Photocatalytic and photoelectrochemical CO2 reduction of artificial photosynthesis is a promising chemical process to solve resource, energy, and environmental problems. An advantage of artificial photosynthesis is that solar energy is converted to chemical products using abundant water as electron and proton sources. It can be operated under ambient temperature and pressure. Especially, photocatalytic CO2 reduction employing a powdered material would be a low-cost and scalable system for practical use because of simplicity of the total system and simple mass-production of a photocatalyst material.In this Account, single particulate photocatalysts, Z-scheme photocatalysts, and photoelectrodes are introduced for artificial photosynthetic CO2 reduction. It is indispensable to use water as an electron donor (i.e., reasonable O2 evolution) but not to use a sacrificial reagent of a strong electron donor, for achievement of the artificial photosynthetic CO2 reduction accompanied by ΔG > 0. Confirmations of O2 evolution, a ratio of reacted e- to h+ estimated from obtained products, a turnover number, and a carbon source of a CO2 reduction product are discussed as the key points for evaluation of photocatalytic and photoelectrochemical CO2 reduction.Various metal oxide photocatalysts with wide band gaps have been developed for water splitting under UV light irradiation. However, these bare metal oxide photocatalysts without a cocatalyst do not show high photocatalytic CO2 reduction activity in an aqueous solution. The issue comes from lack of a reaction site for CO2 reduction and competitive reaction between water and CO2 reduction. This raises a key issue to find a cocatalyst and optimize reaction conditions defining this research field. Loading a Ag cocatalyst as a CO2 reduction site and NaHCO3 addition for a smooth supply of hydrated CO2 molecules as reactant are beneficial for efficient photocatalytic CO2 reduction. Ag/BaLa4Ti4O15 and Ag/NaTaO3:Ba reduce CO2 to CO as a main reduction reaction using water as an electron donor even in just water and an aqueous NaHCO3 solution. A Rh-Ru cocatalyst on NaTaO3:Sr gives CH4 with 10% selectivity (Faradaic efficiency) based on the number of reacted electrons in the photocatalytic CO2 reduction accompanied by O2 evolution by water oxidation.Visible-light-responsive photocatalyst systems are indispensable for efficient sunlight utilization. Z-scheme systems using CuGaS2, (CuGa)1-xZn2xS2, CuGa1-xInxS2, and SrTiO3:Rh as CO2-reducing photocatalyst, BiVO4 as O2-evolving photocatalyst, and reduced graphene oxide (RGO) and Co-complex as electron mediator or without an electron mediator are active for CO2 reduction using water as an electron donor under visible light irradiation. These metal sulfide photocatalysts have the potential to take part in Z-scheme systems for artificial photosynthetic CO2 reduction, even though their ability to extract electrons from water is insufficient.A photoelectrochemical system using a photocathode is also attractive for CO2 reduction under visible light irradiation. For example, p-type CuGaS2, (CuGa)1-xZn2xS2, Cu1-xAgxGaS2, and SrTiO3:Rh function as photocathodes for CO2 reduction under visible light irradiation. Moreover, introducing a conducting polymer as a hole transporter and surface modification with Ag and ZnS improve photoelectrochemical performance.
Photocatalytic and photoelectrochemical CO2 reduction of artificial photosynthesis is a promising chemical process to solve resource, energy, and environmental problems. An advantage of artificial photosynthesis is that solar energy is converted to chemical products using abundant water as electron and proton sources. It can be operated under ambient temperature and pressure. Especially, photocatalytic CO2 reduction employing a powdered material would be a low-cost and scalable system for practical use because of simplicity of the total system and simple mass-production of a photocatalyst material.In this Account, single particulate photocatalysts, Z-scheme photocatalysts, and photoelectrodes are introduced for artificial photosynthetic CO2 reduction. It is indispensable to use water as an electron donor (i.e., reasonable O2 evolution) but not to use a sacrificial reagent of a strong electron donor, for achievement of the artificial photosynthetic CO2 reduction accompanied by ΔG > 0. Confirmations of O2 evolution, a ratio of reacted e- to h+ estimated from obtained products, a turnover number, and a carbon source of a CO2 reduction product are discussed as the key points for evaluation of photocatalytic and photoelectrochemical CO2 reduction.Various metal oxide photocatalysts with wide band gaps have been developed for water splitting under UV light irradiation. However, these bare metal oxide photocatalysts without a cocatalyst do not show high photocatalytic CO2 reduction activity in an aqueous solution. The issue comes from lack of a reaction site for CO2 reduction and competitive reaction between water and CO2 reduction. This raises a key issue to find a cocatalyst and optimize reaction conditions defining this research field. Loading a Ag cocatalyst as a CO2 reduction site and NaHCO3 addition for a smooth supply of hydrated CO2 molecules as reactant are beneficial for efficient photocatalytic CO2 reduction. Ag/BaLa4Ti4O15 and Ag/NaTaO3:Ba reduce CO2 to CO as a main reduction reaction using water as an electron donor even in just water and an aqueous NaHCO3 solution. A Rh-Ru cocatalyst on NaTaO3:Sr gives CH4 with 10% selectivity (Faradaic efficiency) based on the number of reacted electrons in the photocatalytic CO2 reduction accompanied by O2 evolution by water oxidation.Visible-light-responsive photocatalyst systems are indispensable for efficient sunlight utilization. Z-scheme systems using CuGaS2, (CuGa)1-xZn2xS2, CuGa1-xInxS2, and SrTiO3:Rh as CO2-reducing photocatalyst, BiVO4 as O2-evolving photocatalyst, and reduced graphene oxide (RGO) and Co-complex as electron mediator or without an electron mediator are active for CO2 reduction using water as an electron donor under visible light irradiation. These metal sulfide photocatalysts have the potential to take part in Z-scheme systems for artificial photosynthetic CO2 reduction, even though their ability to extract electrons from water is insufficient.A photoelectrochemical system using a photocathode is also attractive for CO2 reduction under visible light irradiation. For example, p-type CuGaS2, (CuGa)1-xZn2xS2, Cu1-xAgxGaS2, and SrTiO3:Rh function as photocathodes for CO2 reduction under visible light irradiation. Moreover, introducing a conducting polymer as a hole transporter and surface modification with Ag and ZnS improve photoelectrochemical performance.
