| Literature DB >> 35160913 |
Beatriz Trindade Barrocas1, Nela Ambrožová1, Kamila Kočí1.
Abstract
The photocatalytic reduction of carbon dioxide to renewable fuel or other valuable chemicals using solar energy is attracting the interest of researchers because of its great potential to offer a clean fuel alternative and solve global warming problems. Unfortunately, the efficiency of CO2 photocatalytic reduction remains not very high due to the fast recombination of photogenerated electron-hole and small light utilization. Consequently, tremendous efforts have been made to solve these problems, and one possible solution is the use of heterojunction photocatalysts. This review begins with the fundamental aspects of CO2 photocatalytic reduction and the fundamental principles of various heterojunction photocatalysts. In the following part, we discuss using TiO2 heterojunction photocatalysts with other semiconductors, such as C3N4, CeO2, CuO, CdS, MoS2, GaP, CaTiO3 and FeTiO3. Finally, a concise summary and presentation of perspectives in the field of heterojunction photocatalysts are provided. The review covers references in the years 2011-2021.Entities:
Keywords: CO2 reduction; TiO2; heterojunction nanocomposite; photocatalysis; renewable fuel; valuable chemicals
Year: 2022 PMID: 35160913 PMCID: PMC8839688 DOI: 10.3390/ma15030967
Source DB: PubMed Journal: Materials (Basel) ISSN: 1996-1944 Impact factor: 3.623
Main products of CO2 reduction and the corresponding potential (pH = 7).
| Reaction | Product | Reference | |
|---|---|---|---|
|
| −0.41 | Hydrogen | [ |
|
| −1.90 | [ | |
|
| −0.87 | Oxalate | [ |
|
| −0.61 | Formic acid | [ |
|
| −0.53 | Carbon monoxide | [ |
|
| −0.48 | Formaldehyde | [ |
|
| −0.38 | Methanol | [ |
|
| −0.33 | Ethanol | [ |
|
| −0.27 | Ethane | [ |
|
| −0.24 | Methane | [ |
Figure 1Schematic illustration of the electron–hole separation on an example of heterojunction photocatalyst type-II. Adapted according to refs. [18,19].
Figure 2Schematic illustration of the three different types of separation of electron–hole pairs in the case of conventional light-responsive heterojunction photocatalysts: (a) type-I, (b) type-II, and (c) type-III heterojunctions. Adapted according to Refs. [18,19].
Figure 3Schematic illustration of the electron–hole separation under the influence of the internal electric field of a p–n heterojunction photocatalyst under light irradiation. Adapted according to Refs. [18,19].
Figure 4Schematic representation of (a) electron–hole separation on the conventional Z-scheme photocatalytic system; (b) the electron–hole separation on all-solid-state Z-scheme photocatalysts; and (c) electron–hole separation on a direct Z-scheme heterojunction photocatalyst. Adapted according to Refs. [18,19].
CO2 photoreduction using g-C3N4/TiO2 heterojunction photocatalysts.
