# Photocatalytic and Photothermal Catalytic Oxidation of Ethene and Ethanol Using TiO2-Based Catalysts under UV-C and UV-A Irradiation

Ravinraj Adaikan Ovannan, Frederic Dappozze, Chantal Guillard

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Ravinraj Adaikan Ovannan, Frederic Dappozze, Chantal Guillard. Photocatalytic and Photothermal Catalytic Oxidation of Ethene and Ethanol Using TiO2-Based Catalysts under UV-C and UV-A Irradiation. Photocatalysis: Research and Potential, 2024, 1 (3), pp.10006-10006. 10.35534/prp.2024.10006. hal-04747831

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Article

# Photocatalytic and Photothermal Catalytic Oxidation of Ethylene and Ethanol Using TiO₂-Based Catalysts under UV-C and UV-A Irradiation

Ravinraj Adaikan Ovannan, Frederic Dappozze and Chantal Guillard *

IRCELYON, UMR 5256, CNRS, Universite Claude Bernard Lyon 1, F-69100 Villeurbanne, France;
ravin1153@gmail.com (R.A.O.); frederic.dappozze@ircelyon.univ-lyon1.fr (F.D.)

* Corresponding author. E-mail: chantal.guillard@ircelyon.univ-lyon1.fr (C.G.)

Received: 28 June 2024; Accepted: 9 August 2024; Available online: Day Month Year

**ABSTRACT:** Photocatalytic (PCO) and photothermocatalytic oxidation (PTCO) of ethene (C₂H₄) and ethanol (EtOH) are investigated using TiO₂ and 1%Pt/TiO₂ coating on velvet glass support in the presence of UV-A and UV-C irradiation. Both VOC are efficiently mineralised under UV-A irradiation and PCO, but the presence of Pt has a minor impact on their transformation. Instead, there is only a slight increase in the disappearance of EtOH and the formation of acetaldehyde, which are already observed in the dark. Surprisingly, when a higher photon flux is emitted with a UV-C lamp, photocatalytic disappearance and mineralisation of EtOH are less effective than under UV-A irradiation in the presence or absence of Pt. Similar behaviour is also observed on C₂H₄ PCO in the presence of 1%Pt/TiO₂ but not on its PCO mineralisation with TiO₂, which is improved by a factor equivalent to the number of photons emitted. Under PTCO, by increasing the temperature from 40 °C to 120 °C, only a benefit impact is observed on C₂H₄ and EtOH disappearance but an important decrease of mineralization of C₂H₄ was observed in presence of TiO₂ and UV-C. The behaviour of these two VOCs under different irradiations and temperatures will be discussed according to the catalytic process.

**Keywords:** Photocatalysis; Photothermocatalysis; Ethylene; Ethanol; TiO₂; Pt/TiO₂; Temperature; UV-A; UV-C

<figure><img src="image_2.png" /></figure>

© 2024 The authors. This is an open access article under the Creative Commons Attribution 4.0 International License (https://creativecommons.org/licenses/by/4.0/).

## 1. Introduction

Volatile organic compounds (VOCs) are colourless organic chemicals released in the gas state due to their high volatility and low boiling point, such as acetone, carbon disulphide, ethylene (C₂H₄), ethanol (EtOH), formaldehyde, toluene and, xylene. C₂H₄ is a natural ripe-causing hormone of plants that helps grow and develop fruits and vegetables. It is a persistent pollutant in the Food and Vegetable (F&V) industry as it causes rapid maturation and deterioration in the storing environment at low temperatures, leading to food waste and money [1]. Meanwhile, EtOH is an emerging pollutant mainly due to the COVID-19 pandemic, increasing its rapid production and emission into the atmosphere due to its high volatility in the last two years. EtOH-based disinfectants can release around 6000 ppb to 8000 ppb in a closed area in an hour [2]. Prolonged exposure to the vast EtOH amount could lead to health risks and other environmental problems. Therefore, reducing the C₂H₄ to prolong F&V's shelf life and airborne EtOH content in the atmosphere is necessary.

