Hostname: page-component-cd9895bd7-dk4vv Total loading time: 0 Render date: 2024-12-24T02:46:03.265Z Has data issue: false hasContentIssue false

Recent developments in solar water-splitting photocatalysis

Published online by Cambridge University Press:  17 January 2011

Frank E. Osterloh
Affiliation:
University of California, Davis; [email protected]
Bruce A. Parkinson
Affiliation:
Department of Chemistry and the School of Energy Resources, University of Wyoming; [email protected]

Abstract

Although photovoltaic cells have great potential for supplying carbon-free energy, they suffer from the lack of an efficient and cost-effective energy storage process that can supply energy for transportation and nighttime use. A direct way to convert solar energy into chemical fuels would solve this problem. Of several possible schemes, the photon-driven electrolysis of water to produce hydrogen and oxygen has been studied most. Photoelectrolysis of water can be achieved with either self-supported catalysts or with photoelectrochemical cells. This article will introduce the basic principles of solar water splitting and highlight recent developments with semiconductor light absorbers and co-catalysts. The role of combinatorial approaches in identifying new metal oxide visible light-absorbing semiconductors will be briefly described, and the potential of using nanomaterials for more efficient devices will be discussed. Separate articles in this special issue will focus on recent developments in water-splitting concepts.

Type
Introduction
Copyright
Copyright © Materials Research Society 2011

Driving force for cheap solar fuels

The world’s population is increasing and is expected to continue increasing until at least mid-century. All of these new inhabitants will require water, food, shelter, transportation, and consumer products, all of which need energy to produce and/or deliver. The population increase, along with the rapid growth of many developing economies, indicates that the demand for energy may more than double by mid-century. Even though they are a finite resource, fossil fuels would be capable of meeting this demand, albeit at an increasing cost as the easy-to-extract sources are depleted. However, the increasing concentration of CO2 in the atmosphere, as a result of the combustion of these carbon-based fuels, is predicted to result in unacceptable changes in the Earth’s climate. In addition, pollution such as sulfur dioxide emissions and oil spills also point to the need for carbon-free alternative energy sources. Nuclear power and wind are both commercially viable carbon-free technologies that can contribute to the present and future energy mix. However, finding a viable way to tap solar energy, the most abundant and universally available source of renewable energy, is urgently needed.Reference Lewis and Nocera1 One problem with solar energy is that it is quite diffuse, requiring large areas of solar collectors to harvest significant amounts of power. Therefore, cost reductions in the production of thin-film solar cells are needed to produce solar electricity at a cost that can compete with conventional power sources if the costs of carbon emissions and other pollution are included. The other “Achilles’ heel” of solar energy is that it is difficult to store as fuel for nighttime and transportation uses. Since fuels account for more than 70% of current energy consumption, there is an urgent need to convert solar energy directly to fuels, ideally liquid fuels that are easy to transport and store. To try and quickly develop systems to directly convert solar energy to fuels, the Department of Energy recently awarded a five-year $125 million research grant to establish a “Solar Hub” to improve what are now only ideas or inefficient laboratory demonstrations into a viable solar fuels technology operating at 10% efficiency or higher.

Solar-based water splitting methods

Plants can convert and store solar energy as complex molecules, such as carbohydrates and other biomass; however, photosynthesis is not very efficient, and the stored energy in plants and the large amounts of arable land needed to grow them compete with other land uses such as food production. Storing solar energy by splitting water into hydrogen and oxygen has long been considered a promising idea; in fact, in 1874, Jules Verne, recognizing the finite supply of coal and the possibilities of hydrogen derived from water electrolysis, made the comment that “water will be the coal of the future” (Jules Verne, The Mysterious Island (available at http://www.literature-web.net/verne/mysteriousisland, 1874). However, as of yet, there are no economical methods for fulfilling this prediction, partially because of problems of efficiently storing and handling hydrogen. In addition to generating the required H2 from photocatalytic water splitting, researchers have devised and tested a number of thermochemical cycles that use high temperatures generated in focusing solar concentrators to split water.Reference Kodama and Gokon2, Reference Abanades, Charvin, Flamant and Neveu3 This process also has its own distinct materials needs and will not be reviewed herein.