.[1] Ag-cocatalyst
for an effective active site for CO2 reduction and Ag/BaLa4Ti4O15 photocatalyst for CO2 reduction to form CO as a main reduction product using water as
an electron donor even in an aqueous solution..[2] Ag/NaTaO3 photocatalyst doped with
alkaline earth cations for CO2 reduction to CO with 90%
of selectivity in an aqueous solution with a basic salt for enhancement
of hydrated CO2 molecules supply..[3] Z-scheme system composed of CuGaS2 as a reducing photocatalyst and RGO–(CoO/BiVO4) as an O2-evolving photocatalyst
for CO2 reduction to CO using water as an electron donor
under visible light irradiation in an aqueous powder suspension system..[4] Employing (CuGa)0.5ZnS2 prepared by a flux method in Z-scheme and
photoelectrochemical systems with tuning a reactant solution for efficient
and stable CO2 reduction to form CO with 10–20%
selectivity using water as an electron donor under visible light.
Introduction
Carbon
dioxide capture storage and utilization technology (CCSU)
has been encouraged, because CO2 emission control is a
critical issue in the world. Ideally, CO2 fixation should
be realized utilizing renewable energies, such as solar energy, as
follows:hydrogenation of CO2 using solar hydrogenbiological
CO2 fixationelectrochemical
CO2 reduction utilizing a
photovoltaic cellphotocatalytic and
photoelectrochemical CO2 reduction directly utilizing solar
lightThere are advantages and disadvantages
to each reaction. Hydrogenation
of CO2 can produce various beneficial chemical compounds
with high CO2 conversion efficiency through a thermal catalytic
process on an industrial scale. Much knowledge toward CO2 hydrogenation has been accumulated in C1 chemistry so far. The hydrogen
should be supplied from solar hydrogen production by water splitting
with no consumption of fossil resources and no CO2 emission
but not from steam reforming of fossil resources. However, the CO2 conversion process requires high temperature and pressure
to operate the catalytic process. Biological CO2 fixation
is based on natural photosynthesis by plants. Natural photosynthesis
involves almost no energy loss for absorbed photon energy conversion.
However, the solar energy conversion efficiency is limited because
a plant absorbs only a part of the solar spectrum as indicated by
its green color. Electrochemical CO2 reduction is also
interesting from the viewpoint of electrocatalysis. The reduction
products and the selectivity change with electrode materials even
under the same electrolysis conditions. However, electrolyzers and
batteries are indispensable for the electrochemical system in addition
to a photovoltaic cell. Photocatalytic and photoelectrochemical CO2 reduction utilizing solar energy in an aqueous solution is
one of the ideal chemical reactions for artificial photosynthesis,
because solar energy is directly converted and stored as chemical
products. Artificial photosynthesis can be operated under ambient
temperature and pressure to produce solar fuels and chemicals and
can exceed natural photosynthesis in solar energy conversion efficiency.
Especially, a powder-based photocatalyst is attractive because it
can be employed for a low-cost and scalable system aimed at artificial
photosynthesis.[5]In this Account,
we introduce several types of CO2 reduction
systems, mainly based on particulate photocatalyst materials, using
water as an electron donor. Key points for evaluation of photocatalytic
and photoelectrochemical CO2 reduction are also discussed.
Overview of Photocatalytic and Photoelectrochemical
CO2 Reduction Systems for Artificial Photosynthesis
Figure shows various
types of photocatalytic and photoelectrochemical systems for artificial
photosynthesis.[6,7] The first is a single-particulate
photocatalyst system via one-photon excitation, in which photocatalytic
reduction by photogenerated electrons and photocatalytic oxidation
by photogenerated holes proceed on one particle (Figure a).[6−9] Photocatalysts of semiconductor
materials have a band structure in which a conduction band (CB) is
separated from a valence band (VB) with a band gap (BG). The thermodynamic
relationship between the band structure of a photocatalyst and the
redox potential for the objective reaction is important. The equilibrium
potentials relative to the normal hydrogen electrode (NHE) at pH 7
and 298 K for CO2 reduction and water splitting are as
follows:The conduction band minimum and valence
band
maximum should locate at more negative and positive levels than redox
potentials of objective reactions such as water splitting and CO2 reduction, respectively. When the energy of the incident
photon is larger than that of the band gap, electrons and holes are
photogenerated in the conduction band and the valence band, respectively.
The photogenerated electrons reduce water and CO2 to generate
H2 and CO2 reduction products such as CO, while
the photogenerated holes oxidize water to form O2. The
O2 evolution is a key issue for photocatalytic CO2 reduction using water as an electron donor. Moreover, since CO2 reduction competes with water reduction, selective CO2 reduction is also challenging from the viewpoints of not
only thermodynamics but also kinetics. Therefore, the catalytic ability
of photocatalyst surface is also a key issue.
Figure 1
Artificial photosynthetic
CO2 reduction based on a powdered
photocatalyst by (a) a single-particulate system, (b) a Z-scheme system,
(c) a photoelectrochemical system using a photocathode, and (d) a
photoelectrochemical system combining a photocathode and a photoanode.
