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. 2018 May 23;118(10):5201-5241.
doi: 10.1021/acs.chemrev.7b00286. Epub 2018 Apr 20.

Mimicking Natural Photosynthesis: Solar to Renewable H2 Fuel Synthesis by Z-Scheme Water Splitting Systems

Affiliations

Mimicking Natural Photosynthesis: Solar to Renewable H2 Fuel Synthesis by Z-Scheme Water Splitting Systems

Yiou Wang et al. Chem Rev. .

Abstract

Visible light-driven water splitting using cheap and robust photocatalysts is one of the most exciting ways to produce clean and renewable energy for future generations. Cutting edge research within the field focuses on so-called "Z-scheme" systems, which are inspired by the photosystem II-photosystem I (PSII/PSI) coupling from natural photosynthesis. A Z-scheme system comprises two photocatalysts and generates two sets of charge carriers, splitting water into its constituent parts, hydrogen and oxygen, at separate locations. This is not only more efficient than using a single photocatalyst, but practically it could also be safer. Researchers within the field are constantly aiming to bring systems toward industrial level efficiencies by maximizing light absorption of the materials, engineering more stable redox couples, and also searching for new hydrogen and oxygen evolution cocatalysts. This review provides an in-depth survey of relevant Z-schemes from past to present, with particular focus on mechanistic breakthroughs, and highlights current state of the art systems which are at the forefront of the field.

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Conflict of interest statement

The authors declare no competing financial interest.

Figures

Scheme 1
Scheme 1. A Typical Model of a Single Photocatalyst System for Water Splitting
Scheme 2
Scheme 2. A Schematic Diagram of a Double Excitation Process on P680 and P700 in Natural Photosynthesis
Scheme 3
Scheme 3. A Double Excitation System Based on a HEP and an OEP with a Shuttle of Ox, oxidant, and Red, reductant, molecules
Two dotted curves indicate the back reactions which should be suppressed.
Figure 1
Figure 1
Band edge positions of typical semiconductors for visible driven water splitting.
Figure 2
Figure 2
Speculated reaction mechanism using IO3/I redox mediator (pH = 7). Reprinted with permission from ref (37). Copyright 2002 Elsevier.
Figure 3
Figure 3
(I) Photocatalytic O2 evolution from aqueous AgNO3 solutions (0.05 mol/L, 320 mL) under visible light irradiation (λ > 420 nm) on (a) BiVO4 (s–t) and (b) BiVO4 (s–m). (II) The working diagram of Z-scheme water splitting based on BiVO4. Reprinted with permission from refs (44) and (36). Copyright 2001 American Chemical Society and 2004 The Chemical Society of Japan.
Figure 4
Figure 4
(I) Schematic band structures of a metal oxide (NaTaO3) and metal (oxy)nitride (BaTaO2N). (II) The working diagram of Z-scheme water splitting based on TaON. Reproduced with permission from refs (5) and (48). Copyright 2007 American Chemical Society and 2008 The Chemical Society of Japan.
Figure 5
Figure 5
(I) (a) Diffuse reflectance spectra of H2WO4 and WO3. (b) Rates of O2 evolution over H2WO4 and WO3 in Fe(ClO4)3 aqueous solution (5 mM, pH 2.3) under visible light irradiation (Xe lamp, cut off filter: L-42, Y-44, Y-46, Y-48 ,Y-50, O-52). (II) The working diagram of Z-scheme water splitting based on H2WO4. Reproduced with permission from ref (55). Copyright 2017 The Royal Society of Chemistry.
Figure 6
Figure 6
(I) Crystal structure of (a) Sillén–Aurivillius oxychloride Bi4NbO8Cl and (b) its related intergrowth compound Bi6NbWO14Cl proposed by Aurivillius. (II) Time course of Z-scheme water splitting coupled with Ru/SrTiO3:Rh photocatalyst via Fe3+/Fe2+ redox mediator. (III) The working diagram of Z-scheme water splitting based on Bi4NbO8Cl. Reproduced with permission from ref (56). Copyright 2016 American Chemical Society.