Moving towards sustainable and greener goals, photocatalytic oxidation (PCO) and photothermal catalytic oxidation (PTCO) of VOCs, especially C₂H₄ and EtOH in the gas phase, have gained attention among researchers to control the VOCs' content in the atmosphere. When the photocatalyst absorbs light, PCO is a redox reaction carried out by photogenerated species, such as holes (h⁺) and electrons (e). In the case of PCO, h⁺ plays a central role since it oxidises VOCs into CO₂ [3], and e⁻ reduces O₂ into O₂⁻ which can also oxide VOC and avoids charge recombination. Similarly, PTCO is an extension of PCO, but it is carried out in the presence of light and heat energy generated either internally by photothermal materials or externally by a heat source [4]. In other words, it is similar to a combination of photocatalysis and thermal catalysis, i.e., catalysis at high temperatures without light irradiation. Thus, the oxidation of C₂H₄ and EtOH via photocatalysis and photothermal catalyst can be expressed as Equations (1) and (2).
$$C_2H_4 + 3O_2 \rightarrow 2CO_2 + 2H_2O \quad (1)$$

$$C_2H_5OH + 3O_2 \rightarrow 2CO_2 + 3H_2O \quad (2)$$

The most common catalyst used for PCO [5–8] and PTCO [9–13] is titanium dioxide alone or coupled with other materials, mainly metals such as Pt, Ag, Au, Ni to enhance the reaction efficiency Other common catalysts are also used in PTCO alone or coupled with TiO₂ such as ZnO, WO₃, and C₃N₄, CeO₂, bismuth-based photocatalysts,etc. [14–21]. Most of these are semiconductors because they possess a unique electronic structure with adequate band gap (Eg) that produces the photogenerated species, h⁺ and e⁻, through migration between valence band (VB) and conduction band (CB) during the photon irradiation, unlike metals and insulators. Primary recent phothermocatalytic researches deal with CO₂ conversion, CH₄ activation, NH₃ synthesis, and water splitting [4] or solar light in the presence of plasmon, allowing plasmonic localised heating [22]

Some studies have been carried out in oxidising C₂H₄ and EtOH using photocatalysis. Park et al. carried out gas-phased C₂H₄ PCO using TiO₂ in ultrafine powder. They studied the factors affecting the reaction and found anatase TiO₂ with a larger surface area, a big Eg and many hydroxyl groups result in higher reaction efficiency [23]. Similar observations were obtained using TiO₂ for photocatalytic oxidation of VOCs, especially C₂H₄ [24,25]

Furthermore, in Park et al.’s study [23], platinised TiO₂ with about 1wt% showed better C₂H₄ PCO than the unplatinised one with higher selectivity towards CO₂ without intermediates. Similarly, Vorontsov and Dubovitskaya observed a double increment in the reaction rate of EtOH PCO by Pt-loaded TiO₂ [26], supported by Murcia et al.[27]. However, Fraters et al. [28] showed that the effect of Pt nanoparticles largely depends on the substrate’s molecular functionality. For example, they found that Pt reduces the propane PCO activity, whereas a positive effect is observed on EtOH PCO. Publications on the effect of UV irradiation with different wavelengths and photon emission rates on gaseous C₂H₄ and EtOH oxidation or another VOC are rare. Pathak et al. [29] mentioned that UV-C lamp with higher photon emission and shorter wavelength produces complete oxidation of C₂H₄, unlike under UV-A. However, the UV-C lamp used is not only 254 nm but also a wavelength of 185 nm and Farhanian et al. [30] show a different behaviour between UV-C lamps, including 185 nm or not on EtOH PCO. In particular, crotonaldehyde is formed in the presence of 185 nm but not observed under only 254 nm. The works of Couts et al. on EtOH [31] and Kaneva et al. [32] on C₂H₄ PCO show that UV-C light gives a higher conversion degree owing to the higher photon energy than UV-A light.

