness until it reaches to its maximum
optimized value of 22 mm [36]. Hence, photocurrent of
a semiconductor photoanode is determined by the crystallinity, the porous structures, the contact between the particles
and the thickness of the film.
Fig. 5b shows variation of photocurrent density for WO3
photoanode (5 mm thick, 0.6 8 cm2 active area) vs. SCE with
and without use of Ag grid embedded FTO substrate
(1 10 cm2). In the absence of Ag grid, photocurrent density
of 0.64 mA/cm2 is observed at 1.23 V vs. SCE for WO3
photoanode. Using Ag grid embedded FTO substrate, WO3
photoanode shows remarkable enhancement in photocurrent
(almost 2-fold increment) illustrating clearly the influence of
Ag grid. The noticed photocurrent enhancement can be
attributed to the use of inter-connected current collecting Ag
grids by virtue of which the photogenerated electrons are
easily collected after being transported from the WO3 to the
FTO substrate. Such current collecting grids also minimize
the voltage drop across the highly resistive TCO substrates,
thereby increasing the overall photocurrent. In other words,
incorporation of Ag grids on FTO substrate lowers the sheet
resistance of overall FTO substrate and provides more effective carrier transfer leading to efficient current collection than
that in the case of highly resistant grid-free FTO substrate.
Surface plasmon resonance (SPR) is believed to be associated
with photocurrent enhancement in semiconductors when
noble metals such Ag, Au are incorporated [38]. In the present
study, however, SPR phenomenon due to Ag grids is ruled out
as Ag grids are encapsulated using non-conducting epoxy in
order to protect from corrosion and are nowhere under the
influence of light.
To see comparatively the effect of up-scaling the photoanode active area on the PEC performance, the current
density-voltage curves are recorded (see Fig. 5c) for WO3
photoanodes having different active areas such as
0.6 0.6 cm2 (square type) and 0.6 8 cm2 (stripe type) and
9.6 13.6 cm2 (stripe type WO3 layers in the Ag grid lines with
a total active area of 130.56 cm2). It is obvious from figure that
the photocurrent density measured at 1.23 V decreases from
2.63 mA/cm2 to 1.5 mA/cm2 to 1.18 mA/cm2 with scale-up of
WO3 photoanode active area from 0.36 cm2 to 4.8 cm2 to
130.56 cm2. The observed relative decrease in photocurrent
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Fig. 5 e IeV characteristics of WO3 photoanodes of different sizes in 0.5 M H2SO4 electrolyte under 1 SUN illumination: (a)
Plot of photocurrent density as a function of applied potential for WO3 photoanodes (active area 0.6 3 0.6 cm2) of different
thicknesses. Inset shows the variation of photocurrent densities measured at 1.23 V vs. SCE as a function of film thickness
(different screen printed layers); (b) Variation of photocurrent density for 0.6 3 8 cm2 WO3 photoanode (5 mm) vs. SCE with
and without use of Ag grid embedded on FTO; (c) Effect of scale-up process on photocurrent of WO3 (5 mm thick) on Ag grid
embedded FTO substrate.
density, while increasing the photoanode active area from
0.36 to 4.8 cm2 (w13 times scale-up) and from 4.8 to 130.56 cm2
(w27 times scale-up) is 43.0% and 21.3%, respectively. Photocurrent density decreased considerably for small change in
active area for tiny TiO2 photoanodes [39], in that almost 50%
relative decrement in photocurrent density (from 5 to
2.55 mA/cm2) is observed when active area increased from
0.21 cm2 to 0.72 cm2. Such a behavior of photocurrent
(decrement with increase in area of electrode) is known to be
due to increase in surface states, originating mostly from
grain boundaries/surface defects, thereby creating recombination centre for charge carriers [39]. Although, the photocurrent density observed for scale-up WO3 photoanode
(130.56 cm2) is relatively lower than that for tiny photoanode
(0.36 cm2), such photocurrent can sufficiently split the water
to generate hydrogen. This can further be increased by
modifying the substrate surface (large surface area) as well
modifying the morphology of WO3 material. Ideally, the
photocurrent should increase with increase in photoanode
area. However, decreased photocurrent with scaling up of
photoanode could be due to defect based recombination
centers in the photoanode. We assume that scale-up of photoanode might have led to disordered structure or defects. For
small area photoanode, due to lower defect density, the photogenerated charge carriers would possess lower recombination rate as compared to the large area photoanode.
Fig. 6 shows a load-line analysis (power matching design)
for a PEC water splitting system based on scale-up WO3 photoanode (130.56 cm2 active area) and a DSSC (front-side series,
3 cells connected). To see the power matching design for
supplying the required bias to the water splitting system,
photocurrent-voltage response curves of WO3 photoanode
(130.56 cm2 active area) in 0.5 M H2SO4 electrolyte vs. SCE
(curves 1 and 2) and power output voltage characteristics of
TiO2 based DSSC (curve 3) under dark and 1 SUN illumination
are superimposed. A DSSC module fabricated in this study can
generate a voltage of about 2.1 V at open-circuit condition.
