# Meeting the Industrial Challenges of CO 2 Photocatalytic Reduction: Moving From Molybdenum Disulfides to Oxysulfides Based Materials?

Sébastien Roth, Audrey Bonduelle-skrzypczak, Christèle Legens, Pascal Raybaud

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Sébastien Roth, Audrey Bonduelle-skrzypczak, Christèle Legens, Pascal Raybaud. Meeting the Industrial Challenges of CO 2 Photocatalytic Reduction: Moving From Molybdenum Disulfides to Oxysulfides Based Materials?. ChemSusChem, 2025, 18 (1), pp.e202400572. 10.1002/cssc.202400572. hal-05080538

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Submitted on 22 May 2025

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# Meeting the Industrial Challenges of CO₂ Photocatalytic Reduction: Moving From Molybdenum Disulfides to Oxysulfides Based Materials?

Sébastien Roth,*[a] Audrey Bonduelle-Skrzypczak,*[a] Christèle Legens,[a] and Pascal Raybaud*[a]

Reducing CO₂ emissions is one of the greatest challenges of the century. Among the means employed to tackle CO₂ emissions, the photocatalytic conversion of CO₂ is an appealing way to valorize CO₂ since it uses the sun energy, which is abundant. However, nowadays, the best photocatalytic systems still report too low efficiencies, and use expensive materials, so they cannot be readily industrialized for use at large scale. In this

report, we first highlight general industrial and process challenges (including operating conditions). Then, focusing on MoS₂/TiO₂ heterojunction systems, we analyze advantages and limitations of such systems and open perspectives on Mo oxysulfides supported on TiO₂ discussing their potential to reach higher efficiency for CO₂ photoconversion.

## 1. Introduction

Nowadays, most of the energy requirements are still fulfilled by the combustion of fossil fuels such as coal, oil and natural gas,[1] leading to a continuous increase in the CO₂ level in the atmosphere. Its current atmospheric concentration (424 ppm in February 2024[2]) is higher than at any point in at least the past 800 000 years,[3] resulting in unprecedented global warming. A critical rise in temperature would cause disastrous environmental consequences such as ice melting at the Earth's poles, collapse of the biodiversity and increases in precipitations, droughts and wildfires.[4] To limit such consequences, a target value of "well below 2°C above pre-industrial temperature levels" was set by the Paris Agreement in 2015. This means that CO₂ emissions need to fall from 36.6 Gt in 2021, to 12 Gt (at maximum) in 2050, following the Announced Pledges Scenario, which would result in a +1.7°C in 2100.[1]

Reducing CO₂ concentration is hence one of the major challenges of our society. Currently, the main strategies to reduce CO₂ emissions are: 1) reducing energy consumption 2) decarbonizing the energy sources 3) CO₂ capture and storage (CCS) or utilization (CCU). The first one, also called "energy sobriety" by governments, can hardly allow to reduce CO₂ emission by itself, given the expected world population growth and energy demand, but it can help to refrain the increase. The

second one translates in the development of renewable sources of energy. But they still represented less than 12% of the global energy consumption in 2021.[1] In cause, their difficult handling and their lower efficiency compared to nonrenewable sources. The third one aims at reducing CO₂ emissions by capturing and/or utilizing it directly from the atmosphere, or at the exhaust of plants like cement factories. CCS is a promising technology but its high cost, limited storage capacity and elevated carbon footprint limit its further development.[5] CCU seems then more promising since it converts CO₂, via biological, physical or chemical/catalytic processes, into value-added products ranging from fuels and chemicals (like methane, methanol, formic acid, etc.) to microalgae, that can be sold or directly re-used.[5,6]

Among the CO₂ conversion methods (thermal, electrochemical, biochemical, etc.),[7,8] photocatalysis is an appealing one since it exploits the sun energy, which is abundant (400 times higher than the annual energy demand[9]). However, the photocatalytic conversion of CO₂ is a complex process which still suffers from a very low energy efficiency yield, well below the target of 10% efficiency for at least 10 years,[10,11] hence it cannot be readily applied at an industrial scale. The low efficiency arises from many physical and chemical limitations of the materials, such as light penetration and absorption, charges recombination, CO₂ stability, selectivity, competing hydrogen evolution reaction (HER), etc.[12]

This perspective aims at introducing an appealing class of materials for heterogeneous CO₂ photoreduction with great potential to reach unprecedented energy efficiencies. For this purpose, we first recall the main process and industrial challenges linked to CO₂ photoreduction. Then, we discuss about TiO₂, MoS₂ and their heterojunction as a potential photocatalytic system for industrial applications. Finally, we present the potential of an alternative class of materials for CO₂ photoreduction: Mo oxysulfides.

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<footnote>[a] IFP Energies Nouvelles, Rond-Point de l'Echangeur de Solaize, Solaize, France</footnote>

<footnote>Correspondence: Sébastien Roth, Audrey Bonduelle-Skrzypczak and Pascal Raybaud, IFP Energies Nouvelles, Rond-Point de l'Echangeur de Solaize, 69360 Solaize, France.</footnote>

<footnote>Email: sebastien.roth@ifpen.fr and audrey.bonduelle@ifpen.fr and pascal.raybaud@ifpen.fr</footnote>

<footnote>© 2024 The Authors. ChemSusChem published by Wiley-VCH GmbH. This is an open access article under the terms of the Creative Commons Attribution License, which permits use, distribution and reproduction in any medium, provided the original work is properly cited.</footnote>
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## 2. Challenges for Implementing CO₂ Photoreduction Process at an Industrial Scale

The industrialization of the photocatalytic conversion of CO₂ could be directly applied to the fumes of cement plants, for instance, since they are mainly composed of water and CO₂, inevitably derived from the conversion of CaCO₃ to CaO. However, nowadays the best photocatalysts (like 1%Pt/TiO₂[¹³]) still record low conversion energetics of about 1%. Making some simple assumptions: only methane is produced, mean solar irradiance of 270 W/m² (for a desert type of land),[¹⁴] no kinetic limitations, no ageing of the photocatalyst, and considering a typical cement factory which produces 75 tons of CO₂ in 1 hour,[¹⁵] it is possible to evaluate the feasibility of the CO₂ conversion by a photocatalytic process. Such data imply that an irradiated surface of 370 km², using the best photocatalysts currently known, would be needed to totally convert the emitted CO₂ of a cement plant. This represents 26 Ivanpah solar plants (14 km²).[¹⁶] If we compare to nature's ability to convert CO₂ with photosynthesis, taking 22 kg of CO₂ absorbed by one tree per year,[¹⁷] and a tree density of 125 000 trees per km² (8 m² per tree), we would need a surface of 200 km² covered by trees to totally convert the CO₂ emitted during 1 year by a cement plant.

As additional limitation, choosing the 1%Pt/TiO₂ photocatalyst to convert the CO₂ emitted by a cement plant would require 94 tons of Pt to synthesize enough catalyst to cover 370 km². This represents about 50% of the global Pt production.[¹⁸] It is hence not a viable photocatalyst to use.

Therefore, for sustainability and feasibility reasons, there is a need to optimize the process and also to develop alternative photocatalysts with higher efficiencies, that do not involve scarce elements such as platinum. Indeed, these two scopes for improvement are key if we want to make the photocatalytic reduction of CO₂ at an industrial scale a reality.

## 3. Process Optimization for High Efficiency Heterogeneous CO₂ Photoconversion

### 3.1. Liquid-Solid Versus Gas-Solid Systems

Heterogeneous CO₂ photoconversion can be performed with liquid-solid and gas-solid systems. Liquid-solid photocatalytic systems are generally made of an aqueous dispersion of a photocatalyst nanoparticles. In this configuration, the photocatalyst is more easily accessible for the photons and the reactants. The processing is also easier than for gas-solid systems. However, the low solubility of CO₂ in water (34 mmol/L at 25°C)[¹⁹] limits the quantity of CO₂ adsorbable by the photocatalyst. Additionally, the separation of products from reactants and photocatalytic materials are quite challenging.[²⁰] Finally, in liquid-solid systems, the catalytic surface is solvated by water which saturates the surface by hydroxyl groups. Those

hydroxyls prevent the adsorption and activation of CO₂ molecules on the Lewis acid sites.[²¹]

In contrast, gas-solid photocatalytic systems are generally made of an immobilized photocatalyst (supported or not) on which a gas flux or reactants will pass. This approach makes it easier to separate the different compounds and allow different configurations for the reactor: batch or continuous. With such type of systems, the CO₂/H₂O ratio can be tuned, the problem of CO₂ solubility in water being overcome. Adsorption and desorption of reactants and products are also facilitated.[²²] However, this approach can decrease the accessible area for photons.

From an industrial point of view, gas-solid photocatalytic systems are more interesting since one of the ultimate goals of such systems would be, for instance, to convert CO₂ directly from the chimney of cement factories, which can reach CO₂ concentrations higher than 10%. In such a situation, CO₂ comes out already gaseous and humid, so there is no need to add any reactant to the mix. Also, theoretically, greater CO₂ conversion yield can be expected for gas-solid systems since there is no solubility limitation, meaning no restriction on the quantity of CO₂ that can be sent to the photocatalyst.