The cost per watt of solar photovoltaic electricity has been steadily decreasing, and current technology can mate solar cells with conventional water electrolysis units to produce hydrogen. If cost were no object, one could generate hydrogen from sunlight and water at very high efficiencies, however, the high-efficiency tandem solar cells and an electrolyzer operating at high faradaic efficiency would be extremely expensive. What is needed are semiconducting materials that can accomplish the absorption of light, the separation of the photo-generated charge carriers, and the efficient transfer of the carriers to an electrolyte solution to produce hydrogen and oxygen from water directly in one inexpensive device. The semiconducting materials must be highly stable, so as not to degrade in 20 or more years due to exposure to sunlight and electrolyte; they must have conduction and valance band energies such that the photo-generated electrons are sufficiently reducing to produce hydrogen, and the holes are sufficiently oxidizing to produce oxygen from water. In addition, they must be inexpensive. The problem is that no material, or combination of materials, that meets these requirements is known. In this issue, we will review some of the approaches that are being used to discover and optimize water splitting via photoelectrochemical or photocatalytic processes. Yang et al. describes bioinspired approaches to improve catalysts for water electrolysis. Zhang emphasizes the promise of inorganic nanostructured materials. Maeda and Domen describe (oxy)nitride materials as a possible way to increase visible light absorption of water splitting photocatalysts. Finally, Kudo will address the same problem using z-scheme photocatalyst systems, in which separate semiconductors are coupled electrochemically or electronically to improve water splitting efficiency.

Photoelectrochemical water splitting

Although oxygen evolution was observed as early as 1968 by illuminating an electrode made from the rutile form of TiO2 in solution,Reference Boddy4 Fujishima and Honda first pointed out the application of this concept to water photoelectrolysis in a series of experiments that used an n-type rutile crystalReference Fujishima and Honda5, Reference Fujishima and Honda6 as part of a photoelectrolysis cell, shown in Figure 1a. Here, the interaction of light with TiO2 produces electron–hole-pairs, of which the holes oxidize water at the TiO2 surface to form oxygen, and the electrons migrate to the Pt counter electrode to reduce water to form hydrogen. It should also be pointed out that the conduction band of rutile is not negative enough to reduce water, and so in the original publications, a “pH bias” was present where the oxygen-producing side of the cell was basic with respect to the hydrogen-producing electrolyte. While rutile is stable under illumination in aqueous electrolytes, its large bandgap (3.0 eV) limits its utilization to the UV portion of the solar spectrum, and thus limits its ultimate efficiency. Later work, using heterojunctions of expensive and not completely stable III–V materials, such as a GaInP2 and a n–p-GaAs junction photoanode in series and a Pt counter electrode, demonstrated a 12.4% efficiency of conversion of light energy to stored chemical energy in the form of hydrogen and oxygen.Reference Khaselev and Turner7 The principal advantage of this tandem or z-scheme configuration (Figure 1b) is that either semiconductor only has to supply part of the photovoltage required to electrolyze water. As a result, materials with smaller bandgaps can be used that absorb more sunlight in the visible and near-infrared region of the solar spectrum. A two-semiconductor system, with both a p-type and n-type semiconductor photoelectrode, can be configured in several ways. Either the two light absorbers are placed side by side so each one is exposed to the full solar spectrum, or, alternatively, the semiconductors are placed in series, with the larger bandgap semiconductor in front of the smaller bandgap material. In both cases, the two materials must absorb nearly equal numbers of solar photons, since the current through each semiconductor must be matched due to the recombination at the ohmic contacts that provides the summation of the two photovoltages. Because a tandem system requires twice as many photons to split water, the quantum yield is half that of a single photoelectrode system. The advantage of placing semiconductors in series is that one glass substrate, with a transparent conducting layer on both sides, could be used for both materials, reducing the total system costs (see Figure 1b). For the parallel arrangement, two substrates would be required, but they need not be transparent (as in the case of the stacked system discussed previously), so cheaper and more abundant materials may be utilized.

