Swarnava
Nandy
a,
Takashi
Hisatomi
ab,
Tsuyoshi
Takata
a,
Tohru
Setoyama
c and
Kazunari
Domen
*ade
aResearch Initiative for Supra-Materials (RISM), Interdisciplinary Cluster for Cutting Edge Research, Shinshu University, 4-17-1 Wakasato, Nagano 380-8553, Japan. E-mail: domen@shinshu-u.ac.jp
bPrecursory Research for Embryonic Science and Technology, Japan Science and Technology Agency, 4-17-1 Wakasato, Nagano-shi, Nagano 380-8553, Japan
cMitsubishi Chemical Group Science and Technology Research Center, 1000 Kamoshida, Aoba, Yokohama 227-8502, Japan
dOffice of University Professors, The University of Tokyo, 2-11-16 Yayoi, Tokyo 113-8656, Japan
eDepartment of Chemistry, Kyung Hee University, Seoul 130-701, Republic of Korea
First published on 14th September 2023
Solar hydrogen production by photocatalytic water splitting is studied to solve energy and environmental problems. It is estimated that practical implementation of this technology will require a photocatalytic water splitting system that is not only highly efficient in solar-to-hydrogen energy conversion but also cheap and scalable. Particulate photocatalyst sheets based on immobilized particulate semiconductors are a promising approach to meet these requirements owing to their scalability without sacrificing their intrinsic water splitting activity. Nevertheless, existing sheet systems have not reached the targeted solar-to-hydrogen energy conversion efficiency yet. This is because the quality of narrow-bandgap photocatalyst materials has not been sufficiently improved, and also because methods for activating such photocatalysts in warm water under ambient pressure, which is assumed to be a practical outdoor operating condition, while suppressing reverse reactions have not been sufficiently developed. This perspective describes recent advancements in photocatalyst sheets and panel reactor systems intended for practical implementation of solar hydrogen production via the overall water splitting reaction, and discusses issues regarding the development of photocatalytic systems that can produce solar hydrogen with satisfactory performance.
In this article, we discuss advancements in the development of photocatalytic materials and their processing into particulate photocatalyst sheets for the OWS reaction. The problem of reverse reactions that would occur in the photocatalytic OWS reaction under atmospheric pressure, which is assumed in practical large-scale applications, is discussed. In relation to practicability, an estimate of the allowable cost for a system that produces solar hydrogen at a certain price by photocatalytic OWS is also given. Directions for design and development of particulate photocatalyst sheets that may lead to the achievement the target STH efficiency are then suggested.
The one-step excitation system is simple and can be driven by a photocatalyst sheet with photocatalytic particles immobilized on a substrate (Fig. 2A).6 To drive the reaction, however, it is important to facilitate the penetration of water into the particle layer and the detachment of products from it. When a photocatalyst sheet is used in ZOWS, HEPs and OEPs are well mixed and immobilized with conductive materials in close proximity to each other. Such a structure can allow efficient charge transfer between HEPs and OEPs while suppressing the solution resistance and H+/OH− concentration overpotentials, which are often issues in (photo)electrochemical systems having spatially separated hydrogen- and oxygen-evolving electrodes.9 Therefore, in principle, photocatalyst sheets can be scaled up without losing their inherent activity. In photocatalyst sheets, p-type and n-type semiconductors are commonly employed as the HEP and OEP, respectively, to achieve ZOWS efficiently, because photoexcited charge carrier migration in the photocatalyst sheet resembles that in photoelectrochemical cells based on a short-circuited photocathode and photoanode, with the HEP and OEP corresponding to the photocathode and photoanode, respectively. The working potential for the sheet is estimated from the intersection of the current–potential (i–E) curves for the photoanode and photocathode. As such, the performance of particulate photocatalysts as the photoelectrode is crucial in determining their utility in a photocatalyst sheet system.