### 3.2. Batch Versus Continuous Flow Reactor

Batch reactors are generally pressurized closed vessels in which samples of the reactor composition are extracted at given times to analyze its composition and evaluate the CO₂ photoconversion. This type of reactor can be applied to both liquid-solid and gas-solid photocatalysis. The advantage of such reactors is their easy handling and operating. However, the accumulation of products within the reactor favors their readsorption and hence their reverse or side reaction like the re-oxidation into CO₂.[²³] They are also not really suitable for long-time and large-scale applications. In continuous flow reactors, the reactants and products are moving at a constant flow rate. The advantage of such reactors is that in-line analyses can be carried out, so it allows a better time dependence following of the reaction. Also, they can avoid the problem of products accumulation and readsorption encountered with batch reactors. However, the contact time of reactants with the photocatalyst is necessarily smaller, which can lead to a decrease of the overall conversion yield.[¹²]

The structure of the reactor also plays a key role on the photocatalytic process. For instance, fiber coated,[²⁴] monolithic-type with honeycomb-like structure,[²⁵] or well-organized nanoporous[²⁶] photoreactors were developed to enhance light harvesting. Dual chamber reactor can also be used to separate reduction and oxidation reactions in batch reactors in order to improve the stability of the photocatalyst.[²⁷]

Overall, continuous flow reactors should be preferred for industrial applications for all the advantages mentioned previously and also because they can be scaled up more easily.
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### 3.3. Operating Conditions

The main parameters that impact the process efficiency are the temperature, partial pressure of CO₂, mass of photocatalyst, CO₂/H₂O (or H₂) ratio, light intensity, wavelengths range of irradiation, volume of solution or gas (for batch reactors) and gas flow rate (for continuous flow reactors).

#### 3.3.1. Temperature

A temperature increase can have several effects on the photocatalytic system: 1) influence on the rate of reactions since the kinetic rate constants are generally increasing exponentially with temperature 2) decrease of the amount of dissolved CO₂ in liquid-solid photocatalysis systems 3) increase of charges recombination probability.[28] Depending on the rate limiting step, increasing the temperature can either favor or disfavor the photocatalytic activity. However, experimental results showed that small temperature variations (26 to 36 °C) do not affect the CO₂ conversion rate.[29]

#### 3.3.2. Pressure and Relative Concentrations

A pressure increase does not influence so much the overall reaction yield, it rather influences the selectivity of the process. In liquid-solid systems, increasing the CO₂ pressure favors the production of gaseous products like CH₄ at the expense of liquid ones like CH₃OH.[29] In gas-solid systems, increasing the CO₂ partial pressure could lead to the formation of longer chains products (C₂ and C₃) like ethane and propane.[30] Also, the overall conversion yield increases when CO₂ partial pressure increases, up to a certain point corresponding to the photocatalyst saturation: when adsorption will not be the kinetically limiting step anymore.[23]

If the CO₂/H₂O ratio is too high, the CO₂ conversion is not optimal due to a lack of proton source. However, if this ratio is too low, the impact is negative as well, favoring Hydrogen Evolution Reaction (HER) instead of CO₂ photoreduction.[31] This ratio is however hard to tune in liquid-solid state photocatalysis due to the low solubility of CO₂ in water.

#### 3.3.3. Illumination

The wavelength range of irradiation has to be adapted to the bandgap of the photocatalyst. Moreover, it can remarkably impact the activity and selectivity of materials. For instance, Hezam et al. reported a MoS₂/TiO₂ system with switchable CO₂ reduction products (from CO to CH₄) when illuminated with solar or visible light.[32]

Increasing the light intensity increases the production yield at rather low intensities (the production yield is proportional to the square root of the light intensity) due to an increase of available photons when the absorption is the kinetically limiting step. However, at higher intensities, increasing the light

intensity favors charges recombination and hence decreases the overall conversion yield.[31]

#### 3.3.4. Catalyst vs Reactant Quantity

The increase of the photocatalyst quantity in liquid-solid systems improves the overall efficiency up to a certain point when it will start to have a screening effect and prevent some photocatalyst particles to be illuminated. The same situation happens with gas-solid systems, mainly due to the limited penetration of light inside the material (less than 1 µm for bulk TiO₂[33] and few µm for TiO₂ thin films[34]).

The increase of volume of solution or gas in batch reactors can lead to diffusion or inhomogeneities problems. In continuous flow reactors, the gas flow rate influences the contact time of the reactants with the photocatalyst. Decreasing the flow rate is beneficial for the process activity up to a certain point where a plateau is reached, which means that the reactants contact time is not the rate limiting step anymore.[35]

### 3.4. Choice of Reactants

Different reactants can be used in order to photoreduce CO₂, the most common is water as protons source and holes scavenger, but H₂ can replace water. Sacrificial agents can also be used as hole scavengers.

The use of sacrificial agents is very common for liquid-solid photocatalysis. One way to improve the CO₂ photoconversion yield is to replace water by another solvent in which CO₂ solubility is greater. In this case, sacrificial agents are needed for the oxidation reaction. They can also be used in combination with water solvent due to their stronger hole accepting property. Classical sacrificial agents are salts (Na₂S/Na₂SO₃), acids (lactic acid, ascorbic acid), alcohols (methanol, ethanol, phenols) or tertiary amines (TEOA, TEA).[20] The use of methanol as sacrificial agent is controversial because it raises the problem of distinguishing methanol used as sacrificial agent from methanol photoproduced from CO₂ reduction.[36] In any case, it is better to avoid the use of sacrificial agents from an economic point of view for industrial processes. Indeed, they are more or less expensive consumables that are not recovered after the reaction.

For gas-solid photocatalysis, H₂ can be used to replace H₂O or as a co-reactant. The CO₂/H₂ mix can result in the same CO₂ photoreduction products as for the CO₂/H₂O mix: CH₄ and CO were obtained on oxide photocatalysts (NiO, Fe₃O₄, CuO),[37] CH₃OH and CO on layered double hydroxide[38] or surface frustrated Lewis pairs[39] systems. Even CO₂/(H₂O + H₂) mix can be used and proved to be the best mix compared to CO₂/H₂ or CO₂/H₂O on TiO₂.[40] Changing the reactants mix also influences the selectivity of the photoreaction probably owing to different reduction mechanism pathways.[41] Despite the CO₂/H₂O mix generally shows better results than CO₂/H₂ for the same photocatalytic system,[41–43] the advantage to use H₂ is to have a better control over the reactants quantities and to avoid the
<figure><img src="image_7.png" /></figure>

competing HER. Moreover, using H₂ as a reactant makes also
sense from an industrial point of view. Indeed, the fumes
coming out of chimneys can be treated to condense water and
produce H₂ with the help of an electrolyzer. The so produced H₂
would then be used for the photocatalytic reaction.

4. Search for Alternative Materials for High Efficiency Heterogeneous CO₂ Photoconversion

To tune the materials physical and chemical properties and enhance the overall photoactivity is a huge challenge that has already been widely described in literature.[44–46] Scheme 1 summarizes the different materials design strategies that can be applied to try to improve each step of the photocatalytic mechanism: 1) light penetration and absorption, 2) charge transport and separation, 3) reactants surface adsorption and redox reactions.

For the first step improvement, the semiconductor texture,
size and dopants are the key features. Additionally, metallic
nanoparticles involving plasmon resonance, and/or dyes can be
deposited on the photocatalyst so as to improve light harvest-
ing. For the second step, the morphology and dielectric
constant of the material are important parameters but the main
strategy employed to improve charges transport and separation
is to combine a semiconductor with another one (to form
heterojunction schemes), or with a co-catalyst. Finally, for the
third step, the main strategies concern the texture and surface
sites of the semiconductor. Metallic dopants can also provide
active sites, and the use of sacrificial agent is popular to avoid
limitations on the oxidation part.

One should not forget that one strategy can impact several
steps of the photocatalytic process, even if only the most
impacted step was aforementioned for simplicity.

Hence, the goal of this part is not to describe in detail the
design of photocatalysts to improve their efficiency, but it is
rather to introduce a new class of materials with high potential
for CO₂ photoconversion. We will predominantly focus on the
challenges for the CO₂ reduction reaction, and address more

occasionally (whenever it is required) some linked to the
Oxygen Evolution Reaction (OER).

