| Literature DB >> 35471594 |
Xiaodong Sun1, Shuaiyu Jiang2, Hongwei Huang3, Hui Li2, Baohua Jia2, Tianyi Ma2.
Abstract
When it comes to using solar energy to promote catalytic reactions, photocatalysis technology is the first choice. However, sunlight can not only be directly converted into chemical energy through a photocatalytic process, it can also be converted through different energy-transfer pathways. Using sunlight as the energy source, photocatalytic reactions can proceed independently, and can also be coupled with other catalytic technologies to enhance the overall catalytic efficiency. Therefore, sunlight-driven catalytic reactions are diverse, and need to be given a specific definition. We propose a timely perspective for catalytic reactions driven by sunlight and give them a specific definition, namely "solar energy catalysis". The concept of different types of solar energy catalysis, such as photocatalysis, photothermal catalysis, solar cell powered electrocatalysis, and pyroelectric catalysis, are highlighted. Finally, their limitations and future research directions are discussed.Entities:
Keywords: Photocatalysis; Photothermal Catalysis; Pyroelectric Catalysis; Solar Cell Powered Electrocatalysis; Solar Energy
Year: 2022 PMID: 35471594 PMCID: PMC9400894 DOI: 10.1002/anie.202204880
Source DB: PubMed Journal: Angew Chem Int Ed Engl ISSN: 1433-7851 Impact factor: 16.823
Figure 1a) Conversion plots for Er3+−TiO2 systems under excitation with Vis/NIR light for the degradation of phenol (left) and methylene blue (right). b) Mechanism of the photocatalytic induction process in the Er3+−TiO2 heterostructures: Top: UV‐assisted mechanism and bottom: NIR up‐conversion assisted mechanism. Reproduced with permission. Copyright 2012, Royal Society of Chemistry. c) NOx destruction activities of C−TiO2, B−UP/C−TiO2, G−UP/C−TiO2, R−UP/C−TiO2, and P25 under irradiation with light of different wavelengths. d) PL spectra of B−UP, G−UP, R−UP, and three composites upon excitation at 980 nm. e) Mechanism of UV, visible and NIR lights induced photocatalysis of up‐conversion phosphors coupled C‐TiO2 composites. Reproduced with permission.[18c] Copyright 2014, Elsevier.
Figure 2a) Distribution of hydrocarbon products obtained over Co‐450 under irradiation with UV/Vis light. b) Comparison of CO conversion for Co‐450 under photothermal heating (UV/Vis irradiation) and direct thermal heating (no UV/Vis irradiation). c) Potential energy profile of CO dissociation on Co3O4(220), Co(111)/Co3O4(220), and Co(111). d) CH2 coupling and C2H4 hydrogenation on Co(111)/Co3O4(220) and Co(111). e) Fabrication of Co‐x catalysts by the reduction of ZnCoAl‐LDH nanosheets with H2 at 300–700 °C, and the selectivity of their products for CO hydrogenation under irradiation with UV/Vis light. Reproduced with permission. Copyright 2018, Wiley‐VCH. f) Aberration‐corrected HAADF‐STEM image of HPC‐800 (single Zn atoms are highlighted with red circles). g) Zn K‐edge XANES and h) k3‐weighted Fourier transform of the EXAFS spectra. The dashed lines highlight the peak difference of the Zn foil and HPC‐800. i) EXAFS R‐space fitting curve of HPC‐800 (inset: schematic model of HPC‐800: Zn red, N blue, and C gray). j) Schematic illustration showing the fabrication and catalytic process of the HPC. Reproduced with permission. Copyright 2019, Wiley‐VCH.
Figure 3a) H2 generation rates of ST NS, AST NS, and ST NS−Au under irradiation with UV light and full spectrum light. b) Temperature profile of SiO2 and AS under irradiation with UV light and full spectrum light. c) Schematic diagram showing the effect of irradiation with UV and Vis/NIR light on the surface potential of AS. d) Schematic diagram showing the effect of irradiation with UV and Vis/NIR light on the surface potential of ST NS−Au. e) Schematic diagram illustrating the mechanism of enhanced photocatalytic H2 generation as a result of photothermal and photochemical effects. Reproduced with permission. Copyright 2021, Wiley‐VCH. f) Photograph of a TiO2/C bilayer paper, size: 25 cm×25 cm. g) Schematic illustration of the photothermal‐assisted triphasic photocatalytic oxidation of phenol. Reproduced with permission. Copyright 2021, Wiley‐VCH.