Figure 7
Figure 7
Proposed band structure and visible light response of Rh-doped SrTiO3 photocatalyst. Reproduced with permission from ref (16). Copyright 2004 American Chemical Society.
Figure 8
Figure 8
(I) UV–vis diffuse reflectace (DR) spectra of ATaO2N (A = Ca, Sr, Ba), TaON, Ta3N5, and WO3. (II) The working diagram of Z-scheme water splitting based on ATaO2N. Reproduced with permission from refs (11) and (60). Copyright 2011 The Chemical Society of Japan and 2008 Elsevier.
Figure 9
Figure 9
(I) Molecular structures of dyes. (II) The working diagram of Z-scheme water splitting based on dye-adsorbed Pt/H4Nb6O17 and IrO2–Pt/WO3. Reproduced with permission from ref (62). Copyright 2013 American Chemical Society.
Figure 10
Figure 10
Time courses of photocatalytic evolution of H2 (closed) and O2 (open) using a mixture of dye-adsorbed [(a) NKX-2311 and NKX-2587, (b) NKX-2677 and NKX-2697, and (c) MK-1 and MK-2] Pt/H4Nb6O17 (50 mg) and IrO2–Pt/WO3 (100 mg) suspended in 5 mM KI aqueous solution (pH ∼ 4.5, without adjustment) under visible light. Arrows indicate evacuation of gas phase. Reproduced with permission from ref (62). Copyright 2013 American Chemical Society.
Figure 11
Figure 11
(I) (a) Crystal structure and optical properties of graphitic carbon nitride. Schematic diagram of a perfect graphitic carbon nitride sheet constructed from melem units. (b) Experimental XRD pattern of the polymeric carbon nitride, revealing a graphitic structure with an interplanar stacking distance of aromatic units of 0.326 nm. (c) Ultraviolet–visible diffuse reflectance spectrum of the polymeric carbon nitride. Inset: Photograph of the photocatalyst. (II) The working diagram of Z-scheme water splitting based on g-C3N4. Reproduced with permission from refs (63) and (35). Copyright 2009 Macmillan Publishers Limited and 2014 American Chemical Society.
Figure 12
Figure 12
Mechanism of water splitting in a Z-scheme photocatalyst system consisting of Ru/SrTiO3:Rh and BiVO4 under visible-light irradiation using RGO as a mediator. Reproduced with permission from ref (99). Copyright 2011 American Chemical Society.
Figure 13
Figure 13
(a) Illustration of the preparation of the SrTiO3:La,Rh/Au/BiVO4:Mo sheet by the particle transfer method, and (b) schematic of overall water splitting on the Ru-modified SrTiO3:La,Rh/Au/BiVO4:Mo sheet. Reproduced with permission from ref (98). Copyright 2016 Macmillan Publishers Limited.
Figure 14
Figure 14
(a) Photograph of the ink used for screen printing the photocatalyst sheet. (b) Photograph of a 10 cm × 10 cm SrTiO3:La,Rh/Au nanoparticle/BiVO4:Mo printed sheet. (c) Time course of the water splitting reaction using a Ru-modified SrTiO3:La,Rh/Au colloid (40 wt %)/BiVO4:Mo printed sheet under simulated sunlight at 288 and 5 KPa. The sample (6.25 cm2) was photodeposited with RuCl3·3H2O (0.17 μmol). Reproduced with permission from ref (98). Copyright 2016 Macmillan Publishers Limited.
Figure 15
Figure 15
Squares (□), circles (○), and triangles (△) stand for Ru-loaded SrTiO3:La,Rh/C/BiVO4:Mo, Cr2O3/Ru-loaded SrTiO3:La,Rh/C/BiVO4:Mo, and a-TiO2/Cr2O3/Ru-loaded SrTiO3:La,Rh/Au/BiVO4:Mo, respectively. Closed and open symbols represent hydrogen and oxygen, respectively. Photodeposition from RuCl3·3H2O (0.2 μmol), K2CrO4 (0.2 μmol), Ti peroxide (1.3 μmol), and the overall water-splitting reaction were carried out under Xe lamp (300 W) illumination (λ > 420 nm) at 288 K. The area of the photocatalyst sheets was 7.5 cm2. Reproduced with permission from ref (107). Copyright 2017 American Chemical Society.