Figure 1. (a) Photoelectrochemical cells with single bandgap and (b) dual bandgap absorber (tandem). Blue and red light are absorbed by the large bandgap (front) and small bandgap semiconductors (back), respectively. E g, bandgap energy; TCO, transparent conductive oxide.

Particulate and colloidal semiconductors

Shortly after the discovery of photoelectrochemical cells, it was also shown that water could be split into hydrogen and oxygen using self-supported photocatalysts (Figure 2a). These “miniature photoelectrochemical cells” consist of a semiconductor powder or colloid (often a large bandgap metal oxide) to which a noble metal (e.g., Pt) is fused. In one configuration, the catalyst absorbs the light and separates the electron–hole-pair at the metal/semiconductor interface. The electron then reduces water on the noble metal, and the hole oxidizes water on the semiconductor surface. To achieve these functions, the energetics of the photocatalysts must satisfy the same thermodynamic demands as a photoelectrochemical cell. An energy diagram is shown in Figure 3. While most photocatalysts are single bandgap absorbers, some employ the z-scheme configuration, shown on the right side of the diagram. In one of the first systems, Arakawa and co-workers used Pt-TiO2 (anatase bandgap energy, E g = 3.2 eV) for water reduction and Pt-TiO2 (rutile) for water oxidation.Reference Abe, Sayama, Domen and Arakawa8 Since the photocatalyst particles could not be wired up like the photoelectrodes of a photoelectrochemical cell, redox shuttles needed to be employed to ensure directional electron transfer between the two light absorbers. These shuttles must have high specificity for accepting electrons from the photoanodic particles and delivering them to the photocathodic particles.

Figure 2. (a) Heterogeneous photocatalyst suspended in water. Each catalyst particle consists of a semiconductor material linked to a co-catalyst. The semiconductors absorb the light and carry out water oxidation, whereas the co-catalyst reduces protons. Charges are separated at the materials interface. E CB, conduction band energy level; E VB, valence band energy level. (b) Design for photocatalytic water splitting reactor. A polymer pipe is used to hold the photocatalyst suspension and to separate the H2 and O2 gas mixture by allowing selective H2 diffusion through the polymer walls. The photo-generated H2 then accumulates in the hydrogen tank. Oxygen gas is carried with the water flow and is removed in the oxygen tank. The H2/O2 gas mixture can be diluted with nitrogen to reduce the explosion risk.

Figure 3. Energy scheme for photocatalytic water splitting. In the single absorber case, a single photon must generate electron–hole-pairs at suitable potentials to both reduce and oxidize water. Kinetic barriers associated with the water redox reactions increase the required potentials above and below the thermodynamic ones (0.00 and 1.23 V at pH = 0). Since about one-third of the semiconductor bandgap energy is used for separating the electron–hole-pair, the minimum bandgap of the single absorber is about 2.00 eV. For the photoanode case, a lower bandgap can be used, but for water oxidation, the photo-generated electrons need to be extracted with an electrode or by using a chemical oxidant. The photocathode requires an electron source (electrode or reducing agent) to enable photocatalytic water reduction. In the tandem (or z-scheme) configuration, photoanode and photocathode are combined in series to split one molecule of water after absorbing four photons. This requires a directional redox shuttle or an external power source. E(H+/H2), E(H2O/O2), normal reduction potentials; A, electron acceptor; D, electron donor.