**4.1. TiO<sub>2</sub>: A Reference Photocatalyst**

TiO₂ is a well-known semiconductor and the Degussa TiO₂ (P25), which is a mix of anatase (80%) and rutile (20%) is still considered as a model photocatalyst.[47] It is not the aim of the present report to review this reference material which has been widely studied in literature. In spite of its chemical stability, long durability, non-toxicity, low cost and easy availability, it is far from being the ideal photocatalyst. Indeed, its conversion efficiency for CO₂ photoreduction is low due to many factors: 1) its wide bandgap (3.0–3.2 eV) that allows only UV-light absorption (5% of the total sun spectrum), 2) its conduction band (CB) energy position (–0.5 V vs NHE at pH = 7)[20] that does not allow a huge overpotential with the reactions of interest (CH₄,CO,.../CO₂ ≤ –0.24 V vs NHE at pH = 7), 3) its high electrical resistivity (10¹³–10¹⁸ Ω.cm) and 4) a limited quantity of adsorption sites due to its small surface area in general (~50 m²/g for TiO₂ P25). Another downside of TiO₂ is that the OER, which is the necessary counter reaction in the CO₂ photoreduction, is not very often analyzed in the literature. Indeed, the absence of the observed O₂ product can be related to several reasons: 1) kinetic limitations in H₂O oxidation, 2) the adsorption of produced O₂ in TiO₂ oxygen vacancies, and 3) the consumption of produced O₂ or O-containing species for backward reactions (CH₄ oxidation).[34]

Many strategies are reported in literature to improve TiO₂
photoactivity for CO₂ conversion: doping,[48]
nanostructuration,[49] co-catalysts,[13] heterojunction with anoth-
er semiconductor,[50,51] etc. A non-exhaustive summary of TiO₂
based photocatalysts for CO₂ conversion is reported in Table 1.
Reported values for produced and used electrons for CO₂
conversion (in e⁻ µmol/h/g) were derived from the products
rate of formation (in µmol/h/g) and the number of electrons
required to form such products.

As shown in Table 1, the best gains in activity are obtained when TiO₂ is combined with another materials: a co-catalyst or another semiconductor. Actually, the best performances reported are for the Pt-TiO₂ UV100 catalyst, which uses Pt nanoparticles as co-catalyst and electrons trap, supported on a very high specific surface TiO₂ UV100 (400 m²/g).[49] This highlights the need to combine TiO₂ with another material in order to tackle some of its previously mentioned limitations. In this regard, MoS₂ seems to be a good candidate since it possesses a small bandgap and high electronic conductivity.

**4.2. MoS<sub>2</sub>: An Excellent Electrocatalyst, but Not Only**

MoS₂ is a visible light responsive photocatalyst that is made of
earth-abundant elements with promising properties. It can be
easily doped, and its bandgap (1.29 – 1.90 eV) can be tuned
depending on the number of layers, the surface defects, the
temperature and/or the strain applied to the material.[52]

<figure><img src="image_8.png" /><figcaption>**Scheme 1.** Summary of the photocatalyst design strategies for enhancing CO₂ photoconversion efficiency.</figcaption></figure>
<figure><img src="image_9.png" /></figure>

<table><caption>**Table 1.** TiO₂ based photocatalysts for CO₂ conversion: operating conditions, produced and used electrons for CO₂ conversion expressed in e- µmol/h/g, gain compared to the reference TiO₂ of the corresponding work.</caption><thead><tr><th>Material</th><th>Conditions</th><th>Produced and used electrons for CO<sub>2</sub> conversion (e- µmol/h/g)</th><th>Gain compared to reference TiO<sub>2</sub></th></tr></thead><tbody><tr><td>TiO<sub>2</sub> (anatase)<sup>[54]</sup></td><td>Solid-gas, continuous flow reactor, CO<sub>2</sub> + H<sub>2</sub>O</td><td>1.3</td><td>-</td></tr><tr><td>TiO<sub>2</sub> (rutile)<sup>[54]</sup></td><td>Solid-gas, continuous flow reactor, CO<sub>2</sub> + H<sub>2</sub>O</td><td>0.4</td><td>-</td></tr><tr><td>TiO<sub>2</sub> P25 (20% rutile, 80% anatase)<sup>[49]</sup></td><td>Solid-gas, continuous flow reactor, CO<sub>2</sub> + H<sub>2</sub>O</td><td>2.3</td><td>-</td></tr><tr><td>N-doped TiO<sub>2</sub> (anatase)<sup>[48]</sup></td><td>Solid-gas, batch reactor, CO<sub>2</sub> + H<sub>2</sub>O</td><td>31</td><td>x2</td></tr><tr><td>TiO<sub>2</sub>·x (101) (anatase)<sup>[55]</sup></td><td>Solid-gas, continuous flow reactor, CO<sub>2</sub> + H<sub>2</sub>O</td><td>16</td><td>x2</td></tr><tr><td>3D-TiO<sub>2</sub>@Si foam (10% rutile, 90% anatase)<sup>[49]</sup></td><td>Solid-gas, continuous flow reactor, CO<sub>2</sub> + H<sub>2</sub>O</td><td>9.9</td><td>x5</td></tr><tr><td>Au/TiO<sub>2</sub> (anatase)<sup>[13]</sup></td><td>Solid-gas, continuous flow reactor, CO<sub>2</sub> + H<sub>2</sub>O</td><td>56.8</td><td>x7</td></tr><tr><td>Pt-TiO<sub>2</sub> UV100 (anatase)<sup>[13]</sup></td><td>Solid-gas, continuous flow reactor, CO<sub>2</sub> + H<sub>2</sub>O</td><td>720</td><td>x90</td></tr><tr><td>Type II co-exposed (101) and (001) TiO<sub>2</sub> (anatase)<sup>[56]</sup></td><td>Solid-gas, batch reactor, CO<sub>2</sub> + H<sub>2</sub>O</td><td>10.8</td><td>x9</td></tr><tr><td>Type II Cu<sub>2</sub>ZnSnS<sub>4</sub>/TiO<sub>2</sub> (anatase)<sup>[50]</sup></td><td>Solid-gas, batch reactor, CO<sub>2</sub> + H<sub>2</sub>O</td><td>14.6</td><td>x12</td></tr><tr><td>S-scheme Zn<sub>3</sub>In<sub>2</sub>S<sub>6</sub>/TiO<sub>2</sub> (rutile and anatase mix)<sup>[51]</sup></td><td>Solid-gas, batch reactor, CO<sub>2</sub> + H<sub>2</sub>O</td><td>96.2</td><td>x50</td></tr><tr><td>Au@CdS/TiO<sub>2</sub> (Inverse Opal) (20% rutile, 80% anatase)<sup>[57]</sup></td><td>Solid-gas, continuous flow reactor, CO<sub>2</sub> + H<sub>2</sub>O</td><td>334</td><td>x24</td></tr></tbody></table>

However, improvements need to be done essentially on two points: 1) its photostability: MoS₂ gets easily oxidized by photogenerated holes during the photocatalytic process, 2) its small bandgap that limits its range of applications as a photocatalyst. Actually, MoS₂ (2H and/or 1T) is often used for its co-catalyst electrons trap property, but for the 2H phase, its semiconductor properties can be exploited as well.

Asadi et al. were the first ones to report the use of MoS₂ for CO₂ electroreduction in 2014.[53] They showed that MoS₂ gives better results than noble metals in CO₂ electroreduction and that the activity is mainly due to MoS₂ edges. Indeed, vertically aligned MoS₂ on glassy carbon showed higher current density than bulk MoS₂. This initial study paved the way to the research in the field of MoS₂ based systems for CO₂ photoreduction. However, the band positions of MoS₂, which depend on its number of layers, are not optimal to favor CO₂ photoreduction as well as OER, even for MoS₂ single layer which shows the widest bandgap (2.4 eV) (Scheme 2).[58] Indeed, large over-potentials (at least 0.7 V) on both the reduction and the oxidation sides may be required from a kinetic point of view[59] and it is still an open question to which extent the VB and CB band positions of MoS₂ single layer can be compatible with the potentials required for both the reduction and oxidation reactions.

Hence, as reported in Table 2, several strategies have been developed to make MoS₂ based materials, potential candidates for CO₂ photoreduction reaction and OER, mainly using MoS₂ with either metallic co-catalysts like Ag and Au[63], or wide bandgap semiconductors like TiO₂,[64] SiC[22] and g-C₃N₄,[65] or involving two materials in heterojunction.[66,67] The best systems however use three different materials in heterojunction[66,67]

<figure><img src="image_10.png" /><figcaption>**Scheme 2.** Monolayer MoS₂ and bulk MoS₂ valence band (VB) and conduction band (CB) positions for CO₂ photoreduction. The CO₂/CH₄ redox couple is the one with the highest potential for CO₂ reduction. Bandgaps value reported here were extracted from DFT calculations.[58] These values tend to be overestimated compared to experimental values, due to the fact that DFT calculations evaluate the fundamental bandgap, while experimental studies often determine the optical bandgap.[60] Note also that experimental values vary depending on the characterization techniques used.[61,62]</figcaption></figure>

leading to better charges separation and band positions adjustment.