Fig. 2 (A) Schematic diagram of one-step photoexcitation based photocatalyst sheet, (B) 100 m2-scale photocatalyst panel reactor: (a) photograph of 625 cm2 panel reactor unit, (b) schematic side view of panel reactor unit, and (c) top view of 100 m2 solar hydrogen production system consisting of 1600 panel reactor units. Reproduced from ref. 16 with permission from Springer Nature, copyright 2021. |
The allowable system and process cost for photocatalytic water splitting has been estimated to be approximately 100 USD m−2 given a STH efficiency of 10%, a hydrogen price of 3.5 USD kg−1, an oxygen price of 0.1 USD kg−1, a lifetime of 10 years, and an annual depreciation rate of 4%. The STH efficiency depends on both the wavelength of the light used by photocatalysts in the OWS reaction and the apparent quantum yield (AQY).1 Considering a constant AQY of unity, the absorption edge wavelength for the photocatalyst material must be longer than 526 nm, because below this wavelength there are too few photons to achieve the STH efficiency target of 10%. This STH efficiency requires an OWS system with an AQY of 60% in response to visible light up to 600 nm. Note that the hydrogen price assumed above is higher than the target cost. Of course, further reductions in costs, improvements to STH efficiency, and extension of the system service life are desirable. When comparing suspension and sheet systems, it appears that the sheet system is technically less difficult and costly to build and operate than the suspension system. Considering the lack of large-scale and long-term experimental demonstrations for the latter. In terms of lifespan, stirring causes long-term mechanical damage to the powder photocatalysts in the suspension system, as demonstrated with a Rh2−yCryO3/GaN:ZnO system.11 The sheet system also has an advantage that it does not require stirring because the photocatalysts are immobilised, but the influence of mass transport is still negligible.
As an alternative technology for solar hydrogen production from water, photovoltaic-assisted electrolysis (PV-E) systems may be considered. PV-E systems can reach STH efficiencies of 30% on a laboratory scale. However, extending these systems to larger scales is expensive due to high capital and balance-of-system expenses.12 It has been estimated that the balance-of-system expense alone would reach US$100 m−2 in PV-E systems.13 which highlights the need for radical innovations in system construction and operation.
The 100 m2-scale arrayed photocatalyst panel reactor split water for a period of eight months under outdoor conditions (Fig. 2B). In other trials using a small panel reactor, 80% of the peak activity was maintained after 1600 h of constant irradiation by simulated sunlight. However, the STH efficiency of the outdoor panel reactor decreased irreversibly during the winter months, because the layer of SrTiO3:Al particles peeled away from the support (due to repeated freezing and melting of water) and particles that settled at the bottom failed to absorb sunlight effectively. Thus, it is necessary to improve the chemical and mechanical stability of the panel reactors to extend their usage timescale.
The STH efficiency achieved with the above panel reactor based on SrTiO3:Al sheets was at most 0.65% because the visible part of the spectrum was not utilized. Even if UV light at wavelengths up to 400 nm was utilized for OWS at an AQY of unity, the STH efficiency would be only 1.3%. Therefore, it is essential to develop photocatalyst sheets with visible–light activity. A solid solution of GaN and ZnO (denoted as GaN:ZnO) loaded with a RhCrOx cocatalyst exhibited a maximum AQY of 5.1% at 410 nm in the OWS reaction and maintained this activity for three months.17 The RhCrOx-loaded GaN:ZnO has been processed into photocatalyst sheets,18 which exhibited an OWS activity comparable to that for a suspension when hydrophilic silica particles with appropriate sizes were incorporated into the particle layer, whereas a sheet made solely from cocatalyst-loaded GaN:ZnO exhibited lower activity. This is probably because the inclusion of such silica particles promoted the permeation of water into the photocatalyst particle layer and the release of product gases from the sheet. However, there is little scientific understanding of this, and further research is needed to clarify the extent to which the hydrophilicity of the sheet affects the performance. Recently, there have been some reports on methods for improving the photocatalytic properties of GaN:ZnO. For instance, deposition of Al2O3 on Rh-loaded GaN:ZnO by atomic layer deposition greatly suppressed the water-forming backward reaction without blocking the active sites, thus improving the AQY from 0.3% to 7.1% at 420 nm in OWS.19 Moreover, highly crystalline GaN:ZnO with a narrow bandgap energy of 2.3 eV was recently synthesized using an ammonium salt as a nitriding reagent in a sealed evacuated tube.20 This method prevented loss of ZnO during nitridation of the starting materials to form GaN:ZnO. Some non-oxide photocatalysts with bandgap energy smaller than 3.0 eV, such as Y2Ti2S2O7, SrTaO2N and TaON having a bandgap energy of 1.9, 2.1 and 2.5 eV, respectively, are active and stable in the OWS reaction via one-step photoexcitation.21–23 Such photocatalysts are expected to be applied to photocatalyst sheets for OWS given that the activity is significantly improved.
Fig. 3 Band diagrams for SrTiO3:La,Rh/C/BiVO4:Mo sheet: (a) before contact, (b) under darkness after contact, and (c) under illumination. Reproduced from ref. 28 with permission from American Chemical Society, copyright 2017. |
For practical large-scale application, it is essential to avoid the use of costly particle transfer methods that require vacuum processes and to simplify the overall manufacturing process. The Z-schematic photocatalyst sheet was also fabricated by screen printing, which does not require vacuum processes as in particle transfer, using transparent indium-doped tin oxide nanoparticles (np-ITO) as a mediator.29 The STH achieved with np-ITO was 0.4% at near ambient pressure. However, further development of cheaper conductive materials and simpler manufacturing processes is desirable.