Apart from photocatalysis, platinum (Pt) loading on TiO₂ has greatly interested experts in photothermal catalysis. Pt is a non-plasmonic material [33] and has been shown to enlarge the catalyst’s absorption spectrum from UV to visible light, which drives both photon flux (UV and Visible flux) and heat energy during the PTCO [34]. Zorn et al. studied a mixture of TiO₂ and ZrO₂ as a catalyst over temperatures below 110 °C on PTCO of C₂H₄ [35]. They found that platinum catalyst improves the photocatalytic reaction of ethylene from a temperature above 70 °C. Fu et al. support the idea that platinised catalysts have a vast potential for photothermal catalytic applications through their study on C₂H₄ [36]. However, neither of these publications mentions whether there is a synergy between photocatalysis and thermocatalysis for C₂H₄ degradation and mineralisation or the impact of light sources on PTCO.

On the other hand, Kennedy and Datye [37], investigating EtOH PTCO using Pt/TiO₂, found that the complete oxidation into CO₂ significantly surpasses the combined contribution of photo-oxidation over TiO₂ and thermal processes. They suggest that Pt thermal activity for acetaldehyde oxidation, formed from EtOH on TiO₂, becomes significant on Pt/TiO₂, favouring the oxidation pathway to CO₂ [37]. These results agree with the works of Vorontsov et al. [26], which showed that acetaldehyde oxidation is favoured on Pt/TiO₂. Besides, the effect of the Pt loading method on the PTCO reaction is discussed in their work. The photo-reduced approach, i.e., photodeposition of Pt on the catalyst, results in higher EtOH conversion and CO₂ mineralisation than the thermal reduction method, i.e., impregnation or adsorption.

Our study aims to understand better the impact of Pt, temperature and nature of light (UV-C and UV-A) on the conversion and mineralisation of two VOC, C₂H₄ and EtOH using TiO₂ coated on a velvet glass support and determine (i) if activation of photocatalyst under UV-C allow improving the PCO and PTCO of these both VOC, (ii) if the presence of Pt is essential, (iii) if a synergy is really obtained between photocatalysis and thermal catalysis and finally (iv) if a general behaviour of the impact of these parameters can be generalised.
## 2. Experimental Setup

### 2.1. Materials

Commercia TiO₂, Hombikat UV-100, is purchased from Sachtleben Chemie. It is a pure anatase phase with a surface area of about 300 m²/g. Around 18 cm × 10 cm glass velvet is used as support, supplied by the industrial partner, TREFFLER. Hydrogen hexachloroplatinate (IV) hydrate is purchased from SigmaAldrich (Saint Louis, Missouri, USA)® to synthesise platinised catalyst. C₂H₄ (497 ppmV in the air) and EtOH (1040 ppmV in air) are purchased in gas cylinders from Air Liquide and Messer.

### 2.2. Deposition of Catalyst on the Glass Velvet Support

Glass velvet from Treffler company has been used as support (Figure 1). The glass velvet is washed with distilled water and oven-dried at 200 °C overnight. An aqueous suspension of TiO₂ is sprayed on the dry velvet and dried at 200 °C overnight on the velvet's surface. About 4 mg/cm² measured by ICP-OES was coated on velvet support.

<figure><img src="image_3.png" /><figcaption>**Figure 1.** Schematic diagram of the experimental setup for the photocatalytic test using a 255 cm³ volume stainless steel tubular reactor with UV lamp (a) and catalyst supported on glass velvet support (b).</figcaption></figure>

### 2.3. Synthesis of Platinised TiO₂

A sample of Pt/TiO₂ is prepared under photo-deposition using about 1% of Pt, which is the best for photothermal catalysis [26]. The photodeposition method is based on M. Yamamoto et al. [38]. Around 5.76 g of TiO₂ (Hombikat UV-100) is mixed in 100 mL of distilled water. Similarly, 0.46 g of hydrogen hexachloroplatinate (IV) hydrate is measured as a Pt precursor and added to the TiO₂ suspension. EtOH with a concentration of 13.06 M is measured at 2.3 mL and added to the suspension as a hole scavenger. The mixture is illuminated under a UV-C lamp under continuous stirring and 10 mL/min argon purging for 72 h. Then, the suspension is centrifuged and dried at 200 °C in the oven overnight. The resulting catalyst is labeled as photo-reduced 1wt% Pt/TiO₂.