Figure 16
Figure 16
Scheme of photocatalytic water splitting. Reproduced with permission from ref (96). Copyright 2011 Cambridge University Press.
Figure 17
Figure 17
Forward and backward reactions in Z-scheme water splitting (potentials at pH 7).
Figure 18
Figure 18
Absorption spectra of aqueous solutions containing I, IO3, or I3 (precursors: KI, KIO3, or I2, without pH adjustment).
Figure 19
Figure 19
Time courses of the hydrogen evolution (squares) and the conversion of iodide ion into triiodide ions (circles) as the result of the photocatalytic reactions using the Pt-loaded TiO2 (TIO-5) particles. The reaction was carried out in the cell containing the photocatalyst (200 mg) and 1.0 mol dm–3 aqueous solution of potassium iodide (50 mL) at pH 2.4. Reproduced with permission from ref (114). Copyright 1996 The Chemical Society of Japan.
Figure 20
Figure 20
pH dependence of the initial rate of the photocatalytic reaction using Pt-loaded TiO2 (Kanto Chemicals) particles as the photocatalyst. The reaction rates were determined from the amounts of triiodide ions generated during the photoirradiation for 1 h. The photocatalyst was heat-treated at 500 °C for 1 h. Reproduced with permission from ref (114). Copyright 1996 The Chemical Society of Japan.
Figure 21
Figure 21
Time course of photocatalytic evolution of H2 using Pt(0.5 wt %)TiO2 (anatase, Ishihara ST-01) photocatalyst suspended in 0.1 M of NaI aqueous solution under UV light irradiation (λ > 300 nm, 400 W Hg lamp). Reproduced with permission from ref (11). Copyright 2011 The Chemical Society of Japan.
Figure 22
Figure 22
Time course of photocatalytic O2 evolution over TiO2 photocatalysts suspended in aqueous solution (400 mL, pH 11 adjusted by NaOH) containing (a)1 mmol of NaIO3 and (b) 1 mmol of NaIO3 and 16 mmol of NaI. Reproduced with permission from ref (11). Copyright 2011 The Chemical Society of Japan.
Figure 23
Figure 23
Adsorption properties of iodate (IO3) and iodide (I) anions on various TiO2 powders. Reproduced with permission from ref (11). Copyright 2011 The Chemical Society of Japan.
Figure 24
Figure 24
Time course of photocatalytic O2 evolution over Pt (0.5 wt %)/WO3 and Pt (0.5 wt %)/BiVO4 (inset) suspended in aqueous solution (250 mL, pH 6.5 without adjustment) containing (a) 0.25 mmol of NaIO3 and (b) 0.25 mmol of NaIO3 and 10 mmol of NaI. Reproduced with permission from ref (11). Copyright 2011 The Chemical Society of Japan.
Figure 25
Figure 25
(a) Dependence of rates of gas evolution over a mixture of Pt-TiO2-A1 and bare TiO2-R2 photocatalysts upon the pH value of NaI solution (NaI: 0.1 M). (b) Dependence of rates of gas evolution over a mixture of Pt-TiO2-A1 and bare TiO2-R2 photocatalysts upon the concentration of NaI aqueous solution (pH 11). Reproduced with permission from ref (11). Copyright 2011 The Chemical Society of Japan.
Figure 26
Figure 26
Time course of photocatalytic evolution of H2 and O2 using a mixture of Pt (0.3 wt %)/SrTiO3 (Cr, Ta 4 mol % doped) and Pt (0.5 wt %)/WO3 photocatalysts suspended in 5 mM of NaI aqueous solution (pH 6.5 without adjustment) under visible light irradiation (λ > 420 nm). Triangles indicate H2 evolution using Pt/SrTiO3:Cr/Ta alone. Reproduced with permission from ref (11). Copyright 2011 The Chemical Society of Japan.