Because the absorption edge wavelengths of SrTiO3:Rh,La and BiVO4:Mo are relatively short, attempts have been made to replace these materials with narrow bandgap photocatalysts in the sheet system. Table 1 summarizes the OWS performance of particulate photocatalyst sheets employing various oxide and non-oxide semiconductors along with their detailed measurement conditions. Non-oxide photocatalysts with a longer absorption edge than SrTiO3:Rh,La have been applied as the HEP for sheet systems.30,31 In particular, La5Ti2Cu0.9Ag0.1O7S5 (LTCA) is a unique oxysulfide photocatalyst exhibiting a positive onset potential (+0.9 V vs. RHE) when used as a photocathode for photoelectrochemical hydrogen evolution.32 Cationic doping with lower-valent species at Ti4+ sites in LTCA can induce p-type semiconducting characteristics due to a positive shift of the Fermi level, thus enhancing the photocathodic current. These features make LTCA very useful as a HEP for photocatalytic sheet systems. Other narrow bandgap materials such as LaMg1/3Ta2/3O2N, and (ZnSe)0.5(CuGa2.5Se4.25)0.5 have also been investigated in sheet form as HEP in combination with BiVO4:Mo as OEP.30,33 However, the performance of LaMg1/3Ta2/3O2N in sheet form was limited due to the n-type conductivity, while most chalcogenides were not suitable for sheet application due to the negative photocurrent onset potential when evaluated as a photocathode.
Entry | Cocatalyst/HEP (absorption edge) | Cocatalyst/OEP (absorption edge) | Mediator | AQY (wavelength/nm) | STH (pressure, temperature) | Ref. |
---|---|---|---|---|---|---|
a n.r.: not reported; BiVO4:Mo synthesis route: (s–l): solid–liquid reaction; (h): hydrothermal; reaction solution pH: without adjustment as that of pure water except for entry 8 where pH was adjusted to 11. | ||||||
1 | Cr2O3/Ru/SrTiO3:Rh,La (520 nm) | BiVO4:Mo (s–l) (520 nm) | Au | 33% (419 nm) | 1.1% (10 kPa, 331 K) | 27 |
2 | Cr2O3/Ru/SrTiO3:Rh,La (520 nm) | BiVO4:Mo (s–l) (520 nm) | C | 26% (419 nm) | 1.2% (10 kPa, 331 K) | 28 |
3 | Cr2O3/Ru/SrTiO3:Rh,La (520 nm) | BiVO4:Mo (s–l) (520 nm) | C | 19% (419 nm) | 1.0% (91 kPa, 331 K) | 28 |
4 | Cr2O3/Ru/SrTiO3:Rh,La (520 nm) | BiVO4:Mo (s–l) (520 nm) | np-ITO | 10.2% (420 nm) | 0.4% (91 kPa, 333 K) | 29 |
5 | Cr2O3/Ru/SrTiO3:Rh,La (520 nm) | BiVO4:Mo (s–l) (520 nm) | Sputter-ITO | n.r. | 0.8% (91 kPa, 333 K) | 29 |
6 | Pt/TiO2-CdS-(ZnSe)0.5(CuGa2.5Se4.25)0.5 (725 nm) | BiVO4:Mo (s–l) (520 nm) | Au | 1.5% (420 nm) | n.r. | 30 |
7 | RhCrOx/LaMg1/3Ta2/3O2N (600 nm) | BiVO4:Mo (s–l) (520 nm) | Au and RGO | 0.25% (418 nm) | 0.0035% | 33 |
8 | Cr2O3/Rh/LTCA:Ga (700 nm) | CoOx/LaTiO2N (600 nm) | Au | 0.04% (420 nm) | n.r. | 38 |
9 | Cr2O3/Rh/LTCA:Ga (700 nm) | CoOx/BiVO4:Mo (s–l) (520 nm) | Au | 11.8% (420 nm) | 0.4% (4 kPa, 301 K) | 31 |
10 | Cr2O3/Rh/LTCA:Mg,Al (700 nm) | CoOx/BiVO4:Mo(h) (520 nm) | Au | 16.3% (420 nm) | 0.67% (4 kPa, 301 K) | 34 |
11 | SiO2/Cr2O3/Rh/LTCA:Mg,Al (700 nm) | SiO2/CoOx/BiVO4:Mo(h) (520 nm) | Au | 9.7% (420 nm) | 0.41% (90 kPa, 333 K) | 34 |