| Photocatalysts | CO2 Photoreduction Condition | Yield of Products | Type of Heterojunction | Ref. | ||||
|---|---|---|---|---|---|---|---|---|
| Type | Prepared | Reaction Mixture | Light Source | Conditions | ||||
| TiO2−x/g-C3N4 | Solid state synthesis | CO2 (99.999%), 5 mL of solution containing 4 mL of methyl cyanide (MeCN) solvent, 1 mL of triethanolamine (TEOA), bipyridine (bpy) (10 mmol L−1) and 25 μL of 20 mmol L−1 CoCl2 aqueous solution | 300 W xenon lamp | 43 mL quartz vessel with a rubber septum; 25 °C; circulation cooling system. | CO = 77.8 μmol g−1 h−1 | Type-II | * | [ |
| (0.3/1)TiO2/g-C3N4 | Simple mechanical mixing of pure g-C3N4 and commercial TiO2 Evonik P25 | CO2 with a certified maximum of hydrocarbons less than 1 ppm (SIAD Technical Gases, CZ) | 8 W Hg lamp | Cylindrical stirred batch reactor, with internal volume of 355 cm3 | CH4 = 70 μmol gcat.−1 | Type-II | ‡ | [ |
| TiO2@g-C3N4-20% | Stirring method | CO2 and 50 mL 0.08 mol L−1 NaHCO3 solution | 300 W Xe lamp with a 420 nm optical filter | quartz glass tube with a volume of 60 mL | CH3OH ~50 μmol gcat−1 after 4 h | Type-II(see Ref. [ | - | [ |
| HCNS@TiO2 | Templating method combined with the subsequent kinetically-controlled coating process | CO2 (high purity) and H2O (400 mL) | Visible-light (300 W Xenon lamp) | cylindrical Pyrex glass photoreactor with 500 mL of volume | CH3OH = 52.1 μmol gcat−1 | Type-II | † | [ |
| 70:30 g-C3N4-N-TiO2 | Hydrothermal method and thermal treatment | Deionized H2O + CO2 (99.999%) | 300 W Xe arc lamp | 780 mL gas-closed circulation Teflon system | CO = 14.73 μmol after 12 h | Type-II | ¥ | [ |
| Nb-TiO2/g-C3N4 | Solid state synthesis | CO2 (99.99%) flow rate 20 mL/min; water vapor was used as hole scavenger | Two 30 W white bulbs | continuous gas system with a reactor (40 mL) located in the center of a dark cover cask using as a reaction chamber (24 L) | CO = 420 μmol g−1 h−1 | Z-scheme | § | [ |
| 8 mass % g-C3N4/Ag-TiO2 | Solvent evaporation followed by calcination | CO2 flow rate 3 mL/min; water vapor was used as hole scavenger | 300 W xenon lamp | 70 mL cylindrical photoreactor | CH4 = 28.0 μmol g−1 | Type-II | ƗƗ | [ |
| Phosphate–oxygen (P–O) bridged TiO2/g-C3N4 | Impregnation-solid state synthesis | CO2 + 3 mL H2O; water vapor was used as a hole scavenger | 300 W xenon lamp | cylindrical steel reactor (volume of 100 mL and area of 3.5 cm2) | CH4 = 40 μmol g−1 h−1 | Z-scheme | I | [ |
| (Au, C3N4)/TiO2 | Immersing (or dipping) method | CO2 + 5 mL H2O | 300 W Xenon arc lamp | 100 mL sealed steel container with cooling water | CO = 0.138 µmol cm−2h−1
| Z-scheme | II | [ |
* Reprinted from [25], Copyright (2019), with permission from Elsevier. ‡ Reprinted with permission from [26]. Copyright 2016 American Chemical Society. † Reprinted from [28], Copyright (2020), with permission from Elsevier. ¥ Reprinted from [29], Copyright (2014), with permission from Elsevier. § Reprinted from [30], Copyright (2019), with permission from Elsevier. ƗƗ Reprinted from [31], Copyright (2017), with permission from Elsevier. I Reprinted from [32], Copyright (2017), with permission from Elsevier. II Reprinted from [33], Copyright (2019), with permission from Elsevier.
CO2 photoreduction using CeO2/TiO2 heterojunction photocatalysts.