Artificial photosynthetic
CO2 reduction based on a powdered
photocatalyst by (a) a single-particulate system, (b) a Z-scheme system,
(c) a photoelectrochemical system using a photocathode, and (d) a
photoelectrochemical system combining a photocathode and a photoanode.The second is a Z-scheme system via a two-photon
excitation process
consisting of a reducing photocatalyst, an oxidizing photocatalyst,
and an electron mediator (Figure b).[10−13] This system mimics natural photosynthesis by a plant. Various photocatalysts
that are active for either photocatalytic reduction of water and CO2 reduction or photocatalytic oxidation of water can be employed
to make a Z-scheme system. From this viewpoint, it is meaningful to
test photocatalytic CO2 reduction using sacrificial electron
donors such as organic compounds and S2– in order
to find potential CO2-reducing photocatalysts in a part
of the Z scheme system, though the sacrificial reaction becomes a
downhill reaction (ΔG < 0).The third
is a photoelectrochemical cell.[7] n-Type
and p-type semiconductors may function as O2-evolving
photoanodes and photocathodes to give H2 and reduction
products of CO2, respectively. The photoelectrochemical
cell can be constructed by combining a photoelectrode of a working
electrode with a counter electrode (Figure c) or combining a photoanode and a photocathode
working via two-photon excitation (Figure d). External bias can be applied between
the photoanode and photocathode to enhance the photoelectrochemical
reaction. However, the external bias should be smaller than the theoretical
voltage of electrolysis of an objective reaction to achieve artificial
photosynthesis from light energy conversion.In the following
sections, several types of the photocatalytic
and photoelectrochemical systems shown in Figure are introduced.
Single
Particulate Photocatalysts with Wide
Band Gaps for CO2 Reduction Using Water as an Electron
Donor (Figure a)
Ag Cocatalyst
for CO Formation by Photocatalytic
CO2 Reduction
CO2 reduction over metal
oxide photocatalysts has extensively been investigated. Although TiO2 has widely been studied for photocatalytic CO2 reduction, those reports involve critical issues such as lack of
quantification of O2 and small amounts of reduction products
such as CH4 due to low activities. Ishitani et al. reported
that CH4 could come from contaminants adsorbed on TiO2.[14] In contrast, Sayama and Arakawa
have reported that a ZrO2 photocatalyst (BG = 5.0 eV) produced
CO, H2, and O2 in stoichiometric amounts in
an aqueous medium.[15] Moreover, loading
a Cu cocatalyst and adding a bicarbonate ion enhanced the photocatalytic
CO2 reduction. This is the first report to demonstrate
photocatalytic CO2 reduction using water as an electron
donor over a particulate photocatalyst. However, the major reduction
product was H2 and the selectivity for CO formation (CO/(H2 + CO)) was about 12%. In such a background, the author found
a highly active Ag cocatalyst for photocatalytic CO2 reduction
to form CO with highly active photocatalysts for water splitting.BaLa4Ti4O15 (BG = 3.9 eV) photocatalyst
with a layered perovskite structure was first chosen because NiO/BaLa4Ti4O15 efficiently split water.[16] The particle
is plate shaped in which an edge plane and a basal plane are reduction
and oxidation site, respectively, as shown in Figure A. The separation of the reduction site from
the oxidation site is beneficial for an uphill reaction, because a
back reaction of a downhill reaction is suppressed. Ag was found to
be a highly active cocatalyst for photocatalytic CO2 reduction
to form CO as shown in Table .[1] To compare photocatalytic CO2 reduction abilities, not only the production rate [mol h–1] but also the selectivity for CO2 reduction
are essential values. The selectivity is calculated according to eq .The
selectivity and the production rate based
on the number of reacted electrons are similar to Faradaic efficiency
and partial current density, respectively, in an electrochemical reaction.
It is noteworthy that CO is the main reduction product with about
70% selectivity, rather than H2, even in an aqueous medium
(Table ). A small
amount of HCOOH was also obtained. It is reasonable that Ag functions
as an efficient cocatalyst to form CO judging from its electrocatalysis
in aqueous CO2 solution.[17,18] The high conduction
band level of BaLa4Ti4O15 should
be important to get an enough driving force for CO2 reduction
and high energy potential of photogenerated electrons applied to the
Ag cocatalyst. A liquid-phase reduction method gives higher activity
for CO formation than photodeposition and impregnation methods for
the Ag cocatalyst loading. There is concern that the Ag cocatalyst
may efficiently reduce O2 produced by water splitting.
However, O2 reduction on the Ag cocatalyst is suppressed
more or less, because the reaction is conducted under CO2 flow conditions smoothly removing the O2 from the reaction
system.
Figure 2
(A) SEM images of Ag/BaLa4Ti4O15 before and after photocatalytic CO2 reduction, and the
proposed mechanism. (B) Photocatalytic CO2 reduction using
water as an electron donor under UV light irradiation over Ag(2 wt
%)/BaLa4Ti4O15.[1] Photocatalyst, 0.3 g; reactant solution, water (360 mL);
flow gas, CO2 (1 atm); light source, 400 W high-pressure
mercury lamp; reaction cell, inner irradiation quartz cell. Reproduced
with permission from ref (1). Copyright 2011 American Chemical Society.
Table 1
Effect of Cocatalyst on CO2 Reduction Using
Water as an Electron Donor under UV Light Irradiation
over BaLa4Ti4O15 Photocatalyst[1]a
activity [μmol h–1]
cocatalyst (wt %)
loading
method
H2
O2
CO
HCOOH
CO selectivity
(%)
e–/h+
none
5.3
2.4
0
0
0
1.1
NiOx (0.5)
impregnationb
58
29
0.02
0
0.03
1.0
Ru (0.5)
photodeposition
84
41
0
0
0
1.0
Cu
(0.5)
photodeposition
96
45
0.6
0
0.6
1.1
Au (0.5)
photodeposition
110
51
0
0
0
1.1
Ag
(1.0)
photodeposition
10
7.0
4.3
0.3
30
1.0
Ag (1.0)
impregnation
8.2
5.7
5.2
0.2
38
1.2
Ag
(1.0)
impregnation
+ H2 reduction
5.6
8.7
8.9
0.3
60
0.9
Ag
(1.0)
liquid-phase
reduction
5.6
12
19
0.4
76
1.0
Photocatalyst,
0.3 g; reactant solution,
water (360 mL); flow gas, CO2 (1 atm); light source, 400
W high-pressure mercury lamp; reaction cell, inner irradiation quartz
cell.
Treated with H2 reduction
and subsequent oxidation.