Compared to photoelectrochemical cells, particulate or colloidal photocatalysts have the advantage that the photolysis can take place in the homogeneous phase without the requirement of expensive transparent electrodes and without the need for directional illumination. On the other hand, one needs to separate the explosive mixtures of hydrogen and oxygen immediately when formed, and this separation process will consume additional energy, reducing the overall efficiency of the water-splitting process. Also, since catalysts for hydrogen and oxygen production from water are often good catalysts for the recombination of hydrogen and oxygen, illumination of such systems without rapid removal of the products will eventually result in a photostationary state, where forward and back reactions have equal rates, and no more net water splitting can occur. The photoreactor design in Figure 2b solves these problems by cycling the catalyst suspension inside a transparent, semipermeable polymer pipe that separates H2 and O2 as they are formed.

For research purposes, when one wants to study only one of the water-splitting half reactions without the complications associated with the kinetics of the other half reaction, sacrificial reagents can be used to scavenge either holes or electrons; however, these additives are not viable for any practical system for sustainable energy production. The most common examples of hole scavenging agents introduced into solution are alcohols (usually methanol), amines (usually triethanolamine or EDTA), or sulfite salts. Electron scavengers, such as the easily reduced Ag+, are also added when studying oxygen evolution.

For suspended photocatalyst powders, metal or metal oxide co-catalysts are often employed to take over the function of the counter electrode in a photoelectrochemical cell (Figure 2a). Co-catalysts can be deposited by soaking the semiconductor powder in a solution of the metal salt followed by reduction with hydrogen gas or photochemically in the presence of a weak electron donor, such as methanol. Under these conditions, co-catalysts often form nanoscale particles. The main purpose of the co-catalysts is to lower the electrochemical overpotentials associated with the multielectron water oxidation and reduction reactions (Figure 3). Another function is to provide an interface to enhance electron–hole separation. For water oxidation, the best known catalytic materials are RuO2 and IrO2, whereas for water reduction, noble metals such as Pt, Pd, and Ni are often used. As mentioned previously, many co-catalysts (e.g., Pt) catalyze the back reaction of H2 and O2 to water. However, work by Domen and co-workers has shown that a Cr2O3 nanoscale coating on Rh particles can inhibit the back reaction by blocking access of O2 to the Rh particles.Reference Maeda, Teramura, Lu, Saito, Inoue and Domen9 Currently, there is a pressing need for new catalyst materials that do not employ precious metals. The recent report where amorphous Co-oxyphosphates are used as water oxidation catalysts is promising.Reference Surendranath, Dincǎ and Nocera10 A different approach involves the synthesis of molecular catalysts made from more abundant and less expensive metals that also offer the flexibility of tuning their properties by rational synthetic control of their structure. The article by Yang et al., in this special issue reports on recent developments in this area.

Maximum theoretical efficiency

The maximum efficiency of a photovoltaic device is governed by the fraction of the solar energy that can be absorbed and the photovoltage that can be generated, both of which are related to the bandgap or bandgaps of the materials in the device. All conventional devices have thermalization losses from carriers created at energies greater than the bandgap relaxing rapidly to the band edge. These losses constrain the efficiency to the so-called Shockley Queisser efficiency limit for photovoltaic cells,Reference Shockley and Queisser11 where the optimum bandgap for a single junction photovoltaic device is around 1.4 eV, and the maximum efficiency is about 30% at 1 sun of illumination. The need to generate a photovoltage of more than 1.23 V, the thermodynamic potential needed to electrolyze water, adds additional considerations for the optimal efficiency for a photoelectrolysis device. The additional voltage that needs to be generated in the device to drive the electrochemical oxidation and reduction of water at current densities that would be generated at one sunlight intensity (15–25 mA/cm2) adds at least 0.6 V to the photopotential needed. Therefore, if a single semiconductor absorber is used for water splitting, good catalysis of water oxidation and reduction are achieved using the rule of thumb that a good photovoltaic device generates at most about two-thirds of its bandgap in photovoltage, at 1 sun. Thus, the minimum bandgap needed is greater than 2.0 eV (0.66 × 2.1 eV + 0.6 eV). This requirement leaves out much of the solar spectrum and reduces the maximum practically achievable efficiency to less than 10%.