Figure 27
Figure 27
Absorption spectra of aqueous solutions containing Fe cation (precursor, FeCl3·6H2O or FeCl2·4H2O, pH 2.1, adjusted by HCl).
Figure 28
Figure 28
Initial rate of oxygen production as a function of the Fe3+ (open circles) and WO3 (closed circles). All solutions were in 0.5 × 10–2 mol dm–3 H2SO4 for the variation of [Fe3+], 7.5 mg cm–3 of WO3 was used, and for the variation in [WO3], 10–2 mol dm–3 of Fe3+ was present. Reproduced with permission from ref (119). Copyright 1982 The Royal Society of Chemistry.
Figure 29
Figure 29
Effect of Fe2+ concentration on the initial rate of oxygen formation over WO3 photocatalyst. Reproduced with permission from ref (119). Copyright 1982 The Royal Society of Chemistry.
Figure 30
Figure 30
Adsorption isotherms of Fe3+ and Fe2+ ions on TiO2 powder at 25 °C: for Fe3+ ions (open circles) and for Fe2+ ions (open squares). When both Fe2+ and Fe3+ ions were added to the solution, their adsorptivity was affected each other: for Fe3+ ions (closed circles) and for Fe2+ ions (closed squares). The molar ratio of Fe3+ ions: Fe2+ ions are described in the figure. Measurements were performed using TiO2 (JCR TIO-5) powder. Reproduced with permission and addition of the correction in the horizontal axis from ref (122). Copyright 1997 American Chemical Society.
Figure 31
Figure 31
Presumed reaction mechanism of the photocatalytic decomposition of water using the Fe3+/Fe2+ redox system. Reproduced with permission from ref (19). Copyright 1997 Elsevier.
Figure 32
Figure 32
Alternative evolution of H2 and O2 gases using a RuO2–WO3 catalyst and Fe3+/Fe2+ redox system. Run 1: mixture of FeSO4 (1 mmol) and H2SO4 (10 mmol) and distilled water (350 mL) was irradiated through a quartz glass filter (λ > 200 nm). Run 2: RuO2(1 wt %)–WO3 catalyst (1 g) was added to the solution after run 1 and light was irradiated through a Pyrex glass filter (λ > 300 nm). Run 3: catalyst powder was filtered from the solution (or sedimented by stop stirring) after run 2, and then the solution was irradiated again through a quartz glass filter (λ > 200 nm). Run 4: same as run 2. Reproduced with permission from ref (19). Copyright 1997 Elsevier.
Figure 33
Figure 33
(a) Schematics of the photocatalytic reaction cell for splitting water and (b) energy diagram of splitting water by combined photocatalytic reactions. Reproduced with permission from ref (124). Copyright 1969 The Royal Society of Chemistry.
Figure 34
Figure 34
Photocatalytic overall water splitting using (Pt (0.5 wt %)/SrTiO3:Rh (1%)–(BiVO4) system under visible light irradiation in an aqueous solution of (a) FeCl3 (2 mmol L–1) and (b) FeCl2 (2 mmol L–1). Open marks, H2; closed marks, O2. Catalyst, 0.1 g for each component; reactant solution, 120 mL, pH 2.4; light source, 300 W Xe-arc lamp with a cutoff filter (λ > 420 nm); cell, top irradiation cell with a Pyrex window. Reproduced with permission from ref (126). Copyright 2007 The Chemical Society of Japan.
Figure 35
Figure 35
Suppression of backward reactions by Fe3+ ions. Reproduced with permission from ref (126). Copyright 2007 The Chemical Society of Japan.