### 4.3. The MoS₂/TiO₂ Heterojunction: An Inspiration for Photocatalysts

The MoS₂/TiO₂ heterojunction is a particularly interesting system for CO₂ photoreduction, even if it is well-known that Pt/TiO₂ is one of the best photocatalysts for that reaction. Indeed, it has been shown that MoS₂ as a co-catalyst can challenge Pt for the hydrogen evolution reaction when combined to TiO₂.[69,70] It is hence interesting to study how this type of material behaves for CO₂ photoreduction.
<figure><img src="image_11.png" /></figure>

<table><caption>**Table 2.** MoS₂ based photocatalysts for CO₂ conversion: operating conditions, produced and used electrons for CO₂ conversion expressed in e- µmol/h/g, gain compared to the reference photocatalyst of the corresponding work.</caption><thead><tr><th>Material</th><th>Conditions</th><th>Produced and used<br>electrons for CO<sub>2</sub><br>conversion<br>(e- µmol/h/g)</th><th>Gain compared to<br>reference material</th></tr></thead><tbody><tr><td>2H-MoS<sub>2</sub><sup>[64]</sup></td><td>Solid-liquid, batch reactor, CO<sub>2</sub> + H<sub>2</sub>O</td><td>15.7</td><td>-</td></tr><tr><td>(2H + 3R)-MoS<sub>2</sub><sup>[68]</sup></td><td>Solid-liquid, batch reactor, CO<sub>2</sub> + H<sub>2</sub>O</td><td>94.8</td><td>-</td></tr><tr><td>Ag/MoS<sub>2</sub><sup>[63]</sup></td><td>Solid-liquid, batch reactor, CO<sub>2</sub> + H<sub>2</sub>O</td><td>31</td><td>x2.4 (vs MoS<sub>2</sub>)</td></tr><tr><td>Au/MoS<sub>2</sub><sup>[63]</sup></td><td>Solid-liquid, batch reactor, CO<sub>2</sub> + H<sub>2</sub>O</td><td>16</td><td>x2.6 (vs MoS<sub>2</sub>)</td></tr><tr><td>Type II TiO<sub>2</sub>/MoS<sub>2</sub><sup>[64]</sup></td><td>Solid-liquid, batch reactor, CO<sub>2</sub> + H<sub>2</sub>O</td><td>156.2</td><td>x10 (vs MoS<sub>2</sub>)<br>x7 (vs TiO<sub>2</sub>)</td></tr><tr><td>S-scheme SiC (3D)/MoS<sub>2</sub> (2D)<sup>[22]</sup></td><td>Solid-gas, batch reactor, CO<sub>2</sub> + H<sub>2</sub>O</td><td>105.2</td><td>x30 (vs MoS<sub>2</sub>)<br>x4 (vs SiC)</td></tr><tr><td>S-scheme g-C<sub>3</sub>N<sub>4</sub>/MoS<sub>2</sub><sup>[65]</sup></td><td>Solid-liquid, batch reactor, CO<sub>2</sub> + H<sub>2</sub>O</td><td>17.1</td><td>x3 (vs g-C<sub>3</sub>N<sub>4</sub>)</td></tr><tr><td>TiO<sub>2</sub>-rGO-MoS<sub>2</sub><sup>[66]</sup></td><td>Solid-gas, batch reactor, CO<sub>2</sub> + H<sub>2</sub>O</td><td>186.4</td><td>x14.5 (vs TiO<sub>2</sub>)</td></tr><tr><td>SnS<sub>2</sub>-rGO-MoS<sub>2</sub><sup>[67]</sup></td><td>Solid-liquid, batch reactor, CO<sub>2</sub> + H<sub>2</sub>O</td><td>451.2</td><td>x205 (vs MoS<sub>2</sub>)</td></tr></tbody></table>

In experimental studies, the TiO₂/MoS₂ heterojunction has been mainly reported in two categories. The first and most common one reports only the role of MoS₂ as a co-catalyst, while TiO₂ harvests the light.[71] Therefore, the role of MoS₂ is to act as electrons trap in order to limit charges recombination, and to provide supplementary active sites (Figure 1.a). In this case, the metallic property of 1T-MoS₂ is exploited as a co-catalyst since it has better charge conductivity, or because 2H-MoS₂ band edges are not adequate for the redox reactions.[72]

The second category invokes the possible formation of a type II heterojunction or of a Z-scheme. In the former case, the charge transfer mechanism will result in the accumulation of electrons in the CB of TiO₂ and of holes in the VB of MoS₂. So that TiO₂ takes charge of the reduction reactions and MoS₂ of the oxidation reactions (Figure 1.b).[64] However, the not negative enough position of the CB of TiO₂ and the not positive enough position of the VB of MoS₂ make this type II heterojunction impossible to reach the expected reduction and oxidation overpotentials for high activity.

Using density functional theory (DFT) with the proper exchange-correlation functional (HSE06) to describe bandgaps, Favre et al. investigated various types of MoS₂/TiO₂ heterojunction. They distinguished a physical from a chemical interaction between 2H-MoS₂ monolayer and anatase TiO₂ (101) and (001) surfaces, and simulated different possible heterostructures.[73] They showed that a chemical interaction involving Ti–O–Mo interfacial bridges leads to a type I heterojunction due to the band positions of 2H-MoS₂ nano-ribbons and TiO₂ (101) surface (which is the major facet in anatase (90%)). This could not result in improved photocatalytic performances since photogenerated charges accumulate on MoS₂ which has weaker redox potentials (Figure 2.a). However, a physical (van der Waals) interaction between 2H-MoS₂ monolayer and TiO₂ (101) or (001) surfaces results in a staggered band position. From this point both classical type II heterojunction and Z-scheme could be considered, even if further calculations of charges distribution at the interface suggest that the Z-scheme heterojunction could be preferentially formed in this system. It means that electrons accumulate in the CB of MoS₂ (the strongest reduction potential) and holes in the VB of TiO₂ (the strongest oxidation potential) (Figure 2.b). Note that such type of Z-scheme has been often invoked as being crucial for obtaining efficient photocatalysts in CO₂ reduction[74]. The same DFT study also shows that these trends highly depend on the hydroxylated and sulfided states of the TiO₂ surfaces. In the case of a sulfided surface, the TiO₂ bandgap

<figure><img src="image_12.png" /><figcaption>**Figure 1.** (a) MoS₂ co-catalyst of TiO₂ for CO₂ photoconversion and organics photodegradation. Reproduced with permission from Ref. [71]. Copyright 2017, RSC Pub. (b) Type II heterojunction MoS₂/TiO₂ for CO₂ photo-conversion. Reproduced with permission from Ref. [64]. Copyright 2019, Elsevier.</figcaption></figure>
<figure><img src="image_13.png" /></figure>

<figure><img src="image_14.png" /><figcaption>**Figure 2.** (a) Type I heterojunction of the 1D chemical interface between MoS₂ nanoribbon and the TiO₂ (101) surface and associated molecular model. (b) Possible Z-scheme for the physical 2D-heterojunction between the MoS₂ sheet and the TiO₂ (101) surface and associated molecular model. Adapted with permission from Ref. [73]. Copyright 2022, RSC Pub.</figcaption></figure>

is significantly reduced due to a valence band maximum (VBM) shift at higher energy level. Another DFT study completed these results and proposed a Z-scheme heterojunction also for the MoS₂/TiO₂ (100) heterostructure with physical interactions,⁷⁵ although the level of theory (GGA) is not accurate enough to guarantee the reliability of the electronic properties. However, classical type II heterojunction could happen if the kinetic effect does not allow the electron migration mechanisms as suggested in Figure 2.b.

The TiO₂/MoS₂ heterojunction is mostly reported in literature for pollutants degradation and hydrogen photoproduction.⁷¹,⁷⁶,⁷⁷ However, there are very few examples of such system for CO₂ photoconversion. Asadi et al. explained that unsaturated S atoms on MoS₂ edges are favorable for the HER, and hence for water splitting, while unsaturated Mo atoms exposed on the edge favor the CO₂ photoreduction.⁵³ However, it is challenging to synthesize MoS₂ with mostly Mo atoms on the edges, so this is probably why the use of TiO₂/MoS₂ and

more generally MoS₂ for CO₂ photoconversion is not as widespread as for hydrogen photoproduction or pollutants degradation.

The first report on a TiO₂/MoS₂ heterojunction system for CO₂ photoconversion was published by Tu et al.⁷⁸ They prepared a MoS₂/TiO₂ nanosheets hybrid that shows excellent liquid-phase photoconversion of CO₂ into CH₃OH. Their best hybrid material is composed of 0.5 wt% MoS₂ and manifests a 3-fold in activity compared to TiO₂ alone (Table 3). This result is due to effective charges separation with electron transfer from the CB of TiO₂ to the CB of MoS₂. More loaded samples showed worst results probably because of the light shielding effect of black MoS₂ nanosheets.

A MoS₂/TiO₂ nanofibers photocatalyst for gas-phase CO₂ conversion was then proposed by Xu et al.⁷⁹ They observed the formation of both CH₄ and CH₃OH while only CH₃OH was observed on TiO₂ alone. Their 8 wt% MoS₂/TiO₂ exhibits a CO₂ conversion rate 9 times higher than TiO₂ alone (Table 3). This improvement is attributed to the increased light absorption thanks to MoS₂ small bandgap, increased specific surface area, and enhanced charges separation. Similarly, Yu et al. reported a core@shell 3D-TiO₂@MoS₂ heterojunction system for CO₂ electroconversion.⁸⁰ Despite not reporting photocatalytic tests, they showed that their material possessed Ti-S bonds that favor the CO₂ conversion to CO at the expense of the HER. This is an interesting result that could be extrapolated to CO₂ photocatalysis.