(A) SEM images of Ag/BaLa4Ti4O15 before and after photocatalytic CO2 reduction, and the
proposed mechanism. (B) Photocatalytic CO2 reduction using
water as an electron donor under UV light irradiation over Ag(2 wt
%)/BaLa4Ti4O15.[1] Photocatalyst, 0.3 g; reactant solution, water (360 mL);
flow gas, CO2 (1 atm); light source, 400 W high-pressure
mercury lamp; reaction cell, inner irradiation quartz cell. Reproduced
with permission from ref (1). Copyright 2011 American Chemical Society.Photocatalyst,
0.3 g; reactant solution,
water (360 mL); flow gas, CO2 (1 atm); light source, 400
W high-pressure mercury lamp; reaction cell, inner irradiation quartz
cell.Treated with H2 reduction
and subsequent oxidation.Figure A shows
SEM images of Ag-cocatalyst before and after photocatalytic CO2 reduction and a reaction mechanism. BaLa4Ti4O15 is a plate-like particle with layered perovskite
structure. Ag particles of ∼10 nm diameter are loaded on both
edge and basal plane by the liquid-phase reduction as prepared. After
photocatalytic CO2 reduction, the number of the Ag cocatalyst
particles on the edge increases while Ag particles on the basal plane
disappear, because Ag on the basal plane dissolves by photooxidation
and is subsequently photodeposited on the edge by photoreduction during
the photocatalytic CO2 reduction.Figure B shows
time courses of CO, H2, and O2 evolution by
photocatalytic CO2 reduction over Ag/BaLa4Ti4O15. The time courses demonstrate not only activity
and durability but also other important points to evaluate photocatalytic
CO2 reduction as discussed below.It is important
to see if O2 evolves in a stoichiometric
amount when the photocatalytic reaction is conducted using water as
an electron donor for light energy conversion without any strong sacrificial
electron donors. CO2 is reduced by photogenerated electrons
on a photocatalyst, while photocatalytic oxidation of water by photogenerated
holes simultaneously proceeds as the counterpart as shown in Figures a and 2B. It is also important to see if the ratio of reacted electrons
to holes estimated from products is unity according to eq .Unity means that reduction and oxidation products
are obtained in a stoichiometric amount. If the e–/h+ is not unity, side reactions or noncatalytic but quantitative
reactions such as reduction or oxidation of the photocatalyst itself
may proceed. In addition, it is necessary to pay attention to whether
some products are not detected by the measurement technique employed.
The O2 evolution with at unity e–/h+ ratio is satisfied for the present photocatalytic CO2 reduction over Ag/BaLa4Ti4O15 as shown in Table and Figure B.Photocatalytic reaction must proceed by irradiation the energy
of which is larger than the band gap energy. The band gap of BaLa4Ti4O15 is 3.9 eV, which corresponds
to about 320 nm light. This photocatalyst works with use of a quartz
reaction cell with a suitable UV lamp, while the activity is negligible
using a Pyrex reaction cell. This result indicates that the photoresponse
of the BaLa4Ti4O15 photocatalyst
is reasonable.Turnover number defined by eq is also an important indicator to consider
if the
reaction proceeds photocatalytically.Turnover number (TON) indicates how
many atoms
or molecules react on one active site. TON based on the number of
reacted electrons is often used for photocatalysis accompanied by
redox reactions according to eq .If the TON is too small, we cannot
guarantee
that it is a photocatalytic reaction because not catalytic but quantitative
reactions on the surface of photocatalyst cannot be excluded. In a
heterogeneous photocatalyst, the molar quantity of the active site
is often replaced with the molar quantity of an employed photocatalyst,
because it is difficult to estimate the number of actual active sites
on the surface of a photocatalyst. In some cases, the molar quantities
of atoms on the surface, dopant, and cocatalyst are used for the denominator.
The TON should be above unity to prove that the reaction proceeds
catalytically. Photocatalytic CO2 reduction over Ag/BaLa4Ti4O15 proceeds steadily under UV light
irradiation and TON to photocatalyst and cocatalyst reach 1.6 and
7.7, respectively, at 7 h being above unity as shown in Figure B.Products of CO and
HCOOH among others must originate from CO2. However, contaminants
on the photocatalyst and some carbon
materials constituting the photocatalyst system may become a carbon
source.[14,19] Therefore, confirmation of the carbon source
of the obtained products is necessary. One approach is an isotope
experiment using 13CO2. Another is a control
experiment using an inert gas to confirm that carbon products are
not obtained. The reactant solution conditions (i.e., pH) of the control
experiment should be similar to those of CO2 reduction.
When 13CO2 is flowed for a photocatalytic reaction
over Ag/BaLa4Ti4O15, 13CO is obtained while 12CO is not. In addition, CO is not
obtained when Ar instead of CO2 is supplied. These two
results prove CO2 is the carbon source.Thus, it
is concluded by confirmations of O2 evolution,
the ratio of reacted e– to h+ estimated
from obtained products, the TON, and the carbon source that the CO2 reduction photocatalytically proceeds using water as an electron
donor over Ag/BaLa4Ti4O15.
Effect of HCO3– in Water on Photocatalytic
CO2 Reduction
La
or alkaline earth metal doped NaTaO3 (BG = 4.1 eV) with
a perovskite structure is also a unique photocatalyst. The doped NaTaO3 has a surface nanostep structure in which a reduction site
is separated from an oxidation site.[20,21] While NiO/NaTaO3 with dopant splits water efficiently but does not reduce
CO2, Ag/NaTaO3:Ba gives CO with about 50% selectivity
under UV light upon flowing CO2 into pure water.[2] Moreover, with addition of a basic salt into
the reactant solution, CO formation rate drastically increases and
the selectivity reaches about 90% even in an aqueous solution (Figure A). The enhancement
of CO2 reduction with salt addition is due to efficient
supply of hydrated CO2 molecule reactant and pH control.