### 2.4. Photocatalytic and Photothermal Catalytic Test

Both tests are carried out in a stainless steel tubular reactor with a length of 27 cm. The light source (UV lamp) is mounted inside the reactor using a removable quartz glass tube with an outer diameter of 2 cm. There is a space between the glass tube and the reactor wall to place the glass velvet, the industrial support from which the catalyst is deposited.
The total volume of the reactor available for VOC is 255 cm³. Each side end of the reactor is screwable, allowing the users to change the catalyst accordingly, as shown in Figure 1. For photothermal catalytic tests, the tubular reactor is wrapped with a heating pad connected to a thermocouple and temperature controller for the heat supply, while the photocatalytic tests are carried out without it. Two UV lamps, Vilber-Lourmat (L = 265 mm, diameter = 15 mm) are utilised in the study: UV-A (365 nm) and UV-C (254 nm). The resulting stream from the reactor is analysed using GC FID Varian 3800 and GC FID-PDHID Clarus 500 for C₂H₄ and EtOH oxidation, respectively.

VOC, C₂H₄ or EtOH, is directly supplied from a gas tank and mixed with compressed air, composed of oxygen and nitrogen at 8 bar. A flowrate of 1 litre/min of VOC at different concentrations is used for the tests. Photocatalytic tests are done without heating. However, the UV lamp produces heat, causing a temperature rise from 25 °C to around 50 °C. Besides, the temperature range studied for the photothermal catalytic test is from 50 °C to 130 °C in both dark and UV irradiance. Since the photocatalysis is observed at 50 °C under UV irradiance, photothermal catalysis is studied at temperatures above the PC's temperature with an external heating supply. For the photothermal catalytic test, the temperature is increased to the desired value once the VOC enters the reactor. The UV lamp is turned on after reaching the adsorption-desorption equilibrium without UV irradiation.

Before every test, the glass-supported catalyst is treated and cleansed under the irradiance of a UV-C lamp and air flowrate of 200 mL/min overnight inside the reactor. Then, the test is started with the VOC concentration until stabilisation at the desired concentration for about 1 to 1.5 h without passing through the reactor (Step 1). It is followed by flowing the VOC stream into the reactor using valves to reach adsorption-desorption equilibrium on the glass-supported catalyst's surface for about 4 h (Step 2) before turning on the UV lamp (Step 3). For photothermal catalytic tests, stabilisation at the desired temperature is carried out simultaneously using the controller attached to the heating pad. Thermal catalysis or VOC catalytic oxidation, if any, is studied in the dark until equilibrium was reached. Then, the UV lamp is turned on, and VOC oxidation is carried out for 4 h.

VOC conversion (%), product yields (%C) and mineralisation (%) are calculated as follows:

$$ 
\begin{aligned}
Conversion (\%) &= \frac{VOC degraded}{Initial VOC} \times 100\% \\
Product i (\%C) &= \frac{Product i concentration}{VOC degraded concentration} \times \frac{Product i carbon number}{2} \times 100\% \\
Mineralisation(\%) &= \frac{CO_2 formed (ppbV)}{VOC degraded and absorbed (ppbV)} \times 100\%
\end{aligned}
$$

## 2.5. Analytical Procedure

### 2.5.1. Analysis of VOC

Ethylene and CO₂ concentrations are monitored on a Varian ((Agilent Technologies, Palo Alto (CA) USA)) 3800 GC-FID system with an automated injection gas valve using a 500 µL loop. Columns used are a Varian CPSil-5 (50 m × 30 mm × 1.2 µm) followed by SupleQPlot (Supelco – 30 m × 0.32 mm × 15 µm). The injector and oven are set at 30 °C for all the analysis. Helium is used as a gas vector (4.4 mL/min). The FID detector (Varian inc., Agilent Technologies, Palo Alto (CA) USA) ) (250 °C) is preceded by a methanization module made of heated (400 °C) nickel powder heated under hydrogen flow.