Jia et al. reported that a MoS₂/TiO₂ composite system with 10 wt% MoS₂ converts CO₂ into CO and CH₄ in a liquid-phase set-up, with an activity enhanced by a factor 7 and 10 compared to TiO₂ and MoS₂ alone respectively⁶⁴ (Table 3). These results were assigned to the improved absorption and to lower charges recombination rate due to the type II heterojunction that was formed.

Then, an heterojunction between MoS₂ flowers and TiO₂ nanosheets allowed the formation of CO and CH₄ with a conversion rate that is multiplied by 2 compared to TiO₂ alone (Table 3) according to Kang et al.⁸¹ They went even further by adding g-C₃N₄ to form a multiple heterojunction system that exhibits an even higher conversion rate.

More recently, Hezam et al. reported a MoS₂/TiO₂ nanowires system with switchable CO₂ reduction products (Figure 3).³²

<table><caption>**Table 3.** MoS₂/TiO₂ based photocatalysts for CO₂ conversion: operating conditions, produced and used electrons for CO₂ conversion expressed in e- µmol/h/g, gain compared to the reference photocatalysts of the corresponding work.</caption><thead><tr><th>Material</th><th>Conditions</th><th>Produced and used<br>electrons for CO<sub>2</sub><br>conversion<br>(e- µmol/h/g)</th><th>Gain compared to<br>reference material</th></tr></thead><tbody><tr><td>0.5wt% MoS<sub>2</sub>/TiO<sub>2</sub> nanosheets<sup>[78]</sup></td><td>Solid-liquid, batch reactor, CO<sub>2</sub> + H<sub>2</sub>O</td><td>63.6</td><td>x3 (vs TiO<sub>2</sub>)</td></tr><tr><td>8wt% MoS<sub>2</sub>/TiO<sub>2</sub> nanofibers<sup>[79]</sup></td><td>Solid-gas, batch reactor, CO<sub>2</sub> + H<sub>2</sub>O</td><td>38.2</td><td>x9 (vs TiO<sub>2</sub>)</td></tr><tr><td>10wt% MoS<sub>2</sub>/TiO<sub>2</sub> composite<sup>[64]</sup></td><td>Solid-liquid, batch reactor, CO<sub>2</sub> + H<sub>2</sub>O</td><td>156.2</td><td>x10 (vs MoS<sub>2</sub>)<br>x7 (vs TiO<sub>2</sub>)</td></tr><tr><td>50wt% MoS<sub>2</sub> flowers/TiO<sub>2</sub> nanofibers<sup>[81]</sup></td><td>Solid-liquid, batch reactor, CO<sub>2</sub> + H<sub>2</sub>O</td><td>43.2</td><td>x2 (vs TiO<sub>2</sub>)</td></tr><tr><td>82wt% MoS<sub>2</sub>/TiO<sub>2</sub> nanowires<sup>[32]</sup></td><td>Solid-gas, batch reactor, CO<sub>2</sub> + H<sub>2</sub>O</td><td>163.2 (visible)<br>72 (solar)</td><td>x45 (vs MoS<sub>2</sub>, visible)<br>x4 (vs MoS<sub>2</sub>, solar)</td></tr></tbody></table>
<figure><img src="image_15.png" /></figure>

<figure><img src="image_16.png" /></figure>

<figure><img src="image_17.png" /><figcaption>**Figure 3.** Products yield resulting from CO₂ photoreduction under visible and solar light. MT–X stands for the experimental conditions which resulted in a given MoS₂/TiO₂ heterojunction (M stands for Mo-containing solution, T stands for Ti-containing solution, and X is linked to the volume of the Ti-containing solution used). Adapted with permission from Ref. [32]. Copyright 2023, Wiley-VCH.</figcaption></figure>

Indeed, they interestingly showed, thanks to in situ irradiated XPS, electron spin resonance, terephthalic acid photoluminescence and photocurrent experiments, that under solar light irradiation, the system exhibits a Z-scheme type of heterojunction as it was proposed in Figure 2.b.[73] However, under visible light irradiation, it exhibits a type II heterojunction. This change of charges transfer mechanism allowed to switch from CO to CH₄ respectively as main product of the CO₂ photoreduction. The switch was ascribed to the change from MoS₂ to TiO₂ for the CO₂ reduction sites. Such system presents an activity (in electrons produced and used for CO₂ conversion) that is similar to TiO₂ and up to 4 times higher than MoS₂ under solar irradiation for the best material. The gain appears to be much more consequent under visible light: up to a 45-fold in activity compared to MoS₂ is reported (TiO₂ does not absorb visible light).

## 4.4. Mo Oxysulfides as Alternative Class of Materials with High Efficiency Potential

A metal oxysulfide is a compound composed of at least a metal, an oxygen and a sulfur atom, with negative oxidation states for both oxygen and sulfur. The classical oxysulfide is a ternary system with the formula MₓOᵧS_z, but quaternary and penternary compounds exist as well. Distinction should be made between metal oxysulfides which contain no O–S bond due to the negative oxidation state of S, and metal sulfates where sulfur has a positive oxidation state and binds to oxygen.[82]

Up to 1947, ternary oxysulfides were limited to lanthanides, actinides, and bismuth.[83-85] Oxysulfides were then extended to transition metals like Cu, Zn, Mo, Ti and W. Inoue et al. were the first to report the crystalline structure of two transition metal oxysulfides: MoO₂.₇₄S₀.₁₂ and MoO₁.₈₈S₀.₁₅.[86] Then Abraham et al. and Pasquariello et al. synthesized various MoOₓS_z amorphous compounds that were used for batteries.[87,88] Actually, before being used for photocatalysis applications, metal oxysulfides were primarily used for batteries, scintillators, screens and lasers.[82] They were also reported very early as key intermediates formed during the genesis of industrial hydrotreating

supported catalysts. In the last decade, the structure of such amorphous MoO₃S₂ intermediates supported on alumina was elucidated both theoretically with DFT simulations,[89] and experimentally by X-ray absorption spectroscopy.[90,91]

Moreover, metal oxysulfide compounds are interesting materials for photocatalysis. Indeed, oxide materials present a too wide bandgap, whereas sulfide materials often present too narrow bandgaps and instability during the photocatalytic process is suspected. In particular, the instability with respect to oxidation (photocorrosion) has been stressed out by numerous studies for the reference CdS photocatalyst[92,93] and suspected for MoS₂.[94] However, this effect is less addressed for oxysulfides. On the one hand, oxysulfides present tunable bandgaps depending on the O and S contents, the more S the narrower the bandgap.[95] On the other hand, the nature of oxysulfides may increase their intrinsic resilience to oxidation due to the S₃p–O₂p hybridization.[96] At this stage, the preparation way of the oxysulfide material may be crucial (under oxidizing environment and specific thermal treatment), since it may induce the formation of stable S-species and prevent them from a reoxidation process under photocatalytic conditions. However, the complete suppression of sulfur ions oxidation is an open challenge in photocatalysis, which may be limited if holes are efficiently extracted from the oxysulfide phase, either through holes migration to another phase (heterojunction with another semiconductor or coupled to a co-catalyst), or by improving the oxidation overpotential to favor the OER at the expense of self-oxidation.

The intermediate oxidation degree of an oxysulfide, between an oxide and a sulfide, can be revealed by XPS, which reports the presence of typical oxide and sulfide components, as well as a mixed intermediate component. For instance, MoO₂.₄S₀.₇ shows a Mo⁶⁺ component (oxide-like), a Mo⁴⁺ component (sulfide-like), and a Mo⁵⁺ component (oxysulfide-like) (Figure 4.a)[97]. This diversity of species is also found for the S₂p peak (Figure 4.b). The proportion of each component directly depends on the oxysulfide.

Focusing on molybdenum oxysulfides, Shahrokhi et al. conducted DFT calculations of the impact of S-doping on bulk and few layers MoO₃ and O-doping on bulk and few layers

<figure><img src="image_18.png" /><figcaption>**Figure 4.** XPS spectra of MoO₂.₄S₀.₇ thin film: (a) Mo 3d<sub>5/2</sub>-3/2 peak; (b) S 2p<sub>3/2</sub>-1/2 peak. Reproduced with permission from Ref. [97]. Copyright 2001, Elsevier.</figcaption></figure>
<figure><img src="image_19.png" /></figure>

MoS₂, on the opto-electronic properties of the oxysulfide resulting materials.[58,98,99] First of all, they showed that the O doping does not impact so strongly many optical properties of bulk MoS₂ such as bandgap, absorption coefficient, dielectric constant or even exciton binding energies.[99] This result may imply that if a loss of efficiency of MoS₂ is observed in oxidizing environment, this is not due to a change of optical properties but rather to a poisoning of surface active sites. By contrast, they showed that the S-doping of bulk MoO₃ reduces significantly the bandgap by ~1 eV and increases the optical absorption with respect to pristine α-MoO₃, while keeping charge mobility and separation at a level compatible for photocatalysis[99]. In addition, the CB and VB edge positions are very sensitive to S-doping of MoO₃ and evolves rather continuously to lower potential values (Figure 5). These Mo oxysulfides (S-doped MoO₃) exhibit a rather strongly positive VB potential which may be compatible with OER, but the CB band level is not compatible with the negative potential required for CO₂ reduction. As a consequence, they proposed to build a Z-scheme heterojunction between S-doped MoO₃ (as single layer or multi-layer) and single layer MoS₂, which might be suitable for CO₂ photoconversion.[58,98] As illustrated in Figure 5, when the MoO₃ heterostructure is doped by at least 8% S, the system exhibits staggered band positions, with bandgaps of similar values ~2.4 eV, characterizing a type II heterojunction or eventually Z-scheme.