Figure 3
(A) Photocatalytic
CO2 reduction using water as an electron
donor under UV light irradiation over Ag/NaTaO3:Ba. Reactant
solution, NaHCO3(aq) (360 mL); flow gas, CO2 (1 atm); light source, 400 W high-pressure mercury lamp; reaction
cell, an inner irradiation quartz cell. (B) Proposed mechanism of
photocatalytic CO2 reduction in the presence of NaHCO3.[2] Reproduced with permission from
ref (2). Copyright
2017 Wiley.
(A) Photocatalytic
CO2 reduction using water as an electron
donor under UV light irradiation over Ag/NaTaO3:Ba. Reactant
solution, NaHCO3(aq) (360 mL); flow gas, CO2 (1 atm); light source, 400 W high-pressure mercury lamp; reaction
cell, an inner irradiation quartz cell. (B) Proposed mechanism of
photocatalytic CO2 reduction in the presence of NaHCO3.[2] Reproduced with permission from
ref (2). Copyright
2017 Wiley.A proposed mechanism of photocatalytic
CO2 reduction
over Ag/NaTaO3:Ba in the presence of a basic additive is
shown in Figure B.
It was confirmed that not HCO3– or CO32– but a hydrated CO2 molecule
is a reactant in photocatalytic CO2 reduction as in electrochemical
CO2 reduction. HCO3– functions
as a buffer for supply of hydrated CO2 molecules. After
the CO2 adsorbs on the Ag-cocatalyst to make CO2•–(ad), CO evolves through path
A (hydrogenation of CO2•–(ad)) or path B (reduction of COOH(ad)). Water is
photooxidized to form O2 on the photocatalyst surface.
Thus, adding a basic salt is key for efficient photocatalytic CO2 reduction with smooth supply of hydrated CO2 molecules.
Ag Cocatalyst-Loaded Photocatalysts for Single
Particulate Photocatalytic CO2 Reduction to Form CO
Various metal oxide photocatalysts with different components and
crystal structure have been developed for CO2 reduction
based on loading Ag cocatalyst and adding NaHCO3 strategies
from our group as shown in Table , for example, CaTa4O11,[22] LaTa7O19,[22] and KCaSrTa5O15[23,24] photocatalysts. In addition, many metal oxide photocatalysts with
wide band gaps have been reported for CO2 reduction such
as La2Ti2O7,[25] CaTiO3,[26] SrTiO3:Al,[27] Ga2O3:Zn,[28] and ZnGa2O4/Ga2O3[29] with the Ag cocatalyst
from other groups. Substitution of elements is also a beneficial approach
to develop new photocatalysts for CO2 reduction as well
as for water splitting. For example, KCaSrTa5O15 (BG = 4.1 eV) has a tungsten bronze structure, which is similar
to a defect type of perovskite structure (A1–BO3). K, Ca, and Sr at an A site in KCaSrTa5O15 can be replaced with various other cations.
SrKNaTa5O15 and K2RETa5O15 (RE = rear earth metal) obtained by
the substitution are also active for photocatalytic CO2 reduction.[30−32]
Table 2
Single Particulate Photocatalysts
with Wide Band Gaps for CO2 Reduction Using Water as an
Electron Donor[1,2,22−24]a
Rh–Ru Cocatalyst for CH4 Formation
by Photocatalytic CO2 Reduction
Although
many photocatalysts have been developed for CO2 reduction
as mentioned above, obtained products are limited to two-electron
reduction products such as CO and HCOOH. Therefore, it is challenging
to demonstrate CO2 reduction to form CH4, an
eight-electron reduction product, using water as an electron donor.
Rh–Ru/NaTaO3:Sr(1%) continuously produces CH4, H2, and O2 under UV irradiation.[33] The selectivity for CH4 formation
based on the number of reacted electrons is about 10%. The e–/h+ ratio estimated from obtained products is 1.1, and
TON based on CH4 formation with Rh and Ru cocatalysts is
2.0. No CH4 is obtained under Ar rather than CO2 flow. These results prove that CH4 is obtained by photocatalytic
CO2 reduction using water as an electron donor over the
Rh–Ru/NaTaO3:Sr(1%).
Z-Scheme
CO2 Reduction Using Water
as an Electron Donor under Visible Light Irradiation (Figure b)
It is a key issue to construct visible light
responsive CO2 reduction system using water as an electron
donor for efficient
sunlight utilization beyond the wide band gap photocatalysts. In this
section, visible light responsive photocatalysts for CO2 reduction in the presence of a sacrificial electron donor (Table ) and application
of those photocatalysts to Z-scheme systems for CO2 reduction
using water as an electron donor under visible light (Table ) are introduced.
Table 3
Sacrificial CO2 Reduction
Using Metal Sulfide Photocatalysts under Visible Light Irradiation[19]a
activity [μmol h–1]
metal sulfide
crystal structure
BG, EG [eV]
electron
donor
H2
CO
HCOOH
CuGaS2
chalcopyrite
2.3
K2SO3
11
0.25
trace
(AgInS2)0.22–(ZnS)1.56
wurtzite
2.3
Na2S + K2SO3
16
0.01
0
(AgInS2)0.1–(ZnS)1.8
wurtzite
2.6
Na2S
23
0.06
0.10
Ag2ZnGeS4
stannite
2.5
Na2S
38
0
0.14
ZnS:Ni(0.1%)
wurtzite + zinc blend
2.3
Na2S
22
trace
4.0
ZnS:Pb(1.0%)
wurtzite + zinc blend
2.4
Na2S
47
0.02
0.96
(ZnS)0.9–(CuCl)0.1
zinc blende
2.9
Na2S
140
0.01
0
ZnGa0.5In1.5S4
layered
2.7
Na2S
14
0.01
0
Photocatalyst, 0.2–0.3 g;
reactant solution, 0.05–0.1 mol L–1 Na2S or 0.1 mol L–1 K2SO3(aq) (120–150 mL) or both; gas, CO2 (1 atm); light
source, 300 W Xe lamp (λ > 420 nm); irradiation area, 33
cm2. BG = band gap, EG = energy gap.