| Photocatalysts | CO2 Photoreduction Condition | Yield of | Type of Heterojunction | Ref. | ||||
|---|---|---|---|---|---|---|---|---|
| Type | Prepared | Reaction Mixture | Light Source | Conditions | ||||
| Mes-CeTi-1.0 | Template method using a nanocasting route | CO2 + H2O | Xe arc lamp 300 W | stainless steel reactor (volume of 1500 mL) | CH4 = 11.5 mmol gcat−1 | - | - | [ |
| CeO2-TiO2 | Stirring method and calcination method | CO2 and 300 mL of 0.1 mol L−1 NaOH solution (for 30 min before irradiation) | Visible light—500 W Xenon lamp, and 2 mol L−1 sodium nitrite solution (to remove UV light) | Pyrex glass reactor (500 mL) | CH3OH = 18.6 μmol gcat−1 after 6 h | Type-II | * | [ |
| CeO2/TiO2-4 | Gas bubbling-assisted membrane precipitation (GBMP) method | CO2 and H2O | 300 W Xe lamp and an optical filter with the absorbed light wavelength of <420 nm | Glass reactor (basal diameter of 4 cm) | CO = 2.06 μmol after 6 h | Type-II | ‡ | [ |
| CeO2/TiO2 | Hydrothermal method | CO2 and H2O (Gaseous CO2 of 8 kPa was in site produced by the reaction of NaHCO3 with a H2SO4 solution (0.5 M).) | 500 W Xenon lamp | reactor connected with mechanical vacuum pump | CO = 61.9 μmol g−1 | Type-II | † | [ |
| 0.2CeO2/TiO2 | One-pot hydrothermal method | CO2 and H2O (Gaseous CO2 of 8 kPa was produced in situ by the reaction of NaHCO3 with a H2SO4 solution (0.5 M).) | 300 W Xenon lamp | reactor connected with mechanical vacuum pump | CO = 46.6 μmol g−1 | Type-II | ¥ | [ |
* Reprinted from [35], Copyright (2015), with permission from Elsevier. ‡ Reprinted with permission from [36]. Copyright 2014 American Chemical Society. † Republished with permission of Royal Society of Chemistry, from [37] copyright 2016; permission conveyed through Copyright Clearance Center, Inc. ¥ Reprinted from [38], Copyright (2016), with permission from Elsevier.
CO2 photoreduction using CuO/TiO2 heterojunction photocatalysts.
| Photocatalysts | CO2 Photoreduction Condition | Yield of Products | Type of Heterojunction | Ref. | ||||
|---|---|---|---|---|---|---|---|---|
| Type | Prepared | Reaction Mixture | Light Source | Conditions | ||||
| CuO/TiO2(AB) | Impregnation method | pure CH3OH solution (30 mL), and pure CO2 gas | 250 W Hg lamp | ideal mixing 50 mL quartz tube | HCOOCH3 = ~1800 μmol gcat−1 after 4 h | - | - | [ |
| 3 wt.% CuO/TiO2 | Impregnation method | CO2 (Ultra high purity grade), | 500 W high pressure Hg lamp with a peak light intensity at 365 nm | quartz reactor | methanol = 12.5 μmol g−1 | -- | - | [ |
| 1.0CuO-TiO2 | Stirring method followed by calcination | CO2 (99.99% purity) and 30 mL of methanol | 250 W high pressure mercury lamp with the radiation peak at about 365 nm | slurry reactor system | Methyl formate ~1600 μmol g−1 h−1 | Z-scheme | * | [ |
| CuO loaded TiO2 nanotube | Hydrothermal method | CO2 (flow rate of 30 mL min−1) and ultrapure water, and NaHCO3 (0.1 M) | 400 W high-pressure mercury lamp with a quartz filter | flow system with an inner-irradiation-type reaction vessel at ambient pressure | 100% CO2 conversion into CH4 and CH3OH after 2.5 h | Type-I | ‡ | [ |
* Reprinted from [39], Copyright (2011), with permission from Elsevier. ‡ Reprinted from [43], Copyright (2018), with permission from Elsevier.
CO2 photoreduction using CdS/TiO2 heterojunction photocatalysts.
| Photocatalysts | CO2 Photoreduction Condition | Yield of Products | Type of Heterojunction | Ref. | ||||
|---|---|---|---|---|---|---|---|---|
| Type | Prepared | Reaction Mixture | Light Source | Conditions | ||||
| TiO2/CdS-3 | Conventional hydrothermal technique | Ar or CO2 (both 99.99%) for 1 h, and aqueous isopropanol solution (1.0 M, 100 mL) | 450 W Xe arc lamp in combination with 320 nm or 420-nm-cutoff filters | airtight glass reactor (120 mL) with a quartz disc for light penetration | methane = ~18 µmol (after 10 h) | Type-II | * | [ |
| TiO2/CdS | Ionic layer adsorption and reaction (SILAR) method | CO2 and H2O vapor (from 84 mg of NaHCO3 and 0.3 mL of HCl solution (4 M)) | 300 W Xenon arc lamp | 200 mL Pyrex reactor | 11.9 mmol h−1 m−2 for CH4 production | Z-scheme | ‡ | [ |
| CdS-TiO2-8 | Hydrothermal method | CO2 and 10 mL cyclohexanol | 250 W high pressure mercury lamp | batch slurry bed reactor with inner capacity of 50 mL | cyclohexyl formate = 20.2 µmol gcat−1h−1 | Z-Scheme | † | [ |
| CdS-TiO2 S3 (45%) | Hydrothermal method | N2 and CO2 | 125 W Hg lamp (350–400 nm) | Pyrex reactor with an effective volume of 125 mL | Under UV-vis irradiation: | Type-II | ¥ | [ |
* Reprinted from [44], Copyright (2016), with permission from Elsevier. ‡ Reprinted from [45], © 2022 WILEY-VCH Verlag GmbH & Co. KGaA, Weinheim. † Reprinted from [46], Copyright (2014), with permission from Elsevier. ¥ Reprinted from [47], Copyright (2014), with permission from Elsevier.