Figure 4a) CO2 conversion as a function of irradiation time under a 300 Xe lamp with an optical density of 2.0 W cm−2. b) CH4 selectivity and CO2 conversion. c)–e) HAADF‐STEM images of c) 0.15Ru@NVO, d) 0.35Ru@NVO, and e) 0.82Ru@NVO. f) Stability testing for the catalytic generation of CH4 over 0.35Ru@NVO. g) Variation in the temperatures of different NVO‐based catalysts under a full‐Arc 300 W Xe lamp with an optical density of 2.0 W cm−2. The error bars represent the standard deviation of five independent measurements on the same catalyst. h) Proposed catalytic reaction mechanism for the hydrogenation of CO2 over the 0.35Ru@NVO catalyst. Reproduced with permission. Copyright 2021, Wiley‐VCH. i) Dependence of the methanol production rate on the light intensity in the presence of the Pd3Cu@UiO‐66 catalyst. j) Methanol formation rates over Pd3Cu@UiO‐66 in the dark or under irradiation at >320 nm or with full‐spectrum light. k) UV/Vis spectra of UiO‐66 and the Pd3Cu@UiO‐66 catalyst. l) ESR spectra of Pd3Cu@UiO‐66 under different conditions. m) Schematic illustration showing the light‐assisted hydrogenation of CO2 to CH3OH over Pd3Cu@UiO‐66 and Pd3Cu/UiO‐66, whereby H2 and CO2 molecules are activated on Pd3Cu NPs and defective Zr‐oxo clusters, respectively, in proximity in Pd3Cu@UiO‐66, which leads to its enhanced activity. Reproduced with permission. Copyright 2021, Wiley‐VCH.
Figure 5Morphology and chemical composition of NiMo/NF. a)–d) SEM images, e) HAADF‐STEM image, f) FFT image, where crystal facets of MoNi4, MoO2, and NiMoO4 are shown in yellow, white, and purple, respectively, and g) EDX mapping of a nanoparticle on the stem‐like structure. h) Schematic illustration of the direct solar water splitting system consisting of a perovskite‐Si tandem cell integrated with NiFe/NF||NiMo/NF electrodes. i) Overlay of the J–V curve of a perovskite‐Si tandem cell with the LSV curve of the NiMo and NiFe electrodes in a two‐electrode configuration. j) Unassisted water splitting current generated by the integrated system. k) Comparison of the STH efficiency achieved in this work with reported values for other solar‐driven water‐splitting systems. Reproduced with permission. Copyright 2014, The American Association for the Advancement of Science. l)–o) Electrochemical performance of different catalyst electrodes by linear sweep voltammetry in 1 m NaOH aqueous electrolyte, and gas chromatographic measurement of gases evolved from NiFe LDH electrodes. p) Schematic diagram of the water‐splitting device. q) A generalized schematic illustration of the energy of the perovskite tandem cell for water splitting. r) J–V curves of the perovskite tandem cell under dark and simulated AM 1.5G 100 mW cm−2 illumination, and the NiFe/Ni foam electrodes in a two‐electrode configuration. s) Current density/time curve of the integrated water‐splitting device without external bias. Reproduced with permission. Copyright 2021, Wiley‐VCH.
Figure 6a) Scanning electron micrograph of as‐prepared CuO nanowires. b) X‐ray diffraction pattern of SnO2‐modified and unmodified samples. From the annotated reflections, the presence of CuO could be observed but no reflections corresponding to SnO2 were detected. c) Schematic illustration of the solar‐driven device for CO2 reduction. d) Photovoltaic and electrocatalytic J–V behaviors. e) Selectivity toward CO, solar current density, and solar‐to‐CO efficiency as a function of photoelectrolysis time. Reproduced with permission. Copyright 2017, Springer Nature. f) EDX elemental mapping of the CuAg nanocoral cathode. g) SEM surface view of IrO2 nanotubes on iridium foil. h) J–V curves of the CuAg nanocoral cathode under various electrolyte conditions. i) J–V curves of the IrO2 nanotube anode on FTO, Ti foil, and Ir foil substrates in 0.2 m CsHCO3 electrolyte. j) CO2 RR product distribution at −1 V vs. RHE (ca. 10 mA cm−2) in 0.2 m CsHCO3 electrolyte. Error bars are standard deviations based on replicate experiments. k) J–V curve of the Ir foil/IrO2 anode under various electrolyte conditions. Electrochemical measurements were performed under constant CO2 bubbling (the conditions used in the electrolysis cell). Reproduced with permission. Copyright 2017, Royal Society of Chemistry.
