| Literature DB >> 28772988 |
Samsun Nahar1,2, M F M Zain3,4, Abdul Amir H Kadhum5, Hassimi Abu Hasan6, Md Riad Hasan7,8.
Abstract
In recent years, the increasing level of CO₂ in the atmosphere has not only contributed to global warming but has also triggered considerable interest in photocatalytic reduction of CO₂. The reduction of CO₂ with H₂O using sunlight is an innovative way to solve the current growing environmental challenges. This paper reviews the basic principles of photocatalysis and photocatalytic CO₂ reduction, discusses the measures of the photocatalytic efficiency and summarizes current advances in the exploration of this technology using different types of semiconductor photocatalysts, such as TiO₂ and modified TiO₂, layered-perovskite Ag/ALa₄Ti₄O15 (A = Ca, Ba, Sr), ferroelectric LiNbO₃, and plasmonic photocatalysts. Visible light harvesting, novel plasmonic photocatalysts offer potential solutions for some of the main drawbacks in this reduction process. Effective plasmonic photocatalysts that have shown reduction activities towards CO₂ with H₂O are highlighted here. Although this technology is still at an embryonic stage, further studies with standard theoretical and comprehensive format are suggested to develop photocatalysts with high production rates and selectivity. Based on the collected results, the immense prospects and opportunities that exist in this technique are also reviewed here.Entities:
Keywords: CO2 reduction; photocatalysis; plasmonic photocatalyst; surface plasmon resonance (SPR); visible light irradiation
Year: 2017 PMID: 28772988 PMCID: PMC5553537 DOI: 10.3390/ma10060629
Source DB: PubMed Journal: Materials (Basel) ISSN: 1996-1944 Impact factor: 3.623
Advances in photocatalytic systems for CO2 reduction with water since the year 2010.
| Photocatalyst | Radiation Source | Major Products | Comments | References |
|---|---|---|---|---|
| 0.5 wt % Cu/TiO2-SiO2 | Xe lamp (2.4 mW cm−2, 250–400 nm) | CO and CH4 | The synergistic combination of Cu deposition and high surface area of SiO2 support enhanced CO2 photoreduction rates. | [ |
| ZnGa2O4 | 300 W Xe arc lamp | CH4 | Strong gas adsorption and large specific surface area of the mesoporous ZnGa2O4 photocatalyst contribute to its high photocatalytic activity for converting CO2 into CH4. | [ |
| (RuO + Pt)-Zn2GeO4 | 300 W Xe arc lamp | CH4 | In the presence of water, ultra-long and ultrathin geometry of the Zn2GeO4 nano-ribbon promotes CO2 photo-reduction, which was significantly enhanced by loading of Pt or RuO2. | [ |
| Ag/ALa4Ti4O15 (A = Ca, Ba and Sr) | 400 W Hg lamp | CO, HCOOH, and H2 | On the optimized Ag/BaLa4Ti4O15 photocatalyst, CO was the reported as the main product. The molar ratio of O2 production (H2 + CO:O2 = 2:1) demonstrated that water was consumed as a reducing reagent in the photocatalytic process. | [ |
| I-TiO2 nanoparticles | 450 W Xe lamp | CO | High photocatalytic activity was observed under visible light and the efficiency of CO2 photoreaction was much greater than undoped TiO2 due to the extension in the absorption spectra of TiO2 to the visible light region and facilitated charge separation. | [ |
| LiNbO3 | Natural sunlight or Hg lamp (64.2 mW cm−2) | HCOOH | The MgO-doped LiNbO3 showed an energy conversion efficiency rate of 0.72% which was lower than that for the gas–solid catalytic reaction of LiNbO3 (2.2%). | [ |
| G-Ti0.91O2 hollow spheres | 300 W Xe arc lamp | CH4, CO | The presence of G nanosheets compactly stacking with Ti0.91O2 nanosheets allows the rapid migration of photo-generated electrons from Ti0.91O2 nanosheets into G and improves the efficiency of the photocatalytic process. | [ |