Figure 36
Figure 36
Photocatalytic O2 evolution on the BiVO4 photocatalyst under visible light irradiation in 2 mmol L–1 aqueous FeCl3 solutions with (a) 0, (b) 1, (c) 2, and (d) 5 mmol L–1 of FeCl2. Catalyst, 0.1 g; reactant solution, 120 mL, pH 2.4; light source, 300 W Xe-arc lamp with a cutoff filter (λ > 420 nm); cell, top-irradiation cell with a Pyrex window. Reproduced with permission from ref (126). Copyright 2007 The Chemical Society of Japan.
Figure 37
Figure 37
Overall water splitting by a (Ru/SrTiO3:Rh)–(BiVO4)–([Co(bpy)3]3+/2+) system under visible light irradiation. Reaction conditions: catalyst, 0.1 g each; starting reactant solution, 120 mL of an aqueous [Co(bpy)3]SO4 solution (0.5 mmol L–1, initial pH 3.8); light source, a 300 W Xe-arc lamp with a cutoff filter (λ > 420 nm); cell, top-irradiation type. SrTiO3:Rh powder was prepared by calcination at 1373 K with Sr 3% excess. Reproduced with permission from ref (92). Copyright 2013 American Chemical Society.
Figure 38
Figure 38
Energy diagrams of the Z-scheme photocatalyst system, (Ru/SrTiO3:Rh)–(BiVO4)–([Co(bpy)3]3+/2+), and the ratio of [Co(bpy)3]2+ ions to [Co(bpy)3]3+ ions during overall water splitting under basic, neutral, and acidic conditions. Reproduced with permission from ref (92). Copyright 2013 American Chemical Society.
Figure 39
Figure 39
(a) Two-compartment-reactor for H2 evolution separated from O2 evolution. (b) H2 evolution separated from O2 evolution for overall water splitting by a (Ru/SrTiO3:Rh)–(BiVO4)–([Co(bpy)3]3+/2+) system. Catalyst, 0.1 g (Ru/SrTiO3:Rh), 0.3 g (BiVO4); starting reactant solution, 0.5 mmol L–1 of an aqueous [Co(bpy)3]SO4 solution, 300 mL; initial pH adjusted to 3.8; light source, two 300 W Xe-arc lamps with cutoff filters (λ > 420 nm). SrTiO3:Rh powder was prepared by calcination at 1373 K with Sr 3% excess. Open and close marks indicate H2 and O2, respectively. Reproduced with permission from ref (92). Copyright 2013 American Chemical Society.
Figure 40
Figure 40
Cyclic voltammograms of 1 mM of K6[SiW11O39MnII(H2O)]·6H2O and K8[SiW11O39]·13H2O in an aqueous solution containing KH2PO4 (0.5 M) as a supporting electrolyte (scan rate, 50 mV s–1; initial potential, 0 V (vs Ag/AgCl); initial scan direction, toward more positive potential; working electrode, glassy carbon; reference electrode, Ag/AgCl; counter electrode, Pt coil). Reproduced with permission from ref (93). Copyright 2016 Wiley-VCH Verlag GmbH & Co. KGaA, Weinheim.
Figure 41
Figure 41
Time courses of H2 evolution over Ru/SrTiO3:Rh from a phosphate solution (0.5 M) containing [SiW11O39MnII(H2O)]6– (photocatalyst, 0.1 g; the amount of water, 50 mL). Reproduced with permission from ref (93). Copyright 2016 Wiley-VCH Verlag GmbH & Co. KGaA, Weinheim.
Figure 42
Figure 42
Adsorption amounts of SiW11Mn on (a) SrTiO3:Rh and (b) WO3 particles in 0.5 M phosphate solution (amount of photocatalyst, 15 mg; amount of Milli-Q water, 10 mL; stirring time, 15 h in dark; BET surface area, SrTiO3:Rh 5.9 m2 g–1, WO3 4.6 m2 g–1). Reproduced with permission from ref (93). Copyright 2016 Wiley-VCH Verlag GmbH & Co. KGaA, Weinheim.