Figure 7Evaluation of the rate of hydrogen production and AQY of composite microfibers. a) Rates of hydrogen evolution using PVDF‐HFP/CNT/CdS−Pt fibers with different CNT contents. Comparison of the hydrogen generation rates (b) and AQY (c) of the above fibers. Characterization of the photogenerated carrier behavior of the samples PVDF‐HFP/CNT/CdS (P−H/C/CdS), PVDF‐HFP/CdS (P−H/CdS), PVDF‐CTFE/CNT/CdS (P−C/C/CdS), and PVDF‐CTFE/CdS (P−C/CdS). d) Photocurrent outputs, e) electrochemical impedance spectroscopy (EIS) Nyquist plots, f) the relative temperature‐dependent photoluminescence (PL) intensity (integrated from 425 to 525 nm, ex. 325 nm). Schematic diagram of IR‐responsive photoinduced carriers for the enhanced photocatalytic generation of hydrogen. g) Schematic representation of the photocatalytic composite microfiber PVDF‐HFP/CNT/CdS−Pt semi‐immersed in water. Under irradiation with light, the CNT absorbs infrared light and is heated first, which then heats the microfiber substrate PVDF‐HFP. The dipoles of the pyroelectric substrate PVDF‐HFP oscillate more evidently and, thus, a pyroelectric potential forms on the microfiber surface. h) Photoexcited carriers from CdS move in opposite directions, driven by the pyroelectric field. Electrons migrate to the co‐catalyst Pt and react with water molecules to generate hydrogen. i) Energy band bending for the ideal interface between the microfiber substrate PVDF‐HFP and CdS. Reproduced with permission. Copyright 2020, Wiley‐VCH.
Different types of catalytic reactions driven by solar energy.
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Catalysts |
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Catalytic condition |
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Catalytic applications |
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Types of SEC reaction |
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Catalytic activity |
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Ref. |
|---|---|---|---|---|---|---|---|---|---|---|
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Pt−Co3O4/18‐facet SrTiO3 |
|
UV light (300 W Xe lamp) |
|
Overall water splitting |
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Photocatalysis |
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AQE value is 0.81 % at 365 nm |
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|
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Ta3N5/Rh/Cr2O3 |
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Visible light (300 W Xe lamp) or solar simulator AM 1.5G |
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Overall water splitting |
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Photocatalysis |
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AQE values are 2.2 % at 320 nm, 0.22 % at 420 nm, 0.024 % at 500 nm |
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|
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Bi4NbO8Cl/Rh‐doped SrTiO3 |
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300 W Xe lamp fitted with L‐42 cut off filter |
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Overall water splitting |
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Photocatalysis |
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About 304.7 μmol of O2 for 60 h |
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|
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Pt‐loaded MgTa2O6− |
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Full light (300 W xenon lamp) |
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Overall water splitting |
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Photocatalysis |
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AQE value is 6.8 % at 420 nm |
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|
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COF‐318‐TiO2 |
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A xenon arc lamp (200 mW cm−2) with a light filter (380–800 nm) |
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CO2 reduction |
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Photocatalysis |
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CO2‐to‐CO conversion efficiency of 69.67μmol g−1/h |
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|
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3DOM CdSQD/NC |
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300 W xenon lamp with a 420 nm cut‐off filter |
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CO2 reduction |
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Photocatalysis |
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AQE value is 2.9 % at 450 nm |
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|
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Single‐atom Ni−OB−CN photocatalyst |
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300 W Xe lamp |
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CO2 reduction |
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Photocatalysis |
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CO and CH4 production rates of 22.1 and 8.7 μmol g−1 h−1 |
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|
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TPA‐PQ |
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A 300 W xenon arc lamp with a visible band pass filter (λ>420 nm) |
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CO2 reduction |
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Photocatalysis |
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CO2 to CH4 yield of 32.2 mmol g−1, with a rate of 2.15 mmol h−1 g−1 and high selectivity of 97 % |
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|
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Er3+−TiO2 |
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UV/Vis‐NIR light |
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Phenol degradation |
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Up‐conversion effect promoted photocatalysis |
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About 90 % phenol is degraded after 120 min |
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|
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QDs/g‐C3N4 |
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Visible light (300 W xenon lamp) |
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Organic dye degradation |
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Up‐conversion effect promoted photocatalysis |
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54 % MO ( |
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1 |
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C−TiO2/three color emitting up‐conversion phosphors |
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LEDs and NIR laser |
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NO |
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Up‐conversion effect promoted photocatalysis |
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NIR light induced photocatalytic ability with about 9.3 % of NO destruction |
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|
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(UCNPs)‐Pt@MOF/Au |
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Full solar light equipped with AM 1.5G |
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H2 evolution |
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Up‐conversion effect promoted photocatalysis |