| Graphene oxides (GOs) | 300 W commercial halogen lamp | CH3OH | Among all GOs, GO-3 exhibited the highest efficiency as a photocatalyst for CO2 reduction under visible light, and the conversion rate of CO2 to CH3OH on modified GO (GO-3) was 0.172 mmol g−1 cat h−1, which is six-fold higher than that of pure TiO2. | [ |
| W18O49 | 300 W Xe lamp | CH4 | The oxygen-vacancy-rich ultrathin W18O49 nanowires can be used to design materials with extraordinary photochemical activity because it displayed high CO2 reduction capability in presence of water. | [ |
| Zn1.7GeN1.8O | 300 W Xe arc lamp | CH4 | Zn1.7GeN1.8O loaded with co-catalysts showed significantly higher conversion rate of CO2 into CH4. | [ |
| Pt-, Au-, or Ag-loaded mesoporous TiO2 | 350 W Xe lamp | CH4 | The mesoporous TiO2 showed higher efficiency towards CO2 reduction when loaded with noble metal particles, and the order of enhanced photocatalytic activity was Pt > Au > Ag. The optimum loading amount of Pt was 0.2 wt %. | [ |
| 0.5 wt % Pt loaded ZnAl2O4-modified mesoporous ZnGaNO | 300 W Xe lamp (λ = 420 nm) | CH4 | The high photocatalytic activity of this photocatalyst was attributed to the improved gas adsorption of the mesoporous structure, the chemisorption of CO2 on the photocatalyst and the narrow bandgap of ZnAl2O4-modified ZnGaNO to extend the light absorption. | [ |
| Ga2O3 with mesopores and macropores | 300 W Xe lamp (500 mW cm−2) | CH4 | Ga2O3 with mesopores and macropores showed high photocatalytic activity due to its higher CO2 adsorption capacity (300%) and increased surface area (200%) compared to the bulk nanoparticles. | [ |
| Pt-TiO2 thin nanostructured films | 400 W Xe lamp | CO and CH4 | The catalyst can be produced at an industrial scale for commercial application and showed high efficiency for selective CH4 formation. | [ |
| HNb3O8 | 350 W Xe lamp | CH4 | KNb3O8 and HNb3O8 were synthesized by the conventional solid-state reaction and performed more effectively in photocatalytic CO2 reduction than commercial TiO2. | [ |
| ZnO-based materials | 8 W fluorescent tube (average intensity 7 mW cm−2) | CO, CH4, CH3OH, H2 | N-doping did not show any important influence on the photocatalytic behavior of ZnO-based photocatalysts. The mesoporous structure of ZnO favored CO and H2 production, but catalysts with Cu showed an enhancement in the hydrocarbon production, mainly CH3OH. | [ |
| Ag, Pt, bimetallic Ag–Pt and core–shell Ag@silica (SiO2) nanoparticles with TiO2 | 100 W Hg lamp (330 nm) | CH4 | The use of a reactor with three optical windows, a combination of both bimetallic co-catalysts, and Ag@SiO2 nanoparticles increased the product formation significantly compared to bare TiO2. | [ |
| Carbon nanotubes Ni/TiO2 Nano-composites | 75 W visible daylight lamp (λ > 400 nm) | CH4 | Compared to Ni/TiO2 and pure anatase TiO2, Ni/TiO2 incorporated with carbon nanotubes demonstrated maximum CH4 product yield of 0.145 mmol h−1 g−1 catalysts after 4.5 h of irradiation under visible light. | [ |
| Pt/Cu/TiO2 | 200 W Xe lamp | CH4, CO, H2 | The addition of co-catalyst Pt decreases the selectivity for CO2 photo-reduction; however, loading Cu onto TiO2 increases the selectivity from 60 to 80%. | [ |
| Au/Pt/TiO2 | 500 W Xe lamp | CH4, CO | Plasmonic photocatalyst Au/Pt/TiO2 provided a more effective way to harvest solar energy by consuming a high-energy photon in the solar spectrum (UV region) and using it for charge carrier generation. Moreover, it also utilized visible light to enhance the photocatalytic activity. | [ |
| 20 wt % montmorillonite modified TiO2 | 500 W Hg lamp (365 nm) | CH4 | Loading of montmorillonite on TiO2 enhanced the surface area and reduced particle size, thus improving charge separation, resulting in maximum yield for CH4 (441.5 mmol·g·cat−1 h−1). | [ |