Table 4
Z-Scheme Photocatalyst
Systems for
CO2 Reduction Using Water as an Electron Donor under UV
or Visible Light Irradiation[3,4,19,43,46]a
activity [μmol h–1]
entry
reducing
photocatalyst
O2-evolving photocatalyst
mediator
additive (mmol L–1)
H2
O2
CO
CO selectivity
(%)
e–/h+
1
CuGaS2
RGO–TiO2
RGO
none
28.8
11.2
0.15
0.5
1.29
2
CuGaS2
RGO–(CoOx/BiVO4)
RGO
none
3.1
1.3
0.04
1.3
1.21
3
Cu0.8Ag0.2GaS2
RGO–(CoOx/BiVO4)
RGO
NaHCO3 (1)
4.0
1.6
0.03
0.7
1.26
4
CuGa0.8In0.2S2
RGO–(CoOx/BiVO4)
RGO
NaHCO3 (1)
3.5
1.6
0.04
1.1
1.11
5
(CuGa)0.5ZnS2
RGO–(CoOx/BiVO4)
RGO
NaHCO3 (1)
3.5
1.9
0.4
11
1.04
6
(CuGa)0.5ZnS2
RGO–(CoOx/BiVO4)
RGO
NaHCO3 (10)
12.0
6.4
1.8
13
1.08
7
(CuGa)0.5ZnS2
RGO–(CoOx/BiVO4)
RGO
KHCO3 (10)
8.1
4.6
2.1
20
1.11
8
(CuGa)0.5ZnS2
RGO–(CoOx/BiVO4)
RGO
NaHCO3 (100)
8.9
3.5
3.2
26
1.73
9
[Ru(dpbpy)]/(CuGa)0.3Zn1.4S2
BiVO4
Co[(tpy)2]3+/2+
NaHCO3 (250)
1.7
0.8
2.7
56
3.00
10
SrTiO3:Rh
BiVO4
none
none
8.7
4.0
0.018
0.2
1.09
11
Au/SrTiO3:Rh
BiVO4
none
none
3.5
1.9
0.031
0.9
0.93
Photocatalyst, 0.1–0.4 g;
reactant solution, water (120–150 mL); flow gas, CO2 (1 atm); light source, 300 W Xe lamp (λ > 300 nm for TiO2 and λ > 420 nm for BiVO4 systems); irradiation
area, 33 cm2.
Photocatalyst, 0.2–0.3 g;
reactant solution, 0.05–0.1 mol L–1 Na2S or 0.1 mol L–1 K2SO3(aq) (120–150 mL) or both; gas, CO2 (1 atm); light
source, 300 W Xe lamp (λ > 420 nm); irradiation area, 33
cm2. BG = band gap, EG = energy gap.Photocatalyst, 0.1–0.4 g;
reactant solution, water (120–150 mL); flow gas, CO2 (1 atm); light source, 300 W Xe lamp (λ > 300 nm for TiO2 and λ > 420 nm for BiVO4 systems); irradiation
area, 33 cm2.
Visible-Light Responsive Metal Sulfide Photocatalysts
for CO2 Reduction Using Sacrificial Electron Donor
Metal sulfide photocatalysts are active for not only water reduction
but also CO2 reduction under visible light using a sacrificial
electron donor. For example, CdS is active for sacrificial CO2 reduction to form CO in an aqueous solution containing a
sacrificial reagent.[34,35] Metal sulfides with various crystal
structures have also been developed for sacrificial CO2 reduction under visible light irradiation as shown in Table .[19] CuGaS2 and ZnS:Ni photocatalysts are highly active for
CO and HCOOH formation, respectively. However, these CO2 reductions are not artificial photosynthesis because strong sacrificial
electron donors are used. Since they cannot oxidize water into O2 because of self-photooxidation (photocorrosion), single particulate
overall water splitting and CO2 reduction accompanied by
O2 evolution by water oxidation as shown in Figure a is difficult. Construction
of Z-scheme systems is a beneficial approach to employ metal sulfide
photocatalysts showing CO2 reduction activity combined
with an O2-evolving photocatalyst as shown in Figure b.
Z-Scheme System Employing RGO as a Solid-State
Electron Mediator (Figure A(a))
A Z-scheme system consisting of CuGaS2 as a reducing photocatalyst, TiO2 as an O2-evolving photocatalyst, and reduced graphene oxide (RGO) as a solid-state
electron mediator is active for not only water splitting[36] but also CO2 reduction to form CO
(Table , entry 1).[19] The carbon source for the CO2 reduction
product should carefully be checked, because RGO is a carbon material. 13CO formed under 13CO2 flow, indicating
that flowed CO2 was the carbon source. However, 12CO was obtained in addition to the 13CO. Moreover, a small
amount of CO formed even under Ar gas instead of CO2. So,
a part of CO formed by Z-scheme CO2 reduction, whereas
other CO formed by photooxidation of RGO on TiO2. The Z-scheme
system works only under UV light because of limitations of TiO2. When visible light responsive RGO–(CoO/BiVO4) is employed instead of RGO–TiO2, Z-scheme CO2 reduction to form CO proceeds using
water as an electron donor under visible light in an aqueous suspension
(Table entry 2).[3] CO is not obtained under Ar flow in the Z-scheme
system composed of RGO–(CoO/BiVO4) unlike that using RGO–TiO2. The inhibition
of RGO oxidation is due to less oxidation power of holes photogenerated
in the valence band of BiVO4 than that of TiO2.Making a solid solution based on CuGaS2 with p-type
character is beneficial to developing a reducing photocatalyst, because
the band structure is tunable by a change in the composition of the
solid solution.[6,37] For example, solid solutions
of CuGaS2 with CuInS2 can absorb longer wavelengths
of visible light than CuGaS2, because In 5s5p orbitals
of CuInS2 lower the conduction band consisting of Ga 4s4p
orbitals of CuGaS2 resulting in band gap narrowing. Red-powdered
CuGa0.8In0.2S2, which absorbs visible
light up to 600 nm functions as a CO2-reducing photocatalyst
in the Z-scheme system (Table , entry 4). Making a (CuGa)1–Zn2S2 solid solution
between CuGaS2 and ZnS improves CuGaS2 performance,
though the band gap does not become narrower than that of CuGaS2.[38] The Z-scheme system using (GuGa)0.5ZnS2 prepared by a solid-state reaction (SSR)
combined with RGO–(CoO/BiVO4) shows higher water splitting and CO2 reduction
activities than that using CuGaS2 prepared by SSR (Figure B). When the (CuGa)0.5ZnS2 particle
is prepared by a flux method, fine particles of (CuGa)0.5ZnS2 with a few hundreds of nanometers in size are obtained,
while the particle size when prepared by conventional SSR is about
1 μm.[39] When the fine particulate
(CuGa)0.5ZnS2 is applied to a Z-scheme system,
photocatalytic water splitting and CO2 reduction are much
enhanced (Figure B).[4] The Z-scheme CO2 reduction activity
strongly depends on the reactant solution conditions (Table , entries 5–8). Addition
of a basic salt not only stabilizes but also enhances Z-scheme CO2 reduction because of efficient supply of hydrated CO2 to the photocatalyst surface. We stress that the selectivity
for CO formation in the Z-scheme CO2 reduction reaches
10–20% even using bare metal sulfide without surface modification.