When a p-n or tandem photoelectrolysis system is used, the photovoltages in the two semiconductors can add at the expense of the recombination of majority carriers at the contact between the two materials. This allows one to employ lower bandgap materials that can absorb photons, even extending into the near-infrared, where there is considerable solar photon flux. The trade-off is that due to the recombination, the quantum yield is reduced by a factor of two, because now two photons are required to generate one electron–hole-pair of sufficient energy to split water. The result is that considerable higher efficiencies can be achieved in these multijunction devices. For a tandem device with two bandgaps of about 1.9 and 1.2 eV, a maximum practical water splitting efficiency of about 15% can be achieved. More detailed treatments of these efficiency limits are given in the literature.Reference Bolton, Strickler and Connolly12Reference Weber and Dignam14

Nanostructured materials

In recent years, nanomaterials have also emerged as efficient components of photoelectrochemical cells and photocatalysts. Because of their small size, photogenerated carriers in nanocrystals are always created near a surface, where water conversion takes place. For example, bulk single-crystal α-Fe2O3 (hematite) has a very low activity as a photocatalyst because its paramagnetism shortens the lifetimes and diffusion length (2–20 nm) of its photogenerated carriers,Reference Cesar, Kay, Martinez and Gratzel15 so they recombine within the material before they reach the electrolyte interface. In addition, the d-d transitions in transition metal oxide semiconductors, which impart visible light absorption in these materials, are forbidden, resulting in low absorption coefficients and carrier creation deep in the material where a space charge field is not present to separate the electron–hole-pairs. Nanocrystalline α-Fe2O3, on the other hand, can more efficiently photocatalyze water oxidation because the small dimensions of the crystallites (10–20 nm) allow the photogenerated carriers to diffuse to the electrolyte interface and react with water. Furthermore, optimizing the nanostructure of the film can result in absorption of all photons with energies above the bandgap.Reference Cesar, Sivula, Kay, Zboril and Grätzel16 In photoelectrolytic cells, such nanoscale effects have led to 50–90% efficiency gain.Reference Cesar, Kay, Martinez and Gratzel15, Reference Duret and Grätzel17, Reference Zhong, Sun, Inumaru and Gamelin18 It is likely that the same principle can be applied to other metal oxides with short carrier diffusion lengths.

For many other semiconductors, quantum size effects can be utilized to increase performance for solar water splitting. By changing the size and shape of semiconductor nanocrystals, the band energies can be modified, and redox potentials of electrons and holes can be tuned. Frame et al. demonstrated for the first time that nano-CdSe (E g = 2.7 eV) becomes active for photocatalytic H2 evolution from water containing sulfite/sulfide as a sacrificial electron donor, while bulk CdSe (E g = 1.7 eV) is not.Reference Frame, Carroll, Larsen, Sarahan, Browning and Osterloh19, Reference Frame and Osterloh20 The activation is due to a raised conduction band edge (–0.55 V, normal hydrogen electrode, NHE, pH = 7) caused by quantum size confinement. As a result, electrons are about 0.45 V more reducing than those in bulk CdSe (–0.10 V, NHE, pH = 7).

Sambur et al. has recently demonstrated a photovoltaic system with PbS quantum dots covalently bound to a TiO2 crystal surface that when excited with photons of more than 2.8 times the quantum dot bandgap, can collect two electrons per photon injected into the TiO2 conduction band as photocurrent.Reference Sambur, Novet and Parkinson31 Systems with quantum yields for electron generation of more than one for high-energy photons can reduce some of the losses associated with the Shockley-Queisser limit, as discussed previously, but this multiple exciton collection has not yet been demonstrated in a water-splitting system.

Combinatorial techniques for discovery and optimization of photocatalysts

It is primarily for their stability that metal oxide semiconductors arguably hold the most promise for constructing a stable photoelectrolysis system. However, many of the early transition metal oxides are wide bandgap materials that do not absorb a sufficient amount of the solar spectrum. Several research directions have emerged to overcome this limitation. They include nitrogen incorporation into the metal oxide lattice and combinatorial metal oxide syntheses. While metal oxynitrides will be discussed in the article by Maeda and Domen, combinatorial techniques will be briefly discussed here.