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H2 evolution rate of 280 μmol g−1 h−1 |
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|
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Co‐ |
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UV/Vis irradiation (300 W Xe light) |
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Fischer–Tropsch synthesis |
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Light‐driven thermal catalysis |
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An olefin (C2–4 =) selectivity of 36.0 % and an olefin/paraffin ratio of 6.1 at a CO conversion of 15.4 % |
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|
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MnO‐modified Ni‐based catalyst systems |
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UV/Vis irradiation (300 W Xe light) |
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CO hydrogenation to light olefins |
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Light‐driven thermal catalysis |
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33 % selectivity to light olefins at a CO conversion of 14.9 % |
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|
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Metal‐organic‐framework derived hollow N‐doped porous carbon |
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300 mW cm−2 full spectrum irradiation |
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CO2 cycloaddition |
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Light‐driven thermal catalysis |
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The yield of cycloaddition of CO2 with 3‐bromopropylene oxide is 94 % |
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|
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PMo12@Zr−Fc MOFs |
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Light irradiation with sunlight intensity of 0.2 W cm−2 |
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CO2 cycloaddition |
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Light‐driven thermal catalysis |
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The yield of cycloaddition of CO2 with styrene oxide is 88.05 % |
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|
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Zn SA−NC |
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300 mW cm−2 full spectrum irradiation |
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CO2 cycloaddition |
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Light‐driven thermal catalysis |
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Yields of 99 % for epichlorohydrin and 97 % for 3‐bromopropylene oxide |
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|
|
Ni@C−X |
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UV/Vis‐IR light irradiation |
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CO2 reduction |
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Light‐driven thermal catalysis |
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CH4 production rates of 488 mmol g−1 h−1 |
|
|
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Plasmonic ZnCu alloy catalyst |
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AM 1.5 light as the illuminant, and a maximum light intensity of 788 mW cm−2 |
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Water and methanol activation for H2 production |
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Light‐driven thermal catalysis |
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H2 production rate of 328 mmol g−1 h−1 with a solar energy conversion efficiency of 1.2 % |
|
|
|
Cu@HKUST‐1 composites |
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300 W Xe lamp |
|
Cascade reactions (hydrogenation of nitrobenzene followed by reductive amination of benzaldehyde) |
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Light‐driven thermal catalysis |
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100 % selectivity toward N‐benzylideneaniline over 10 h |
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|
|
Pd nanocubes@ZIF‐8 |
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60 mW cm−2 full‐spectrum |
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Hydrogenation of 1‐hexene |
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Light‐driven thermal catalysis |
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Approximately 100 % conversion in 90 mins |
|
|
|
Ga−Cu/CeO2 |
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300 W xenon arc lamp was utilized as the illuminant |
|
CO2 reduction |
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Light‐driven thermal catalysis |
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A CO production rate of 111.2 mmol g−1 h−1 with nearly 100 % selectivity |
|
|
|
Rh/Al nanoantenna catalyst |
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Simulated solar irradiation (11.3 W ⋅ cm−2) |
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CO2 methanation |
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Light‐driven thermal catalysis |
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CH4 productivity of 550 mmol g−1 h−1 with nearly 100 % selectivity |
|
|
|
Ag@SiO2@TiO2−Au |
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UV and full‐spectrum irradiation |
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H2 evolution |
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Thermal‐assisted photocatalysis |
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H2 evolution rate of 30.2 mmol g−1 h−1 |
|
|
|
Bilayer paper from commercialized TiO2 and carbon nanomaterials |
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Full‐spectrum irradiation |
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Photocatalytic phenol oxidation |
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Thermal‐assisted photocatalysis |
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88.4 %mineralization of high concentration phenol within 90 min |
|
|
|
Silver‐decorated titanium oxide at a gas–water boundary |
|
Full‐spectrum irradiation |
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CO2 reduction |
|
Thermal‐assisted photocatalysis |
|
CO2 reduction rate of 305.7 μmol g−1 h−1 |
|
|
|
Pt/PCN‐224(M) |
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Visible light irradiation with relatively low intensity (<100 mW cm−2) |
|
Oxidation of primary alcohols to aldehydes |
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Thermal‐assisted photocatalysis |
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The yield of oxidation of benzyl alcohol by O2 is >99 % within 50 min |
|
|
|
Triphenylbenzene‐dimethoxyterephthaldehyde‐COF |
|
Visible light (300 W Xe lamp) |
|
Photocatalytic hydrogen peroxide production |
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Thermal‐assisted photocatalysis |
|
H2O2 production rate of 2.9 mmol g−1 h−1 |
|
|
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Ni/mesoporous TiO2 |
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Xenon light (XE‐300F) is used as the light source |
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Methane dry reforming reaction |
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Thermal‐assisted photocatalysis |
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The average conversions of CH4/CO2 increased by around 14.18 % and 15.91 % |
|
|
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Ni/TiO2 |