Photocatalyst sheets composed of Mg,Al-doped LTCA (LTCA:Mg,Al) as the HEP and BiVO4:Mo as the OEP achieved an AQY of 16.3% (420 nm) and a STH efficiency of 0.67% under reduced pressure upon depositing a CoOx/Cr2O3/Rh cocatalyst.34 A schematic of the LTCA:Mg,Al/Au/BiVO4:Mo sheet fabrication procedure is presented in Fig. 4. Photocatalyst sheets made of short-circuited LTCA:Mg,Al/Au photocathode and BiVO4:Mo/Ti photoanode placed side by side, which serve as the HEP and OEP, respectively, exhibits lower ZOWS activity due to the solution resistance and the pH gradient. Similar phenomena were also observed in the SrTiO3:Rh,La and BiVO4:Mo systems earlier.6,28 The ZOWS activity dropped steeply with increasing Ar background pressure for both mixed and parallel types of photocatalyst sheets. This is attributed to backward ORR occurring on the bare surface of the LTCA particles and the Au layer, which was verified by investigating the (photo)electrochemical ORR activity of the relevant samples with various surface modifications (Fig. 5A). Importantly, the oxysulfide surface was not covered with a photodeposited Cr2O3 layer, which acts to suppress the ORR, while the Rh cocatalyst surface was covered. Therefore, it is essential to coat the oxysulfide surface with a material that can suppress the ORR while preserving the hydrogen evolution reaction.
Fig. 4 (A) Schematic illustration of the preparation procedure for photocatalyst sheet composed of LTCA:Mg,Al and BiVO4:Mo. (B) Photograph of 3 × 3 cm2 LTCA:Mg,Al/Au/BiVO4:Mo photocatalyst sheet (a) before and (b) after particle transfer. Panel (A) was reproduced from ref. 34 with permission from Elsevier Inc., copyright 2023. |
Fig. 5 (A) Oxygen reduction current density for (a) Au/Ti, (b) LTCA:Mg,Al/Au, (c) Rh/LTCA:Mg,Al/Au, (d) Cr2O3/Rh/LTCA:Mg,Al/Au, (e) TiO2/Cr2O3/Rh/LTCA:Mg,Al/Au and (f) SiO2/Cr2O3/Rh/LTCA:Mg,Al/Au photoelectrodes. (B) Temperature (T) dependence of ZOWS activity and STH efficiency for SiO2-modified LTCA:Mg,Al/Au/BiVO4:Mo photocatalyst sheet at atmospheric pressure under simulated sunlight. Reproduced from ref. 34 with permission from Elsevier Inc., copyright 2023. |
A CoOx/Cr2O3/Rh-modified LTCA:Mg,Al/Au/BiVO4:Mo photocatalyst sheet coated with an amorphous SiO2 layer 5–8 nm in thickness was found to suppress the ORR and to largely maintain the ZOWS activity at elevated pressures and temperatures. The resulting SiO2-coated sheet yielded a STH efficiency of 0.41% at a pressure of 90 kPa and a temperature of 333 K (Fig. 5B). In contrast, a photocatalyst sheet coated with an amorphous TiO2 layer, which is also known to suppress the ORR, did not operate at temperatures above 318 K owing to condensation restricting mass transport across the TiO2 layer. These results show the applicability of non-oxide photocatalysts that are prone to backward reactions under field conditions when appropriate surface modifications are applied. Note that some non-oxide photocatalysts modified with unprotected noble metal cocatalysts have already been reported to achieve STH efficiencies exceeding 1% in ZOWS in the form of a suspension.35,36 Although the applicability of such systems in the form of photocatalyst sheets is interesting, in our experience, such systems will inevitably lose their activity at ambient pressure due to backward reactions. For practical use, it is essential to measure the pressure dependence of ZOWS activity.