Multicomponent materials are often required when a material with special properties needs to be discovered or optimized. Elements specific to performing each of the required roles in the overall functionality of these special materials need to be combined in specific proportions in order to create the desired synergy. High-temperature superconductivity is a good example of a special property requiring multicomponent materials. The superconducting oxides with the highest known transition temperatures contain four or five metals (HgBa2CaCu2O6+δ and Hg0.8Tl0.2Ba2Ca2Cu3O8.33). Since our present theoretical knowledge is insufficient to a priori calculate the behavior of such complex systems or estimate the identity and atomic ratios of the specific metals needed to perform the efficient photoelectrolysis of water, for now empirical methods will be necessary to identify the best material. Hundreds of thousands or perhaps millions of mixed metal oxide photocatalyst compositions may need to be produced and tested for efficiency and corrosion resistance until an effective material is discovered.

Combinatorial methods provide tools to speed the discovery process when a large number of candidate materials need to be synthesized and screened for the property of interest.Reference Reddington, Sapienza, Gurau, Viswanathan, Sarangapeni, Smotkin and Mallouk21 Baeck and MacFarland have demonstrated the electrochemical deposition of metal oxide compositions using robotics to plate and screen individually created materials and have looked at water photo-oxidation catalysts using multiplexed photoelectrochemical cells.Reference Baeck, Jaramillo, Brandli and McFarland22 Woodhouse and Parkinson have developed a high throughput combinatorial search strategy for the identification of multicomponent metal oxide materials with suitable bandgaps and band positions for water photoelectrolysis operating as either a photoanode or a photocathode. Their combinatorial search strategy uses ink jet printing of overlapping patterns of metal oxide precursors onto conductive glass substrates.Reference Woodhouse, Herman and Parkinson23 The simplest metal oxide precursors are metal nitrates that decompose to form metal oxides, oxygen, and NO2 by heating at relatively low temperatures (<500°C). The low cost, speed, and versatility of ink jet printing have already made it attractive for combinatorial searches for fuel cell catalysts,Reference Reddington, Sapienza, Gurau, Viswanathan, Sarangapeni, Smotkin and Mallouk21, Reference Cong, Doolen, Fan, Giaquinta, Guan, McFarland, Poojary, Self, Turner and Weinberg24 organic device combinations,Reference Sirringhaus, Kawase, Friend, Shimoda, Inbasekaran, Wu and Woo25 and biomaterials.Reference MacBeath and Schreiber26 We feel that the ink jetting approach has several major advantages for identifying oxide photoelectrolysis materials. It is a simple method, and even inexpensive off-the-shelf ink jet printers can be used. It can be adapted to broad screening of compositions for discovery or very fine control of stoichiometry and doping for optimization. We have used this approach to discover several new promising oxide semiconductors.Reference Woodhouse and Parkinson27 Since there are so many possible combinations to produce and screen, we have developed a project to enlist a multitude of undergraduates and high school students to help with the effort to discover these most important materials. The Solar Hydrogen Activity research Kit, or SHArK Project, uses simple materials such as Lego Mindstorms to provide the students with everything they need to produce libraries of metal oxides and screen them for photoelectrolysis activity.Reference Parkinson28, 29

Additional design criteria

Besides high efficiency, there are additional criteria that need to be considered for a successful solar water-splitting system. As stated previously, the photoactive materials must be inexpensive and very stable against photocorrosion to allow an energy and financial return from the initial investment. Any photoelectrochemical cell will have to be designed with an ion-conducting separator or electrolyte path between the two electrodes and with separate gas collection plumbing for hydrogen and perhaps oxygen (a conceptual photoelectrochemical device is shown in Figure 4). These supporting structures, electrolyte and gas handling systems, must also last for many years. Since almost none of these design criteria can be met with current materials, it is clear that there is a strong need for basic research in solar water splitting and for many researchers to get involved in the discovery and optimization of these materials.