Although a Ag cocatalyst is effective for CO2 reduction
to form CO over wide band gap metal oxides as mentioned in section , Ag on a metal
sulfide does not enhance CO formation in the Z-scheme CO2 reduction at the present stage, probably due to poisoning of the
Ag surface by sulfurization. Therefore, further highly selective CO2 reduction is expected by introducing a suitable active site
and surface modification of the metal sulfide photocatalyst for Z-scheme
CO2 reduction.
Figure 4
(A) Various types of Z-scheme photocatalysts
for CO2 reduction using water as an electron donor. (B)
Z-scheme CO2 reduction under visible light irradiation
using CuGaS2 or (CuGa)0.5ZnS2 prepared
by a SSR
or a flux method combined with RGO–(CoO/BiVO4). Reproduced with permission from ref (4). Copyright 2022 American
Chemical Society. (C) Z-scheme CO2 reduction under visible
light irradiation using [Ru(dpbpy)]/(CuGa)0.3Zn1.4S2, BiVO4, and [Co(tpy)2]3+/2+. Reproduced with permission from ref (43). Copyright 2018 The Royal Society of Chemistry.
Photocatalyst, 0.1–0.4 g; reactant solution, NaHCO3(aq) (120–150 mL); flow gas, CO2 (1 atm); light source,
300 W Xe lamp (λ > 420 nm); irradiation area, 33 cm2.
(A) Various types of Z-scheme photocatalysts
for CO2 reduction using water as an electron donor. (B)
Z-scheme CO2 reduction under visible light irradiation
using CuGaS2 or (CuGa)0.5ZnS2 prepared
by a SSR
or a flux method combined with RGO–(CoO/BiVO4). Reproduced with permission from ref (4). Copyright 2022 American
Chemical Society. (C) Z-scheme CO2 reduction under visible
light irradiation using [Ru(dpbpy)]/(CuGa)0.3Zn1.4S2, BiVO4, and [Co(tpy)2]3+/2+. Reproduced with permission from ref (43). Copyright 2018 The Royal Society of Chemistry.
Photocatalyst, 0.1–0.4 g; reactant solution, NaHCO3(aq) (120–150 mL); flow gas, CO2 (1 atm); light source,
300 W Xe lamp (λ > 420 nm); irradiation area, 33 cm2.
Z-Scheme
System Employing a Co-Complex as
an Electron Mediator (Figure A(b))
Metal complexes have been widely examined as
selective CO2-reducing catalysts in electrochemistry, coordination
chemistry, and photochemistry.[40,41] Recently, hybrid systems
combining a metal complex catalyst with semiconductor photocatalyst
materials have been studied for highly selective CO2 reduction
in photoelectrochemical and photocatalytic systems.[42] For example, Z-scheme CO2 reduction under visible
light has been demonstrated using [Ru(dpbpy)]-loaded (CuGa)0.3Zn1.4S2, BiVO4, and a Co-complex
as an electron mediator (Figure C).[43] CO evolves as a main
reduction product with introduction of the highly active Ru-complex
catalyst for CO2 reduction on (CuGa)0.3Zn1.4S2. HCOOH is also produced in the reaction. The
catalytic activity of a metal complex is usually inhibited in the
presence of O2. Therefore, it is notable that CO2 reduction and simultaneous O2 evolution proceed even
using a metal complex catalyst with a semiconductor photocatalyst
in an aqueous solution, though the amount of O2 is small
compared with a stoichiometric amount.
Z-Scheme
System Driven by Interparticle Electron
Transfer without an Electron Mediator (Figure A(c))
SrTiO3:Rh shows
high sacrificial H2 evolution activity, though it does
not oxidize water into O2.[44] However, SrTiO3:Rh can be employed to construct a Z-scheme
system working via interparticle electron transfer with BiVO4 without an electron mediator (Figure A(c)).[45,46] The Z-scheme system reduces CO2 to CO accompanied by H2 and O2 under
visible light. Loading Ag or Au cocatalyst on SrTiO3:Rh
improves the CO evolution activity (Table , entries 10, 11). The suitable pH is around
4, because SrTiO3:Rh and BiVO4 particles aggregate
well with each other to get good contact between the particles, resulting
in smooth electron transfer from BiVO4 to SrTiO3:Rh via interparticle electron transfer. It is notable that the Z-scheme
CO2 reduction proceeds using just photocatalyst powders,
water, and CO2 because of self-pH-adjustment by dissolved
CO2.
CO2 Reduction
on p-Type Cu(I)-Containing Metal Sulfide
Photocathodes under Visible Light Irradiation (Figure c,d)
A photoelectrochemical CO2 reduction system
is also
interesting to construct an artificial photosynthesis system. Photoelectrochemical
measurement is generally conducted in a 3-electrode system or a 2-electrode
system connected to a potentiostat and a power supply (Figure A). Scientifically intrinsic
information on the working electrode, for example, an absolute electrode
potential, is obtained with the 3-electrode system using a reference
electrode. The 2-electrode system is useful for evaluation of cell
performance such as open circuit voltage, short circuit current, and
energy conversion efficiency. It is meaningless in a photoelectrochemical
cell if an externally applied voltage is larger than the theoretical
voltage of electrolysis, for example, 1.23 V for water splitting.