Thermodynamically, the LTCA:Mg,Al/Au/BiVO4:Mo system could yield a STH efficiency of approximately 9%, while the presently-achieved efficiency is at most 0.67%. The ZOWS activity could be further improved by refining the synthesis and modification methods for the HEP and OEP. Li and co-workers invented the use of hydrothermally-synthesized BiVO4 exposing anisotropic facets that collect electrons and holes, respectively, under photoexcitation as an OEP.37 The BiVO4 modified with Ir-CoFeOx cocatalysts yielded a STH of 0.6% when combined with ZrO2-modified TaON as the HEP in an aqueous K4Fe(CN)6 solution, which was the highest reported value using suspension systems. The use of such hydrothermally-synthesized BiVO4 was shown to improve the STH efficiency of the LTCA:Mg,Al/Au/BiVO4:Mo sheet system compare to the one using BiVO4:Mo synthesized by solid–liquid reaction, as was demonstrated in our recent work.34
There is also interest in replacing BiVO4 with non-oxide photocatalysts with a narrower bandgap to extend the wavelength range of light available for ZOWS and expand the types of photocatalysts that can be applied as OEPs. A photocatalyst sheet based on Ga-doped LTCA (LTCA:Ga) and LaTiO2N embedded onto Au layer was investigated, but the resultant LTCA:Ga/Au/LaTiO2N sheet exhibited negligible ZOWS activity.38 The Schottky junction at the interface between LTON and Au obviously suppressed the injection of electrons from the OEP to the Au. However, deposition of CoOx onto the LaTiO2N was found to weaken the Schottky barrier and promoted electron injection from LaTiO2N to Au, allowing ZOWS to occur, although the AQY was estimated to be only about 0.04% at 420 nm. It is noteworthy that in a recent study, narrow-bandgap GaN:ZnO synthesized in a sealed evacuated tube and loaded with IrO2 (IrO2/GaN:ZnO) exhibited a relatively negative photoanodic current onset (+0.3 V vs. RHE) compared to CoOx/LaTiO2N (+0.75 V vs. RHE) when studied as a photoanode for photoelectrochemical oxygen evolution.20 Therefore, IrO2/GaN:ZnO would be an interesting candidate of the OEP to replace CoOx/BiVO4:Mo and CoOx/LaTiO2N in the photocatalyst sheet, which may allow to improve the ZOWS performance.
Overall, the systems based on narrow bandgap non-oxide materials have demonstrated lower STH efficiencies at atmospheric pressure than those based on metal oxides, despite the superior light absorption ability of the former. This is due the weaker driving force for forward reactions and susceptibility to backward reactions. Activation and stabilization of narrow bandgap photocatalysts are essential to enable commercialization of photocatalytic solar hydrogen production processes, particularly under outdoor operating conditions. To advance the development of narrow-bandgap OEPs, it is important to precisely control the energy states at the interface between the photocatalyst and the cocatalyst, conductive material, or reaction solution so as to allow facile charge separation and transfer. To this end, development of technologies for tracking the migration of carriers under the reaction environment is important.
In particulate photocatalyst sheet systems, water splitting performance can be significantly affected by backward reactions and mass transfer of reactants and products. The release of gas bubbles can be a significant concern when OWS is conducted under elevated background pressure, because it would increase the bubble residing time at the sheet surface and thus the opportunity for reverse reaction. Therefore, the identification of active sites and mechanisms for desired and undesired reaction pathways and the understanding of the associated transport phenomena are of particular importance. In the experimental observation, hydrogen and oxygen are probably generated in the narrow cavities between the photocatalyst particles during the water splitting reaction and eventually form submillimetre-sized gas bubbles of oxyhydrogen on the surface of the sheet.16 However, there are still many unsolved phenomena regarding the physical existence of reactant and product molecules. It will be desirable to clarify the mass transport of chemical species and the nucleation/growth of gas bubbles from a chemical engineering and hydrodynamic point of view, taking into account the actual structural and physical properties of the particle layer of photocatalyst sheets. This will enhance the introduction of the reactant (water) and the release of products (hydrogen and oxygen), thereby reducing the probability of reverse reactions under elevated pressure. In addition, visualisation of reduction and oxidation sites on photocatalyst particles has been reported using scanning electrochemical microscopy and single-molecule fluorescence spectroscopy in conjunction with probe molecules.39,40 Such spatially-resolved analytical techniques will be useful in identifying the active sites for backward reactions. Given the insufficient STH efficiencies achieved to date, improvements in charge separation and charge injection within individual photocatalyst particles and composite sheets are still essential. For example, surface photovoltage spectroscopy has been used to determine the facets of photocatalyst particles on which e− and h+ preferentially migrate.41,42 In addition, transient absorption spectroscopy has been used to elucidate carrier dynamics.30 These techniques are expected to be useful in comprehending the timeframe of reactions and the distribution of reaction sites on photocatalytic sheets. Apart from the development of photocatalytic materials and reactors with adequate performance, chemical processes should be carefully designed to balance STH efficiency, cost, and safe operation of renewable hydrogen production systems.
We consider that particulate photocatalyst sheets are promising because they can exhibit OWS activity under such practical conditions with appropriate surface modifications. The technological immaturity of this system offers considerable room for innovation. The authors hope that this contribution will stimulate researchers from diverse fields to collaborate on technical advancements to produce sustainable hydrogen for human society.
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