Mo oxysulfides, apart from their opto-electronic properties, present also interest for orienting the selectivity of reactions. Indeed, Mayhall et al. calculated that water adsorption happen on Mo atoms and is more favorably adsorbed on Mo oxide species than on Mo sulfides.[100] They also reported that water dissociation is favored on Mo oxides. So, the use of oxysulfides for CO₂ photoconversion is interesting from an opto-electronic point of view, but also for the reaction selectivity since oxysulfides have greater chances to favor the

CO₂ reduction compared to the HER, oppositely to pure oxide materials.

Transition metal oxysulfides containing Mo have been reported in literature for numerous photocatalytic applications, but never for CO₂ photoconversion. Indeed, MoCoOS,[101] MoO₃·S₂·CoP,[102] MoO₃·S₂/CdS,[103] and MoO₃·S₂/Ni₃S₂[104] were used for the photocatalytic HER. Pollutants degradation with systems like bimetallic MoSrOS[105] and V-doped Mo(O,S)₂[106] were also reported. Among these systems, many could be good candidates for CO₂ photoconversion. Especially MoCoOS that exhibits a Z-scheme with appropriate band edges position for CO₂ photoconversion. Indeed, the experimentally measured VB of Mo(O,S) (Mo oxysulfide: called "S-doped Mo₄O₁₁" in Ref. [101]) is greater than the O₂/H₂O potential and the CB of Co(O,S) is way below the H₂/H⁺ potential (Figure 6). Therefore, it would also be way above CO₂ reduction potentials and hence be suitable for CO₂ photoconversion from a thermodynamic point of view. At this stage, it is important to stress that the experimental CB/ VB positions assigned to the synthesized Mo-oxysulfide material illustrated in Figure 6, significantly differ from the theoretical ones assigned to similar materials in Figure 5. This trend is also valid for the positions of the CB/VB edges of α-MoO₃ which positions are shifted to more negative potentials.[101,107] Possible origins of these shifts are provided in literature:[108] the reduction of the pristine α-MoO₃ into substoichiometric MoOₓ material and the hydroxylation of the α-MoO₃ surfaces. Interestingly similar effects have been reported for TiO₂ surfaces.[73,109] As a consequence, it is highly crucial to precisely control the surface state of the Mo-oxysulfides (S/O ratio, surface hydroxyl or sulfhydryl groups...) in order to reach the targeted properties.

Even though transition metal oxysulfides are not widely reported in literature for photocatalytic applications, they exhibit interesting properties for this application and should not be forgotten when developing new photocatalysts. The heterojunction of Mo oxysulfides with TiO₂ seems to be a particularly appealing strategy for CO₂ photoconversion. Moreover, the genesis of such metal oxysulfides from an oxide precursor supported on TiO₂ would require the use of sulfiding agent. This step may simultaneously induce the S-doping of bulk TiO₂ or TiO₂ surfaces which has been shown to reduce the bandgap and shift the light absorption of TiO₂ from UV to visible light.[73,110,111] As a consequence, a synergy effect for TiO₂ supported metal oxysulfides can be expected at various levels: from light absorption to reactivity.

<figure><img src="image_20.png" /><figcaption>**Figure 5.** Calculated conduction and valence band edges position for S-substituted single layer (SL) MoO₃ and single layer to six layers (1L-6L) MoS₂ with respect to the vacuum level and the standard hydrogen electrode at pH = 0. Reproduced with permission from Ref. [58], Copyright 2021, American Chemical Society.</figcaption></figure>

<figure><img src="image_21.png" /><figcaption>**Figure 6.** Band positions of the Mo(O,S)/Co(O,S) S-scheme heterojunction (a) before contact and (b) after contact. Reproduced with permission from Ref. [101], Copyright 2022, RSC Pub.</figcaption></figure>
<figure><img src="image_22.png" /></figure>

## 5. Conclusions and Perspectives

Even though the photoreduction of CO₂ is a hot topic in the literature, it remains a daunting task to reach high enough conversion yields for industrialization perspectives (10% for at least 10 years<sup>[10,11]</sup>) with this approach. Challenges currently encompass both process and materials aspects so as to reach high efficiencies, sustainability and economic feasibility. Indeed, multiple operating parameters (reactor type, temperature, pressure, reactants type, light intensity, etc.) greatly affect the overall process efficiency as well as key materials properties (bandgap, band positions, charges conductivity, affinity with CO₂, etc.). Up to date, the best systems record energetic efficiencies of around 1% and often use scarce materials. They are hence not ready for industrialization and use at a large scale. Therefore, the search of efficient and sustainable photocatalysts to convert CO₂ remains as one of nowadays biggest challenges.

TiO₂ is a widely studied photocatalysts which shows serious drawbacks to be a good candidate for CO₂ conversion by itself. Several strategies have been reported to improve its activity, the most efficient being the use of a Pt co-catalyst<sup>[13]</sup> which cannot be proposed as an industrial solution due to the serious constraints on this strategic and critical metal. MoS₂ which is rather known for its good electrocatalytic properties can also be used as a photocatalyst even though it suffers from stability and overpotentials limitations. However, it has been reported as a better TiO₂ co-catalyst than Pt for H₂ production<sup>[69]</sup> and has hence great potential for CO₂ photoreduction. Indeed, few articles, that were mentioned in this perspective, with promising results report a MoS₂/TiO₂ heterojunction for CO₂ photocatalytic reduction with good improvement compared to bare TiO₂.

However, the MoS₂/TiO₂ system may not be sufficient to reach high efficiency and within this perspective, we suggest to explore more deeply Mo oxysulfides supported on TiO₂, which may offer more favorable properties for CO₂ photoreduction. In this perspective oxysulfides advantages were highlighted: easy bandgap and band positions tuning depending on the chemical composition of the oxysulfide,<sup>[95,98]</sup> stability toward photo-oxidation,<sup>[96]</sup> and favorable CO₂ adsorption.<sup>[100]</sup> Moreover, other wide bandgap semiconductors than TiO₂, like CdS, WO₃, ZnO, etc. could be combined to Mo oxysulfides, providing their band positions are appropriate to provide good heterojunction schemes.

Considering the analysis provided in this Perspective, it seems particularly interesting to encourage more systematic synthesis, characterization and photocatalytic evaluation of Mo oxysulfide materials for the challenging CO₂ photoreduction reaction, which has not been done yet. Only few applications for H₂ production and pollutants degradation have been reported.

## Conflict of Interests

The authors declare no conflict of interest.

**Keywords:** Photocatalysis · Carbon storage · MoS₂ · TiO₂ · Oxysulfides

[1] International Energy Agency, "World Energy Outlook ", can be found under https://www.iea.org/reports/world-energy-outlook-2023 2023.

[2] National Oceanic & Atmospheric Administration (NOAA) Research, "Trends in Atmospheric Carbon Dioxide", can be found under https://gml.noaa.gov/ccgg/trends/2023.

[3] J. P. Smol, *Nature* **2012**, *483*, S12.

[4] Contribution of Working Group III to the Sixth Assessment Report of the Intergovernmental Panel on Climate Change, "Climate Change 2022: Mitigation of Climate Change", can be found under https://www.ipcc.ch/report/ar6/wg3/ **2022**.

[5] S. S. Iyer, I. Bajaj, P. Balasubramanian, M. M. F. Hasan, *Ind. Eng. Chem. Res.* **2017**, *56*, 8622.

[6] Y. Zheng, W. Zhang, Y. Li, J. Chen, B. Yu, J. Wang, L. Zhang, J. Zhang, *Nano Energy* **2017**, *40*, 512.

[7] A. Taheri Najafabadi, *Int. J. Energy Res.* **2013**, *37*, 485.

[8] E. V. Kondratenko, G. Mul, J. Baltrusaitis, G. O. Larrazabal, J. Perez-Ramirez, *Energy Environ. Sci.* **2013**, *6*, 3112.

[9] N. S. Lewis, D. G. Nocera, *PNAS* **2006**, *103*, 15729.

[10] H. Lin, S. Luo, H. Zhang, J. Ye, *Joule* **2022**, *6*, 294.

[11] T. Hisatomi, K. Takanabe, K. Domen, *Catal. Lett.* **2015**, *145*, 95.