Figure 43
Figure 43
Time courses of O2 evolution over PtOx/WO3 from an aqueous solution containing [SiW11O39MnIII(H2O)]5–. Dotted lines indicate the theoretical amount of O2 calculated from added [SiW11O39MnIII(H2O)]5– (photocatalyst, 0.1 g; the amount of water, 100 mL). Reproduced with permission from ref (93). Copyright 2016 Wiley-VCH Verlag GmbH & Co. KGaA, Weinheim.
Figure 44
Figure 44
X-ray photoelectron spectra of I 3d and Pt 4f for Pt (3 wt %)–anatase TiO2 powders; fresh sample (a), after stirring in an aqueous solution of NaI (1 mM) for 12 h in dark (b), after photoreaction in an aqueous solution of NaI (1 mM) for 20 h under UV light irradiation (c). X-ray photoelectron spectrum of I-3d for bare anatase TiO2 powder after stirring in an aqueous solution of NaI (1 mM) for 12 h in the dark (d). Reproduced with permission from ref (133). Copyright 2003 Elsevier.
Figure 45
Figure 45
Water formation from H2 and O2 in gas phase reaction over (a) fresh and (b) I-adsorbed 3 wt % Pt–TiO2 photocatalyst powders. A mixture of H2 and O2 (H2:O2 = 2:1) gases was introduced to a closed gas-circulating system with a Pyrex glass cell containing 10 mg of photocatalyst powder without water. Reproduced with permission from ref (133). Copyright 2003 Elsevier.
Figure 46
Figure 46
Consumptions of H2 and O2 due to back-reactions with 2 mmol L–1 aqueous FeCl3 solution on the (Pt (0.3 wt %)/SrTiO3:Rh)–(BiVO4) (triangles) and (Ru (0.7 wt %)/SrTiO3:Rh)–(BiVO4) (circles) systems in the dark. Catalyst, 50 mg each; reactant solution, 120 mL, pH 2.4, adjusted by H2SO4. Reproduced with permission from ref (85). Copyright 2008 Elsevier.
Figure 47
Figure 47
Photocatalytic overall water splitting on (a) the (Ru (0.7 wt %)/SrTiO3:Rh)–(BiVO4) system and (b) the (Pt (0.1 wt %)/SrTiO3:Rh)–(BiVO4) system. Catalyst, 50 mg each; reactant solution, 2 mmol L–1 of aqueous FeCl3 solution, 120 mL, pH 2.4; light source, 300-W Xe-arc lamp (λ > 420 nm); cell, top-irradiation cell with a Pyrex glass window. Reproduced with permission from ref (85). Copyright 2008 Elsevier.
Figure 48
Figure 48
Time courses of photocatalytic H2 evolution under visible light (λ > 410 nm) on NKX-2677 dye-adsorbed Pt(in)/H4Nb6O17, Pt(in–out)/H4Nb6O17, and Pt/TiO2 photocatalysts suspended in (a) 0.1 M aqueous KI solution (pH ∼ 6.5, without adjustment) and (b) 0.1 M aqueous triethanolamine solution (pH ∼ 7, adjusted with HCl). Reproduced with permission from ref (62). Copyright 2013 American Chemical Society.
Figure 49
Figure 49
Conceptual schemes for suppression of backward reaction using nanostructured layered semiconductors. Reproduced with permission from ref (62). Copyright 2013 American Chemical Society.
Figure 50
Figure 50
Rates of O2 evolution over ex-Ca2Nb3O10/K+ loaded with 0.3 wt % of various metal oxides (PtO, RuO2, IrO2, Rh2O3, and CoOx) in 5 mM NaIO3 aqueous solution under UV light irradiation (λ > 300 nm, Xe lamp) and overpotentials for IO3 reduction on each catalyst. Reproduced with permission from ref (136). Copyright 2015 The Royal Society of Chemistry.
Figure 51
Figure 51
Dependence of rates of O2 evolution over Pt(0.5 wt %)–WO3 photocatalysts upon the calcination temperature after impregnation of H2PtCl6. The reaction was carried out in aqueous solution (250 mL) containing NaIO3 (2 mM). Reproduced with permission from ref (59). Copyright 2011 Wiley-VCH Verlag GmbH & Co. KGaA, Weinheim.