Applying no external bias is ideal. To compare the performance of
a photoelectrode, a current–potential curve is usually measured
using the 3-electrode system. In addition, analysis of products by
bulk electrolysis is also indispensable, as well as measurement of
photocurrent to examine the Faradaic efficiency, that is, electrochemical
selectivity. The Faradaic efficiency reveals if the photocurrent is
due to desired redox reactions. Moreover, not only the Faradaic efficiency
but also a partial photocurrent density (i.e., rate of production)
are important to see how fast a certain product is formed. Incident
photon to current conversion efficiency (IPCE) and solar energy conversion
efficiency are also important.
Figure 5
(A) Two-electrode and three-electrode
systems for photoelectrochemical
CO2 reduction. (B) Photoelectrochemical CO2 reduction
under visible light irradiation over a (CuGa)0.5ZnS2 powder-based photocathode. Electrolyte, 0.1 mol L–1 KHCO3(aq); flow gas, CO2 (1 atm); light source,
300 W Xe lamp (λ > 420 nm); applied bias, 0.1 V vs RHE (−0.5
V vs Ag/AgCl (pH 6.9)). Reproduced with permission from ref (4). Copyright 2022 American
Chemical Society.
(A) Two-electrode and three-electrode
systems for photoelectrochemical
CO2 reduction. (B) Photoelectrochemical CO2 reduction
under visible light irradiation over a (CuGa)0.5ZnS2 powder-based photocathode. Electrolyte, 0.1 mol L–1 KHCO3(aq); flow gas, CO2 (1 atm); light source,
300 W Xe lamp (λ > 420 nm); applied bias, 0.1 V vs RHE (−0.5
V vs Ag/AgCl (pH 6.9)). Reproduced with permission from ref (4). Copyright 2022 American
Chemical Society.The photoelectrochemical
cell can employ p-type semiconductors
as a photocathode even photocorrosive materials. For example, visible
light responsive CuGaS2,[47] (CuGa)0.5ZnS2,[4,38] Cu0.8Ag0.2GaS2,[48,49] and Cu2ZnGeS4[50] function as a CO2-reducing photocathodes. The bare (CuGa)0.5ZnS2 photocathode reduces CO2 to CO with high stability under
visible light with application of an external bias (Figure B).[4] Faradaic efficiencies for CO and H2 formation are 20%
and 80%, respectively, being almost 100% of total Faradaic efficiency.
It is stressed that high CO formation is observed even without cocatalyst
and surface modification on the photocathode.Surface modification
with CdS and ZnS of an n-type semiconductor
and loading of a cocatalyst improve the performance of p-type Cu0.8Ag0.2GaS2,[49] Cu2ZnGeS4,[51] and
(CuGa1–In)1–Zn2S2 solid solution[52] photocathodes.
Introduction of an electrically conducting polymer such as polypyrrole
(PPy) or poly(3,4-ethylenedioxythiophene) (PEDOT) as hole transporter
also improves a photocathode composed of a powdered material, because
electric contact between the powders and the substrate electrode such
as FTO is usually poor.[53,54] PPy-modified CuGaS2 gives higher cathodic photocurrent for water and CO2 reduction than a bare CuGaS2 photocathode. Moreover,
the 2-electrode system combining a PEDOT–CuGaS2 photocathode
and a CoO/BiVO4 photoanode
with visible light response also reduces CO2 to CO using
water as an electron donor under application of a small bias and simulated
sunlight irradiation.
Conclusions and Perspectives
Artificial photosynthesis is ideal green chemistry and technology
to convert and store solar energy to chemical products as an uphill
reaction. Solar water splitting to produce H2 is representative
of artificial photosynthesis. Solar water splitting using a powder-based
photocatalyst on a large scale (100 m2) has been demonstrated.[5] It will accelerate the industrial application
of solar hydrogen production in the near future. In contrast to solar
water splitting, artificial photosynthetic CO2 utilization
using photocatalysts is still at the stage of basic research. However,
recent and rapid progress of this research area is hopeful. A variety
of photocatalyst and photoelectrode systems for CO2 utilization
has been extensively developed using homogeneous and heterogeneous
photocatalyst materials. This Account focused on photocatalytic and
photoelectrochemical systems based on particulate photocatalysts for
CO2 reduction as an artificial photosynthesis system working
under UV and visible light.Highly active photocatalysts for
water splitting such as BaLa4Ti4O15 (BG = 3.9 eV) and doped NaTaO3 (BG = 4.1 eV) were able
to be applied to CO2 reduction,
because they have sufficiently high conduction bands and enough potential
for water oxidation to form O2. The O2 evolution
ability and a suitable cocatalyst working as a reaction center for
CO2 reduction are indispensable for photocatalytic CO2 reduction using water as an electron donor. Ag and Rh–Ru
cocatalysts were developed for CO and CH4 formation, respectively.
Moreover, the photocatalytic activity was increased with optimization
of reaction conditions such as tuning of the reactant solution. Metal
sulfide photocatalysts with a high conduction band and visible light
response are attractive for CO2 reduction, though they
cannot oxidize water. This means that the metal sulfide photocatalyst
itself cannot use water as an electron donor to achieve an uphill
reaction. However, CuGaS2, (CuGa)1–Zn2S2, and
CuGa1–InS2 metal sulfide materials were able to be employed
as a CO2-reducing photocatalysts to make a Z-scheme photocatalyst
system to achieve photocatalytic CO2 reduction using water
as an electron donor under visible light irradiation. p-Type metal
sulfides CuGaS2, (CuGa)1–Zn2S2, and Cu1–AgGaS2 were
able to be applied to a photocathode for photoelectrochemical CO2 reduction, even if their powdered materials were employed.Strategies to design photocatalytic and photoelectrochemical systems
for CO2 reduction using water as an electron donor under
visible light irradiation become clearer as mentioned above. Therefore,
it is expected that more efficient photocatalyst and photoelectrode
systems can be developed with further extensive study. We believe
that photocatalyst and photoelectrode systems for solar CO2 utilization can be a practical use in the future as well as solar
hydrogen production by water splitting.