[12] E. Gong, S. Ali, C. B. Hiragond, H. S. Kim, N. S. Powar, D. Kim, H. Kim, S.-I. In, *Energy Environ. Sci.* **2022**, *15*, 880.

[13] S. Bardey, A. Bonduelle-Skrzypczak, A. Fécant, Z. Cui, C. Colbeau-Justin, V. Caps, V. Keller, *Faraday Discuss.* **2019**, *214*, 417.

[14] World Bank Group, "Global Solar Atlas", can be found under https://globalsolaratlas.info 2017.

[15] Data from Lafarge Port-La-Nouvelle cement plant **2014**.

[16] C. K. Ho, C. A. Sims, J. M. Christian, *Energy Procedia* **2015**, *69*, 1296.

[17] European Environment Agency, "Trees help tackle climate change", can be found under https://www.eea.europa.eu/articles/forests-health-and-climate-change/key-facts/trees-help-tackle-climate-change **2012**.

[18] Statista - Mine production of platinum worldwide from 2010 to 2022 - https://www.statista.com/statistics/1170691/mine-production-of-platinum-worldwide/.

[19] The Engineering Toolbox, "Solubility of Gases in Water vs. Temperature", can be found under https://www.engineeringtoolbox.com/gases-solubility-water-d **1148.html**.

[20] S. N. Habisreutinger, L. Schmidt-Mende, J. K. Stolarczyk, *Angew. Chem. Int. Ed.* **2013**, *52*, 7372.

[21] M. Gattrell, N. Gupta, A. Co, *Electroanal. Chem.* **2006**, *594*, 1.

[22] Y. Wang, Z. Zhang, L. Zhang, Z. Luo, J. Shen, H. Lin, J. Long, J. C. S. Wu, X. Fu, X. Wang, C. Li, *J. Am. Chem. Soc.* **2018**, *140*, 14595.

[23] M. Dilla, R. Schlögl, J. Strunk, *ChemCatChem* **2017**, *9*, 696.

[24] J. C. S. Wu, T.-H. Wu, T. Chu, H. Huang, D. Tsai, *Top Catal.* **2008**, *47*, 131.

[25] Z. Xiong, Z. Lei, S. Ma, X. Chen, B. Gong, Y. Zhao, J. Zhang, C. Zheng, J. C. Wu, *Appl. Catal. B: Environ.* **2017**, *219*, 412.

[26] S. S. Thind, M. Paul, J. B. Hayden, A. Joshi, D. Goodlett, J. Scott McIntyre, *Ind. Chem. Mater.* **2023**, *1*, 431.

[27] F. Li, Li Zhang, J. Tong, Y. Liu, S. Xu, Y. Cao, S. Cao, *Nano Energy* **2016**, *27*, 320.

[28] R. Katoh, A. Furube, *J. Phys. Chem. Lett.* **2011**, *2*, 1888.

[29] K. Kočí, L. Obalová, D. Plachá, Z. Lacný, *Collect. Czech. Chem. Commun.* **2008**, *73*, 1192.

[30] S. Singh, A. Modak, K. K. Pant, A. Sinhamahapatra, P. Biswas, *ACS Appl. Nano Mater.* **2021**, *4*, 8644.

[31] M. Dilla, A. Mateblowski, S. Ristig, J. Strunk, *ChemCatChem* **2017**, *9*, 4345.

[32] A. Hezam, K. Alkanad, M. A. Bajiri, J. Strunk, K. Takahashi, Q. A. Drmosh, N. Al-Zaqri, L. N. Krishnappagowda, *Small Methods* **2023**, *7*, e2201103.

[33] A. Hagfeldt, M. Graetzel, *Chem. Rev.* **1995**, *95*, 49.

[34] M. Dilla, N. G. Moustakas, A. E. Becerikli, T. Peppel, A. Springer, R. Schlögl, J. Strunk, S. Ristig, *Phys. Chem. Chem. Phys.* **2019**, *21*, 13144.

[35] S. Sorcar, S. Yoriya, H. Lee, C. A. Grimes, S. P. Feng, *Mater. Today Chem.* **2020**, *16*.

[36] S. Navalón, A. Dhakshinamoorthy, M. Alvaro, H. Garcia, *ChemSusChem* **2013**, *6*, 562.

[37] F. Sastre, A. V. Puga, L. Liu, A. Corma, H. García, *J. Am. Chem. Soc.* **2014**, *136*, 6798.
<figure><img src="image_23.png" /></figure>

[38] N. Ahmed, Y. Shibata, T. Taniguchi, Y. Izumi, *J. Catal.* **2011**, *279*, 123.

[39] L. Wang, M. Ghoussoub, H. Wang, Y. Shao, W. Sun, A. A. Tountas, T. E. Wood, H. Li, J. Y. Y. Loh, Y. Dong, M. Xia, Y. Li, S. Wang, J. Jia, C. Qiu, C. Qian, N. P. Kherani, H. Le, X. Zhang, G. A. Ozin, *Joule* **2018**, *2*, 1369.

[40] C.-C. Lo, C.-H. Hung, C.-S. Yuan, J.-F. Wu, *Sol. Energy Mater. Sol. Cells* **2007**, *91*, 1765.

[41] M. Tahir, B. Tahir, N. A. Saidina Amin, H. Alias, *Appl. Surf. Sci.* **2016**, *389*, 46.

[42] H. Zhang, Y. Izumi, *Front. Chem.* **2018**, *6*, 408.

[43] C.-C. Yang, J. Vernimmen, V. Meynen, P. Cool, G. Mul, *J. Catal.* **2011**, *284*, 1.

[44] N.-N. Vu, S. Kaliaguine, T.-O. Do, *Adv. Funct. Mater.* **2019**, *29*, 1901825.

[45] Z. Zhang, G. Yi, P. Li, X. Zhang, H. Fan, X. Wang, C. Zhang, Y. Zhang, *Int. J. Energy Res.* **2021**, *45*, 9895.

[46] Q. Wang, K. Domen, *Chem. Rev.* **2020**, *120*, 919.

[47] D. C. Hurum, A. G. Agrios, K. A. Gray, T. Rajh, M. C. Thurnauer, *J. Phys. Chem. B* **2003**, *107*, 4545.

[48] Ó. R. Andrade, V. Rodríguez, R. Camarillo, F. Martínez, C. Jiménez, J. Rincón, *Nanomaterials* **2022**, *12*.

[49] S. Bernadet, E. Tavernier, D.-M. Ta, R. A. L. Vallée, S. Ravaine, A. Fécant, R. Backov, *Adv. Funct. Mater.* **2019**, *29*, 1807767.

[50] K. Kim, A. Razzaq, S. Sorcar, Y. Park, C. A. Grimes, S.-I. In, *RSC Adv.* **2016**, *6*, 38964.

[51] H. She, Y. Wang, H. Zhou, Y. Li, L. Wang, J. Huang, Q. Wang, *ChemCatChem* **2019**, *11*, 753.

[52] S. Rashidi, A. Caringula, A. Nguyen, I. Obi, C. Obi, W. Wei, *Front. Energy* **2019**, *13*, 251.

[53] M. Asadi, B. Kumar, A. Behranginia, B. A. Rosen, A. Baskin, N. Repnin, D. Pisasale, P. Phillips, W. Zhu, R. Haasch, R. F. Klie, P. Král, J. Abiade, A. Salehi-Khojin, *Nat. Commun.* **2014**, *5*, 4470.

[54] L. Liu, H. Zhao, J. M. Andino, Y. Li, *ACS Catal.* **2012**, *2*, 1817.

[55] L. Liu, Y. Jiang, H. Zhao, J. Chen, J. Cheng, K. Yang, Y. Li, *ACS Catal.* **2016**, *6*, 1097.

[56] J. Yu, J. Low, W. Xiao, P. Zhou, M. Jaroniec, *J. Am. Chem. Soc.* **2014**, *136*, 8839.

[57] Y. Wei, J. Jiao, Z. Zhao, J. Liu, J. Li, G. Jiang, Y. Wang, A. Duan, *Appl. Catal. B: Environ.* **2015**, *179*, 422.

[58] M. Shahrokhi, P. Raybaud, T. Le Bahers, *ACS Appl. Mater. Interfaces* **2021**, *13*, 36465.

[59] J. Li, N. Wu, *Catal. Sci. Technol.* **2015**, *5*, 1360.

[60] J.-L. Bredas, *Mater. Horiz.* **2014**, *1*, 17.

[61] Y. L. Huang, Y. Chen, W. Zhang, S. Y. Quek, C. Chen, L. Li, W. Hsu, W. Chang, Y. J. Zheng, W. Chen, A. T. S. Wee, *Nat. Commun.* **2015**, *6*.

[62] K. F. Mak, C. Lee, J. Hone, J. Shan, T. F. Heinz, *Phys. Rev. Lett* **2010**, *105*, 136805.

[63] S. Sun, Q. An, M. Watanabe, J. Cheng, H. Ho Kim, T. Akbay, A. Takagaki, T. Ishihara, *Appl. Catal. B: Environ.* **2020**, *271*, 118931.