However, when connected to the load (here, PEC cell), this
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hSTH ¼
Fig. 6 e Load-line analysis (power matching design) for
a PEC water splitting system based on scale-up WO3
photoanode (130.56 cm2 active area) and a DSSC module
(front-side series, 3 cell connected). Shown are the
superimposed IeV response curves of WO3 photoanode in
0.5 M H2SO4 electrolyte vs. SCE (curves 1 and 2) and TiO2
based DSSC (curve 3) under 1 SUN illumination, indicating
an operation point of 153 mA at 1.4 V.
value will decrease. Crossing of superimposed IeV curves at
1.4 V under 1 SUN illumination indicate an operation point of
the coupled system, meaning that a bias of 1.4 V (153 mA) from
DSSC will extract maximum photocurrent from PEC cell. This
suggests that DSSC can effectively be coupled with water
splitting system to supply the required external potential bias
to the PEC cell for hydrogen generation.
The effective solar-to-hydrogen (STH) conversion efficiency of the PEC water splitting system is of prime importance for the economic evaluation. The STH conversion
efficiency is determined using relation (1) [40e42],
1:23 J
100%
Ip
(1)
where J is the current density (mA cm 2), Ip is the incident
power intensity (1.5 AM in the present case i.e. 100 mW cm 2).
The measured short circuit current densities (J ) such as 2.63
and 1.5 mA cm 2 at 1.23 V vs. Ag/AgCl for small size (0.36 cm2)
and single stripe size (4.8 cm2) WO3 photoanodes linearly
translates to STH conversion efficiencies of 3.24% and w2%,
respectively. The obtained STH efficiencies are quite better
since the theoretically maximum possible value for monoclinic WO3 is only 5% [20]. Although, these STH efficiencies are
slightly less that the reported one for 1 cm2 WO3 electrode [21],
we report the highest ever STH efficiency using scale-up WO3
photoanodes. These efficiencies can further be expected to
increase with structural and morphological improvements in
the WO3 photocatalyst.
To examine the hydrogen generation under solar light, the
PEC cell with photoanode area of 130.56 cm2 is biased using
a DSSC module. Fig. 7 shows the experimental arrangement of
actual PEC set-up involving 130.56 cm2 WO3 photoanode,
platinum counter electrode and gas collection arrangement
(calibrated cylindrical tube from a syringe) immersed in 0.5 M
H2SO4 electrolyte. The volume of hydrogen gas evolved was
determined from downward displacement of the electrolyte
in the cylindrical tube. The hydrogen production rate was
determined for an applied bias from DSSC module under 1
SUN illumination. About 1 mL of H2 gas was generated in 20 s
using scale-up of WO3 (130.56 cm2) photoanode. The rate of
hydrogen generation was calculated to be 3 mL/min. The rate
of hydrogen generation mainly depends on the charge carrier
generation and their combination with hydrogen ions at the
counter electrode and hence on the photocurrent density in
the PEC cell. More work is underway so as to improve the
hydrogen generation rate while scaling up the photoanodes.
One has to accept that hydrogen generation scheme will not
come into practice with tiny electrodes and necessitates large
Fig. 7 e Experimental arrangement of actual PEC set-up involving 130.56 cm2 WO3 photoanode, platinum counter electrode
and gas collection arrangement (calibrated cylindrical syringe) immersed in 0.5 M H2SO4 electrolyte. 1 mL of H2 was
generated in 20 s using scaled up WO3 (130.56 cm2) photoanode.
i n t e r n a t i o n a l j o u r n a l o f h y d r o g e n e n e r g y 3 6 ( 2 0 1 1 ) 5 2 6 2 e5 2 7 0
scale synthesis of photoanodes at the cost of decreased
performance. Both scale-up of electrodes and conversion
efficiency are however important for commercialization.
Therefore, a compromise between efficiency and photoanode
area should be established. A further study is needed in this
respect to simultaneously achieve the required target so as to
have efficient realization of photoelectrochemical water
splitting. The present work provides a direction for future
development of solar powered photocatalysis towards
hydrogen generation.
[5]
[6]
[7]
[8]
4.
Conclusions
We have successfully demonstrated the scale-up of screen
printed WO3 photoanodes for H2 generation under simulated
sunlight. A new idea of embedding Ag grid lines on FTO
substrate is introduced for efficient water splitting using WO3.
The additional bias required for photoelectrochemical water
splitting is fulfilled by using DSSC module. The WO3 coated on
Ag grid embedded FTO showed almost two-fold degree of
photocurrent density enhancement as compared to that on
bare FTO substrate under 1 SUN illumination in 0.5 M H2SO4
electrolyte. The solar-to-hydrogen (STH) conversion efficiencies calculated at 1.23 V for small (0.36 cm2) and large (4.8 cm2)
area WO3 photoanodes prepared using Ag grid embedded FTO
substrates are 3.24% and w2%, respectively. Although the
present STH efficiency in large area photoanode (4.8 cm2) is
less than that for tiny electrode (area <1 cm2), an efficiency of
w2% is the highest ever reported value using large area WO3
photoanodes.
[9]
[10]
[11]
[12]
[13]
[14]
[15]
Acknowledgments
This work was performed for Hydrogen Energy R&D center,
one of the 21st century frontier R&D program, funded by
Ministry of Education, Science and Technology of Korea.
[16]
[17]
Appendix A. Supplementary material
[18]
Supplementary data associated with this article can be found,
in the online version, at doi:10.1016/j.ijhydene.2011.02.013.
[19]
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