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Solar light simulator (CEL‐HXF300, 300 W Xenon lamp) |
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N2 hydrogenation |
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Thermal‐assisted photocatalysis |
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Ammonia yield of 19.9 μg (gcath)M‐>1 |
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|
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Ru@Ni2V2O7 |
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300 W Xe lamp irradiation (about 2.0 W cm−2) |
|
Sabatier reaction |
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Photothermal synergistic catalysis |
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CO2 methanation rate of 114.9 mmol g−1 h−1 |
|
|
|
Pd3Cu@UiO‐66 |
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Light irradiation with a 300 W Xe lamp |
|
CO2 hydrogenation |
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Photothermal synergistic catalysis |
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A methanation production rate of 340 μmol g−1 h−1 |
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|
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M‐doped TiO2 (M=Zn, Ni, and Cu) |
|
300 W Xe lamp |
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CO2 conversion |
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Photothermal synergistic catalysis |
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Stable production of CO of 10.80 μmol g−1 |
|
|
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Fe‐based catalysts |
|
Light irradiation |
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CO2 conversion |
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Photothermal synergistic catalysis |
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11.3 mmol g−1 h−1 activity for the catalytic conversion of CO2 |
|
|
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NiFe DLH/Ni foam coupled with/perovskite tandem cell |
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Simulated AM 1.5G solar irradiation (100 mW cm−2) |
|
Overall water splitting |
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Solar cell powered electrocatalysis |
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Solar‐to‐hydrogen efficiency of 12.3 % |
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|
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NiMo alloy NiFe alloy/perovskite/Si tandem semiconductors |
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incident irradiation power (100 mW m−2) |
|
Overall water splitting |
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Solar cell powered electrocatalysis |
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Solar‐to‐hydrogen efficiency of 20 % |
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|
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Perovskite‐organic monolithic tandem solar cells/NiFe LDH electrodes |
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Simulated AM 1.5G illumination |
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Overall water splitting |
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Solar cell powered electrocatalysis |
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Solar‐to‐hydrogen efficiency of 12.30 % and 11.21 % for rigid, and flexible perovskite‐organic tandem solar cell based PV‐driven electrolysis systems |
|
|
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A p+nn+‐Si/Ti/Pt photocathode |
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Simulated AM 1.5G illumination |
|
Overall water splitting |
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Solar cell powered electrocatalysis |
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17.6 % STH efficiency |
|
|
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two monolithically encapsulated perovskite solar cells with CoP and FeNi(OH) |
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Simulated AM 1.5G illumination |
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Overall water splitting |
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Solar cell powered electrocatalysis |
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Solar‐to‐hydrogen efficiency of 8.54 % |
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|
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NiCoFe‐based electrocatalyst/monolithic perovskite/silicon tandem solar cell |
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Simulated AM 1.5G illumination |
|
Overall water splitting |
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Solar cell powered electrocatalysis |
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20 % solar‐to‐hydrogen efficiency |
|
|
|
SnO2 modified CuO nanowire electrodes/GaInP/GaInAs/Ge photovoltaic |
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Simulated AM1.5G spectrum at 1 sun intensity |
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CO2 reduction |
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Solar cell powered electrocatalysis |
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A solar‐to‐CO efficiency of 13.4 % |
|
|
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CuAg bimetallic cathode/four‐terminal III–V S−1i tandem solar cell |
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1 Sun illumination |
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CO2 reduction |
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Solar cell powered electrocatalysis |
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Conversion efficiency to hydrocarbons and oxygenates exceeding 5 % |
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|
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GaAs solar cell/nano‐Au electrocatalyst |
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1 Sun illumination |
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CO2 reduction |
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Solar cell powered electrocatalysis |
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Solar‐to‐CO photoconversion efficiency of 15.6 % |
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|
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Si solar cell/Cu catalyst |
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1 Sun illumination |
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CO2 reduction |
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Solar cell powered electrocatalysis |
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Solar conversion efficiencies of 4.47 % and 6.4 % for C2H4 and C2+ |
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|
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Lead zirconate titanate |
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Thermal cycling |
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H2 evolution |
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Pyroelectric catalysis |
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H2 evolution rate of 0.654 μmol/h |
|
|
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PVDFHFP/CNT/CdS |
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280 W xenon lamp with simulated full‐spectra solar light |
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H2 evolution |
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Pyroelectric catalysis |
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Apparent quantum yield of 16.9 % |
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