| 0.5 wt % Pt/NaNbO3 | 300 W Xe lamp (λ > 300 nm) | CH4, CO, H2 | The cubic-orthorhombic surface-junctions of mixed-phase NaNbO3 enhanced the charge separation, thereby improving its photoactivity. | [ |
| Ag supported on AgIO3 (Ag/AgIO3 particles) | 500 W Xe arc lamp | CH4 and CO | In the conversion of CO2 to CH4 and CO using water vapor, Ag/AgIO3 particles showed high and stable activity because of the surface plasmon resonance effect of Ag particles. | [ |
| g-C3N4/NaNbO3 nanowires | 300 W Xe arc lamp | CH4 | An intimate interface formation was suggested between the C3N4 and NaNbO3 nanowires in g-C3N4/NaNbO3 heterojunction photocatalyst, resulting in almost eight-fold higher CO2 reduction than individual C3N4 under visible light irradiation. | [ |
| In2O3/g-C3N4 | 500 W Xe lamp | CH4 | The addition of In2O3 nanocrystals onto g-C3N4 surface improved the photocatalytic CO2 reduction process significantly due to the interfacial transfer of photo-generated electrons and holes between g-C3N4 and In2O3. | [ |
| SnO2−x/g-C3N4 composite | 500 W Xe lamp | CO, CH3OH, and CH4 | Enhancement in the surface area of g-C3N4 was observed by introducing SnO2−x. Improve photocatalytic performance was attributed to the increased light absorption and accelerated the separation of electron–hole pairs. | [ |
| AgX/g-C3N4 (X = Cl and Br) nanocomposites | 15 W energy-saving daylight bulb. | CH4 | Under ambient condition and low-power energy-saving lamps, the optimal 30 AgBr/pCN (protonated graphitic carbon nitride photocatalyst) sample showed highest photocatalytic activity with significant enhancement in CH4 formation compared to individual AgBr and pCN photocatalyst. | [ |
| Ag supported on Ag2SO3 (Ag/Ag2SO3) | 500 W Xe lamp | CH4 and CO | Plasmonic photocatalyst Ag/Ag2SO3 was stable towards CO2 photoreduction after 10 repetitive catalytic cycles with high efficiency under visible light irradiation. | [ |
Figure 1Schematic diagram of photo-excitation and electron transfer process (adapted from [63]).
Reduction potentials for the CO2 reduction process. E0: Standard reduction potential.
| Reactions | E0/eV |
|---|---|
| CO2 + e− → CO2 | |
| CO2 + 2e− + 2H+ → HCOOH | −0.61 |
| CO2 + 2e−+ 2H+ → CO + H2O | −0.53 |
| CO2 + 4e− + 4H+ → HCHO + H2O | −0.48 |
| CO2 + 6e− + 6H+ → CH3OH + H2O | −0.38 |
| CO2 + 8e− + 8H+→ CH4 + 2H2O | −0.24 |
Figure 2Schematic representation of conduction band, valence band potentials, and band gap energies of various semiconductor photocatalysts and relative redox potentials of the compounds involved in CO2 reduction at pH 7 (Adapted from [22]).
Figure 3Advantages and disadvantages of metal complex catalysts for CO2 reduction with H2O oxidation (adapted from [8]). (a) The advantages of H2O oxidation of a metal complex catalyst (H2O oxidation site) with a sacrificial electron acceptor (SA); (b) the advantages of CO2 reduction for a metal complex catalyst (CO2 reduction site) with a sacrificial electron donor (SD); (c) the problems encountered when combining H2O oxidation site and CO2 reduction site.
Influence of reaction phase on photocatalytic reduction a of CO2 with H2O using TiO2 and 0.5 wt % Pt-TiO2 photocatalyst [107].
| Reaction Mode | Photocatalyst | Formation Rate (μmol·g−1h−1) | R (Electron) (μmol·g−1h−1) | Selectivity for CO2 Reduction (%) | ||
|---|---|---|---|---|---|---|
| CO | CH4 | H2 | ||||
| Solid–gas | TiO2 | 1.2 | 0.38 | 2.1 | 10 | 56 |
| solid–liquid | TiO2 | 0.80 | 0.11 | 5.3 | 13 | 19 |
| solid–gas | Pt-TiO2 | 1.1 | 5.2 | 33 | 110 | 40 |
| solid–liquid | Pt-TiO2 | 0.76 | 1.4 | 55 | 123 | 11 |
a Reaction conditions: catalyst, 0.020 g; CO2 pressure, 0.2 MPa; H2O, 4.0 mL; irradiation time, 10 h.