CO2 photoreduction using MoS2/TiO2 heterojunction photocatalysts.
| Photocatalysts | CO2 Photoreduction Condition | Yield of | Type of Heterojunction | Ref. | ||||
|---|---|---|---|---|---|---|---|---|
| Type | Prepared | Reaction Mixture | Light Source | Conditions | ||||
| 10% MoS2/TiO2 | Calcined at 300 °C for 4 h with argon shielding gas | 100 mL deionized H2O which was preprocessed for 30 min with CO2 (99.99%) of 100 kPa | Xe-arc lamp 300 W acting | 500 cm3 cylindrical reactor | CO = 268.97 μmol gcat−1 | Type-II | * | [ |
| 10% MoS2/TiO2 | In situ growing MoS2 nanosheets onto TiO2 nanofibers by hydrothermal method | CO2 and H2O vapor were in situ generated by the reaction of NaHCO3 (0.12 g) and H2SO4 aqueous solution (0.25 mL, 2 M) | 350 W Xe lamp | 200 mL homemade Pyrex reactor | CH4 = 2.86 μmol g−1 h−1 | Type-II | ‡ | [ |
| 0.5 wt% MoS2/TiO2 | Hydrothermal method | 200 mL of 1 M NaHCO3 solution and pure CO2 | 300 W Xenon arc lamp. | airtight quartz glass reactor | CH3OH = 10.6 μmol g−1 h−1 | - | [ | |
* Reprinted from [49], Copyright (2019), with permission from Elsevier. ‡ Reprinted from [50], © 2022 WILEY-VCH Verlag GmbH & Co. KGaA, Weinheim.
CO2 photoreduction using GaP/TiO2, CaTiO3/TiO2 and FeTiO3/TiO2 heterojunction photocatalysts.
| Photocatalysts | CO2 Photoreduction Condition | Yield of Products | Type of Heterojunction | Ref. | ||||
|---|---|---|---|---|---|---|---|---|
| Type | Prepared | Reaction Mixture | Light Source | Conditions | ||||
| 1:10 GaP/TiO2 | Mechanically milling of Commercial TiO2 Evonik P25 and GaP Aldrich powders | CO2 and water | 1500 W high pressure Xe lamp | gas–solid Pyrex batch photoreactor of cylindrical shape (V = 100 mL, Φ = 94 mm, height = 15 mm) | CH4 = 118.18 | Z-scheme | * | [ |
| 20% FeTiO3/TiO2 | Hydrothermal method | 30 mL distilled water containing sodium bicarbonate (NaHCO3, 0.08 M) | 500 W high-pressure Xe lamp. | quartz reaction vessel, connected to a gas chromatograph. | CH3OH = 0.462 μmol g−1 h−1 under UV-vis irradiation and | - | - | [ |
| 13.4% CaTiO3/TiO2 | In situ hydrothermal method | CO2 and water | 300 W Xe lamp | Quartz tube reactor, with 43 mL volume | CO = 11.72 μmol g−1 h−1 | Z-scheme | ‡ | [ |
* Reprinted from [52], Copyright (2014), with permission from Elsevier. ‡ Republished with permission of Royal Society of Chemistry, from [54] copyright 2019; permission conveyed through Copyright Clearance Center, Inc.