[64] P. Jia, R. Guo, W. Pan, C. Huang, J. Tang, X. Liu, H. Qin, Q. Xu, *Colloids Surf. A: Physicochem. Eng. Asp.* **2019**, *570*, 306.

[65] H. Qin, R. Guo, X. Liu, W. Pan, Z.-Y. Wang, X. Shi, J. Tang, C. Huang, *Dalton Trans.* **2018**, *47*, 15155.

[66] H. Jung, K. M. Cho, K. H. Kim, H.-W. Yoo, A. Al-Saggaf, I. Gereige, H.-T. Jung, *ACS Sustain. Chem. Eng.* **2018**, *6*, 5718.

[67] S. Yin, J. Li, L. Sun, X. Li, D. Shen, X. Song, P. Huo, H. Wang, Y. Yan, *Inorg. Chem.* **2019**, *58*, 15590.

[68] R. A. Geioushy, S. M. El-Sheikh, I. M. Hegazy, A. Shawky, S. El-Sherbiny, A.-H. T. Kandil, *Mater. Res. Bull.* **2019**, *118*, 110499.

[69] Y. Liu, Y. Li, F. Peng, Y. Lin, S. Yang, S. Zhang, H. Wang, Y. Cao, H. Yu, *Appl. Catal. B: Environ.* **2019**, *241*, 236.

[70] Y.-J. Yuan, Z.-J. Ye, H.-W. Lu, B. Hu, Y.-H. Li, D.-Q. Chen, J.-S. Zhong, Z.-T. Yu, Z.-G. Zou, *ACS Catal.* **2016**, *6*, 532.

[71] B. Chen, Y. Meng, J. Sha, C. Zhong, W. Hu, N. Zhao, *Nanoscale* **2017**, *10*, 34.

[72] S. Bai, L. Wang, X. Chen, J. Du, Y. Xiong, *Nano Res.* **2015**, *8*, 175.

[73] R. Favre, P. Raybaud, T. Le Bahers, *Phys. Chem. Chem. Phys.* **2022**, *24*, 2646.

[74] G. Zhang, Z. Wang, J. Wu, *Nanoscale* **2021**, *13*, 4359–4389.

[75] Y. Tang, Q. Liu, J. Lei, M. Zhang, H. Yang, M. Duan, X. Ma, T. Song, *Mater. Res. Express* **2022**, *9*, 105502.

[76] L. Zheng, F. Teng, X. Ye, H. Zheng, X. Fang, *Adv. Energy Mater.* **2020**, *10*, 1902355.

[77] C. Maheu, E. Puzenat, C. Geantet, L. Cardenas, P. Afanasiev, *Int. J. Hydrogen Energy* **2019**, *44*, 18038.

[78] W. Tu, Y. Li, L. Kuai, Y. Zhou, Q. Xu, H. Li, X. Wang, M. Xiao, Z. Zou, *Nanoscale* **2017**, *9*, 9065.

[79] F. Xu, B. Zhu, B. Cheng, J. Yu, J. Xu, *Adv. Opt. Mater.* **2018**, *6*, 1800911.

[80] L. Yu, Y. Xie, J. Zhou, Y. Li, Y. Yu, Z. Ren, *J. Mater. Chem. A* **2018**, *6*, 4706.

[81] S. Kang, H. Khan, C. S. Lee, *Sol. Energy Mater. Sol. Cells* **2021**, *221*, 110890.

[82] C. Larquet, S. Carenco, *Front. Chem.* **2020**, *8*, 179.

[83] C. G. Mosander, *Einiges über Cerium, Archiv für die gesammte Naturlehre*, vol. 5 (Eds; Johann Leonhard Schrag), Schrag, Nürnberg, **1827**, pp. 470–483.

[84] J. J. Pitha, A. L. Smith, R. Ward, *J. Am. Chem. Soc.* **1947**, *69*, 1870.

[85] E. Koyama, I. Nakai, K. Nagashima, *Acta Crystallogr.* **1984**, *B40*, 105.

[86] M. Inoue, Y. Ueda, H. Neigishi, M. Sasaki, T. Ohiba, Y. Kitano, Y. Komura, *J. Less-Common Met.* **1986**, *115*, 261.

[87] K. M. Abraham, D. M. Pasquariello, E. B. Willstaedt, *J. Electrochem. Soc.* **1989**, *136*, 576.

[88] D. M. Pasquariello, W. J. Dunn, K. M. Abraham, *IEEE* **1990**.

[89] A. Sahu, S. N. Steinmann, P. Raybaud, *J. Catal.* **2022**, *408*, 303.

[90] A. Rochet, B. Baubet, V. Moizan, C. Pichon, V. Briois, C. R. Chim. **2016**, *19*, 1337.

[91] D. Ryaboshapka, T. Len, P. Bargiela, M. Aouine, C. Geantet, V. Briois, L. Piccolo, P. Afanasiev, *ACS Catal.* **2023**, *13*, 10511–10526.

[92] J. L. DiMeglio, B. M. Bartlett, *Chem. Mater.* **2017**, *29*, 7579.

[93] C. M. Wolff, P. D. Frischmann, M. Schulze, B. J. Bohn, R. Wein, P. Livadas, M. T. Carlson, F. Jäckel, J. Feldmann, F. Würthner, J. K. Stolarczyk, *Nat. Energy* **2018**, *3*, 862.

[94] Cédric Lambin Joachim Jelken, María O. Avilés, François, Lagugné-Labartherth, *J. Phys. Chem. C* **2023**, *127*, 14270.

[95] P. Arunachalam, K. Nagai, M. S. Amer, M. A. Ghanem, R. J. Ramalingam, A. M. Al-Mayouf, *Catalysts* **2021**, *11*, 160.

[96] Q. Wang, M. Nakabayashi, T. Hisatomi, S. Sun, S. Akiyama, Z. Wang, Z. Pan, X. Xiao, T. Watanabe, T. Yamada, N. Shibata, T. Takata, K. Domen, *Nat. Mater.* **2019**, *18*, 827.

[97] J. C. Dupin, D. Gonbeau, I. Martin-Litas, P. Vinatier, A. Levasseur, *Appl. Surf. Sci.* **2001**, *173*, 140.

[98] M. Shahrokhi, T. Le Bahers, P. Raybaud, *Phys. Chem. Chem. Phys.* **2022**, *24*, 25440.

[99] M. Shahrokhi, P. Raybaud, T. Le Bahers, *J. Mater. Chem. C* **2020**, *8*, 9064.

[100] N. J. Mayhall, E. L. Becher, A. Chowdhury, K. Raghavachari, *J. Phys. Chem. A* **2011**, *115*, 2291.

[101] Q. Wu, A. B. Abdeta, D.-H. Kuo, H. Zhang, Q. Lu, J. Zhang, O. A. Zelekew, M. T. Mosisa, J. Lin, X. Chen, *J. Mater. Chem. A* **2022**, *10*, 5328.

[102] N. Iqbal, I. Khan, A. Ali, A. Qurashi, *J. Adv. Res.* **2022**, *36*, 15.

[103] X. Lu, C. Y. Toe, F. Ji, W. Chen, X. Wen, R. J. Wong, J. Seidel, J. Scott, J. N. Hart, Y. H. Ng, *ACS Appl. Mater. Interfaces* **2020**, *12*, 8324.

[104] Z. Yu, H. Yao, Y. Yang, M. Yuan, C. Li, H. He, T.-S. Chan, D. Yan, S. Ma, P. Zapol, M. G. Kanatzidis, *Chem. Mater.* **2022**, *34*, 798.

[105] Q. Wu, X. Wang, J. Fu, O. A. Zelekew, A. B. Abdeta, D.-H. Kuo, J. Zhang, Z. Yuan, J. Lin, X. Chen, *J. Sci.: Adv. Mater. Devices* **2021**, *6*, 578.

[106] S. F. Tadesse, D.-H. Kuo, W. L. Kebede, L. W. Duresa, *New J. Chem.* **2020**, *44*, 19868.

[107] N. Kodan, A. P. Singh, M. Vandichel, B. Wickman, B. R. Mehta, *Int. J. Hydrogen Energy* **2018**, *43*, 15773.

[108] K. T. Butler, R. Crespo-Otero, J. Buckeridge, D. O. Scanlon, E. Bovill, D. Lidzey, A. Walsh, *Appl. Phys. Lett.* **2015**, *107*, 231605.

[109] J. Kullgren, B. Aradi, T. Frauenheim, L. Kavan, P. Deak, *J. Phys. Chem. C* **2015**, *119* (38), 21952.

[110] T. Ohno, M. Akiyoshi, T. Umebayashi, K. Asai, T. Mitsui, M. Matsumura, *Appl. Catal. A: Gen.* **2004**, *265*, 115.

[111] M. Harb, P. Sautet, P. Raybaud, *J. Phys. Chem. C* **2013**, *117*, 8892.

<footnote>Manuscript received: March 15, 2024</footnote>

<footnote>Revised manuscript received: July 9, 2024</footnote>

<footnote>Version of record online: September 10, 2024</footnote>