Figure 52
Figure 52
Current–potential curves of TaON electrodes loaded with Ru species and an unmodified TaON electrode in an aqueous Na2SO4 solution (0.1 M) containing NaIO3 (1.0 mM) under dark conditions. Reproduced with permission from ref (137). Copyright 2017 The Royal Society of Chemistry.
Figure 53
Figure 53
Initial rate of O2 evolution on Ru-x and Ru-x-Co photocatalysts (50 mg) prepared at different temperatures in an aqueous solution (250 mL) containing NaIO3 (1.0 mM) under visible light (λ > 400 nm). Reproduced with permission from ref (137). Copyright 2017 The Royal Society of Chemistry.
Figure 54
Figure 54
Summary of the speculated role and activities of the cocatalysts loaded onto TaON. Reproduced with permission from ref (137). Copyright 2017 The Royal Society of Chemistry.
Figure 55
Figure 55
Photocatalytic O2 evolution over (a) WO3 without Cs-treatment, (b) Cs-WO3 (first run) prepared by the IMP method, and (c) Cs-WO3 (second run) under visible light irradiation. The dashed line shows the upper limit of O2 evolution expected from the amount of Fe3+ (1260 μmol) added to the solutions. The second run reaction was performed by exchanging the reactant solution of the first run with fresh Fe2(SO4)3 aqueous solution. Reproduced with permission from ref (138). Copyright 2010 American Chemical Society.
Figure 56
Figure 56
Time courses of the photocatalytic O2 evolution over PtOx/H–Cs–WO3 (solid line) and PtOx/WO3 (dotted line) suspended in the solutions containing 10 mM NaI and different concentrations of I3 (circles, 1 mM; squares, 0.5 mM; triangles, 0.2 mM). Catalyst, 0.4 g; reactant solution, 300 mL; light source, 300 W Xe lamp attached with L-42 cutoff filter. The dashed lines (30, 75, and 150 μmol) show the upper limits of O2 evolution (four-electron oxidation reaction) expected from the amount of I2 (I3) (reduced by two electrons) added to the solutions. Reproduced with permission from ref (80). Copyright 2013 The Royal Society of Chemistry.
Figure 57
Figure 57
Time courses of photocatalytic evolution of H2 and O2 using a mixture of 0.2 g of Pt/SrTiO3:Cr Ta as the H2 evolution photocatalyst and 0.4 g of PtOx/H–Cs–WO3 (circle plots) or PtOx/WO3 (triangle plots) as the O2 evolution photocatalyst suspended in 10 mM NaI aqueous solution (300 mL, pH 6.8). Light source: 300W Xe lamp attached with L42 cutoff filter. Reproduced with permission from ref (80). Copyright 2013 The Royal Society of Chemistry.
Figure 58
Figure 58
(a–c) SEM images of WO3 samples prepared via hydrothermal reaction at different temperatures (reaction time, 4 h). (d) TEM image of HT-315. Reproduced with permission from ref (91). Copyright 2016 The Chemical Society of Japan.
Figure 59
Figure 59
Adsorption isotherm (at 20 °C) of Fe cation on the surface of various WO3 samples in aqueous solution with different concentration of FeCl3 or FeCl2 (amount of WO3, 0.1 g; amount of solvent, 10 mL; time for mixing in dark under inert gas atmosphere, 15 h). Reproduced with permission from ref (91). Copyright 2016 The Chemical Society of Japan.
Figure 60
Figure 60
(a) Influence of Fe3+ concentration on the rate of O2 evolution under light irradiation. (b) Initial rate of O2 evolution on various WO3 photocatalysts suspended in aqueous solutions containing Fe3+ (16 mM) and Fe2+ (0, 1.6, 3.1, 7.9, and 12.4 mM) under light irradiation (pH 2.1 adjusted with HCl). Reproduced with permission from ref (91). Copyright 2016 The Chemical Society of Japan.

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