Figure 4. Conceptual design of photoelectrochemical water-splitting system with light concentration. The cylindrical pipes serve as light concentrators and gas collectors. H2 gas (green) is formed at the illuminated photoelectrode and O2 gas (red) at the counterelectrode. Ion transport between pipes is accomplished using porous membranes. Adapted with permission from Reference Reference Turner30. ©2008, Macmillan Publishers.

Acknowledgments

Frank Osterloh thanks the National Science Foundation (NSF Grant 0829142) for support and Research Corporation for Science Advancement for a Scialog award. Bruce Parkinson acknowledges the U.S. Department of Energy, Office of Science, NSF, and the University of Wyoming for support of his research in photoelectrochemical energy conversion.

References

1.Lewis, N.S., Nocera, D.G., Proc. Nat. Acad. Sci. U.S.A. 103, 15729 (2006).CrossRefGoogle Scholar
2.Kodama, T., Gokon, N., Chem. Rev. 107, 4048 (2007).CrossRefGoogle Scholar
3.Abanades, S., Charvin, P., Flamant, G., Neveu, P., Energy 31, 2805 (2006).CrossRefGoogle Scholar
4.Boddy, P.J., J. Electrochem. Soc. 115, 199 (1968).CrossRefGoogle Scholar
5.Fujishima, A., Honda, K., Nature 238, 37 (1972).CrossRefGoogle Scholar
6.Fujishima, A., Honda, K., Bull. Chem. Soc. Jpn. 44, 1148 (1971).CrossRefGoogle Scholar
7.Khaselev, O., Turner, J.A., Science 280, 425 (1998).CrossRefGoogle Scholar
8.Abe, R., Sayama, K., Domen, K., Arakawa, H., Chem. Phys. Lett. 344, 339 (2001).CrossRefGoogle Scholar
9.Maeda, K., Teramura, K., Lu, D.L., Saito, N., Inoue, Y., Domen, K., Angew. Chem. Int. Ed. 45, 7806 (2006).CrossRefGoogle Scholar
10.Surendranath, Y., Dincǎ, M., Nocera, D.G., J. Am. Chem. Soc. 131, 2615 (2009).CrossRefGoogle Scholar
11.Shockley, W., Queisser, H.J., J. Appl. Phys. 32, 510 (1961).CrossRefGoogle Scholar
12.Bolton, J.R., Strickler, S.J., Connolly, J.S., Nature 316, 495 (1985).CrossRefGoogle Scholar
13.Varghese, O.K., Grimes, C.A., Sol. Energy Mater. Sol. Cells 92, 374 (2008).CrossRefGoogle Scholar
14.Weber, M.F., Dignam, M.J., Int. J. Hydrogen Energy 11, 225 (1986).CrossRefGoogle Scholar
15.Cesar, I., Kay, A., Martinez, J.A.G., Gratzel, M., J. Am. Chem. Soc., 128, 4582 (2006).CrossRefGoogle Scholar
16.Cesar, I., Sivula, K., Kay, A., Zboril, R., Grätzel, M., J. Phys. Chem. C 113, 772 (2009).CrossRefGoogle Scholar
17.Duret, A., Grätzel, M., J. Phys. Chem. B 109, 17184 (2005).CrossRefGoogle Scholar
18.Zhong, D.K., Sun, J.W., Inumaru, H., Gamelin, D.R., J. Am. Chem. Soc. 131, 6086 (2009).CrossRefGoogle Scholar
19.Frame, F.A., Carroll, E.C., Larsen, D.S., Sarahan, M.S., Browning, N.D., Osterloh, F.E., Chem. Commun. 2206 (2008).CrossRefGoogle Scholar
20.Frame, F.A., Osterloh, F.E., J. Phys. Chem. C, 114, 10628 (2010).CrossRefGoogle Scholar
21.Reddington, E., Sapienza, A., Gurau, B., Viswanathan, R., Sarangapeni, S., Smotkin, E.S., Mallouk, T.E., Science 280, 1735 (1998).CrossRefGoogle Scholar
22.Baeck, S.H., Jaramillo, T.F., Brandli, C., McFarland, E.W., J. Comb. Chem. 4, 563 (2002).CrossRefGoogle Scholar
23.Woodhouse, M., Herman, G.S., Parkinson, B.A., Chem. Mater. 17, 4318 (2005).CrossRefGoogle Scholar
24.Cong, P., Doolen, R.D., Fan, Q., Giaquinta, D.M., Guan, S., McFarland, E.W., Poojary, D., Self, K., Turner, H.W., Weinberg, W.H., Angew. Chem. Int. Ed. 38, 484 (1999).3.0.CO;2-#>CrossRefGoogle Scholar
25.Sirringhaus, H., Kawase, T., Friend, R.H., Shimoda, T., Inbasekaran, M., Wu, W., Woo, E.P., Science 290, 2123 (2000).CrossRefGoogle Scholar
26.MacBeath, G., Schreiber, S.L., Science 289, 1760 (2000).CrossRefGoogle Scholar
27.Woodhouse, M., Parkinson, B.A., Chem. Mater. 20, 2495 (2008).CrossRefGoogle Scholar
28.Parkinson, B., Energy Environ. Sci. 3, 509 (2010).CrossRefGoogle Scholar
30.Turner, J., Nat. Mater. 7, 770 (2008).CrossRefGoogle Scholar
31.Sambur, J.B., Novet, T., Parkinson, B.A., Science, 330, 63 (2010).CrossRefGoogle Scholar
Figure 0