CO2 reduction over ALa4Ti4O15 (A = Ca, Sr and Ba) photocatalysts with various co-catalysts a [39].
| Photo-Catalyst | Band Gap/eV | Co-Catalyst (wt %) | Loading Method | Activity/μmol·h−1 | |||
|---|---|---|---|---|---|---|---|
| H2 | O2 | CO | HCOOH | ||||
| BaLa4Ti4O15 | 3.9 | none | - | 5.3 | 2.4 | 0 | 0 |
| BaLa4Ti4O15 | 3.9 | NiOx b (0.5) | impregnation | 58 | 29 | 0.02 | 0 |
| BaLa4Ti4O15 | 3.9 | Ru (0.5) | photodeposition | 84 | 41 | 0 | 0 |
| BaLa4Ti4O15 | 3.9 | Cu (0.5) | photodeposition | 96 | 45 | 0.6 | 0 |
| BaLa4Ti4O15 | 3.9 | Au (0.5) | photodeposition | 110 | 51 | 0 | 0 |
| BaLa4Ti4O15 | 3.9 | Ag (1.0) | photodeposition | 10 c | 7.0 c | 4.3 c | 0.3 c |
| CaLa4Ti4O15 | 3.9 | none | - | 1.3 | 0.6 | 0.07 | 0 |
| CaLa4Ti4O15 | 3.9 | Ag (1.0) | photodeposition | 5.6 | 2.1 | 2.3 | 1.3 |
| SrLa4Ti4O15 | 3.8 | none | - | 0.8 | 0.5 | 0.06 | 0 |
| SrLa4Ti4O15 | 3.8 | Ag (1.0) | photodeposition | 2.7 | 1.8 | 1.8 | 0.5 |
a Catalyst 0.3 g, water 360 mL, CO2 flow system (15 mL·min−1), a 400 W high-pressure mercury lamp, an inner irradiation quartz cell. b Pretreatment: Reduced at 673 K and subsequently oxidized at 473 K after impregnation (543 K for 1 h). c Initial activity.
Effect of loading method of Ag co-catalyst on the photocatalytic activity for CO2 reduction over ALa4Ti4O15 (A = Ca, Sr, and Ba) a [39].
| Photocatalyst | Loading Amount/wt % | Loading Method | Activity/μmol·h−1 | |||
|---|---|---|---|---|---|---|
| H2 | O2 | CO | HCOOH | |||
| BaLa4Ti4O15 | 1.0 | Impregnation b | 8.2 | 5.7 | 5.2 | 0.2 |
| BaLa4Ti4O15 | 1.0 | Impregnation b + H2 red c | 5.6 | 8.7 | 8.9 | 0.3 |
| BaLa4Ti4O15 | 0.5 | Liquid-phase reduction | 4.5 | 6.8 | 11 | 0.03 |
| BaLa4Ti4O15 | 1.0 | Liquid-phase reduction | 5.6 | 12 | 19 | 0.4 |
| BaLa4Ti4O15 | 2.0 | Liquid-phase reduction | 10 | 16 | 22 | 0.7 |
| BaLa4Ti4O15 | 3.0 | Liquid-phase reduction | 9.7 | 14 | 19 | 0.1 |
| BaLa4Ti4O15 | 5.0 | Liquid-phase reduction | 4.8 | 6.6 | 12 | 0.02 |
| BaLa4Ti4O15 | 1.0 | Liquid-phase reduction | 20 d | 11 d | 0 d | 0 d |
| SrLa4Ti4O15 | 1.0 | Liquid-phase reduction | 4.8 | 5.8 | 7.1 | 0.8 |
| CaLa4Ti4O15 | 1.0 | Liquid-phase reduction | 3.2 | 6.6 | 9.3 | 0.4 |
a Catalyst 0.3 g, water 360 mL, CO2 flow system (15 mL·min−1), a 400 W high-pressure mercury lamp, an inner irradiation quartz cell. b 723 K for 1 h, c 473 K for 2 h, d Ar flow.
Figure 4The schematic diagram is representing surface plasmon resonance in a spherical metal particle induced by the electric field component of incident light (adapted from [138]).
Figure 5(a) Schematic diagrams of bare Au, Au/TiO2 and the bare TiO2 photocatalysts, (b) amount of CH4 formed on these photocatalyst surfaces after 15 h and (c) the relevant redox potentials of CO2 and H2O under visible light and energy band positions of anatase TiO2 and Au (Adapted from [155]).
Figure 6Schematic diagram showing time dependence yields of CH4 and CO yields under visible light irradiation over Ag/AgIO3 particles and over N doped-TiO2. The inset shows the time dependence of CH4 and CO yields over AgIO3 under UV-vis light (Reproduced from [57]).
Figure 7Formation of the product over TiO2 (P25), Ag2SO3, and Ag/Ag2SO3 photocatalysts under visible light irradiation as a function of time (Reproduced from [62]).