Figure 1. (a) Photoelectrochemical cells with single bandgap and (b) dual bandgap absorber (tandem). Blue and red light are absorbed by the large bandgap (front) and small bandgap semiconductors (back), respectively. Eg, bandgap energy; TCO, transparent conductive oxide.

Figure 1

Figure 2. (a) Heterogeneous photocatalyst suspended in water. Each catalyst particle consists of a semiconductor material linked to a co-catalyst. The semiconductors absorb the light and carry out water oxidation, whereas the co-catalyst reduces protons. Charges are separated at the materials interface. ECB, conduction band energy level; EVB, valence band energy level. (b) Design for photocatalytic water splitting reactor. A polymer pipe is used to hold the photocatalyst suspension and to separate the H2 and O2 gas mixture by allowing selective H2 diffusion through the polymer walls. The photo-generated H2 then accumulates in the hydrogen tank. Oxygen gas is carried with the water flow and is removed in the oxygen tank. The H2/O2 gas mixture can be diluted with nitrogen to reduce the explosion risk.

Figure 2

Figure 3. Energy scheme for photocatalytic water splitting. In the single absorber case, a single photon must generate electron–hole-pairs at suitable potentials to both reduce and oxidize water. Kinetic barriers associated with the water redox reactions increase the required potentials above and below the thermodynamic ones (0.00 and 1.23 V at pH = 0). Since about one-third of the semiconductor bandgap energy is used for separating the electron–hole-pair, the minimum bandgap of the single absorber is about 2.00 eV. For the photoanode case, a lower bandgap can be used, but for water oxidation, the photo-generated electrons need to be extracted with an electrode or by using a chemical oxidant. The photocathode requires an electron source (electrode or reducing agent) to enable photocatalytic water reduction. In the tandem (or z-scheme) configuration, photoanode and photocathode are combined in series to split one molecule of water after absorbing four photons. This requires a directional redox shuttle or an external power source. E(H+/H2), E(H2O/O2), normal reduction potentials; A, electron acceptor; D, electron donor.

Figure 3

Figure 4. Conceptual design of photoelectrochemical water-splitting system with light concentration. The cylindrical pipes serve as light concentrators and gas collectors. H2 gas (green) is formed at the illuminated photoelectrode and O2 gas (red) at the counterelectrode. Ion transport between pipes is accomplished using porous membranes. Adapted with permission from Reference 30. ©2008, Macmillan Publishers.