EtOH is analysed with a Clarus 500 gas chromatograph (Perkin Elmer, Waltham, MA, USA). Separation occurs on an RT-Q-Bond column (25 m × 0.53 mm × 20 µm). The oven is set at 50 °C then heated at 20 °C/min to 200 °C. A Polyarc® (Activated Research Company, Eden Prairie, MN, USA) module is used as an oxidiser/methanizer to transform all carbonated molecules into CO₂ and methane before FID (250 °C) detection.

### 2.5.2. Analysis of the Number of Photons

A CCD Spectrometer Avantes AvaSpec-ULS2048 (Avantes B.V., Apeldoorn, The Netherlands) is used to measure the emission spectra of both lamps. Before the analysis, a calibration is carried out using a Deuterium Halogen Light Source. Light intensities received by the catalyst have been determined using a VLX-3W radiometer equipped with a UVA-365 nm ± 10 nm probe and UVC_254 ± 10 nm, depending of the lamp used. Optical properties of both UV lamps are given in Table 1.
<table><caption>**Table 1.** Optical properties of UV lamps.</caption><thead><tr><th>Parameters</th><th>UV-A</th><th>UV-C</th></tr></thead><tbody><tr><td>Lamp surface area</td><td>122.5 cm<sup>2</sup></td><td></td></tr><tr><td>Irradiance on support surface</td><td>3.54 mWatt/cm<sup>2</sup></td><td>8.7 mWatt/cm<sup>2</sup></td></tr><tr><td>Luminous power</td><td>0.434 W</td><td>1.066 W</td></tr><tr><td>Photon flux</td><td>8 × 10<sup>17</sup> ± 1 photons/s</td><td>13.6 × 10<sup>17</sup> ± 1.4 photons/s</td></tr></tbody></table>

### 3. Result and Discussion

#### 3.1. Photocatalytic Degradation (PCO)

##### 3.1.1. Comparison of C₂H₄ and EtOH Photocatalytic Oxidation (PCO)

PCO of C₂H₄ and EtOH have been studied in the presence of platinised and unplatinised TiO₂ Hombikat coated on velvet glass. The profiles of C₂H₄ and C₂H₅OH concentration versus time during PCO in the presence of unplatinised TiO₂ Hombikat are shown in Figure 2a,b.

<figure><img src="image_4.png" /><figcaption>**Figure 2.** Profile of C₂H₄ concentration (a) and C₂H₅OH concentration (b) versus time during PCO in the presence of 100 ppmV of VOC and TiO₂ Hombikat coated on velvet glass.</figcaption></figure>

Depending on the VOC type, after overnight UV treatment, a distinct photocatalytic pattern is observed for each degradation on the velvet glass (Figure 2). After the first step (Step 1) of VOC stabilisation outside the reactor, no or negligible adsorption of C₂H₄ on photocatalytic material was detected after introducing C₂H₄ into the reactor where the catalyst is placed (Step 2), but adsorption of EtOH occurs. This behavior is due to the presence of the OH group in EtOH favoring hydrogen bonds with the surface of the hydrated catalyst. Moreover, after achieving adsorption equilibrium, EtOH does not return to its initial concentration, suggesting dissociative EtOH adsorption on TiO₂ [39,40]. About 17% of EtOH appears to be irreversibly adsorbed. At the same time, no CO₂ concentration or new compound is detected during these two steps for both VOCs.

Once the UV lamp is illuminated (Step 3), the concentration of CO₂ shoots up while both VOC concentration decreases, reaching equilibrium as time goes by. As for EtOH, the formation of acetaldehyde (MeCHO) is detected as a by-product, whereas no by-product was observed with C₂H₄, including the formation of formaldehyde not detected in our analytical conditions or other products remaining adsorbed. Indeed, in the given conditions, only 60% was mineralised (Table 2). Table 2 indicates the adsorption, conversion, mineralisation and by-product detected during the PCO of C₂H₄ and EtOH.
<table><caption>**Table 2.** Percentage of conversion, mineralisation and by-product detected during PCO of C₂H₄ and EtOH in the presence of TiO₂ Hombikat. Remarks: All % conversion, mineralisation and by-products are taken into account of the initial concentration of VOC disappeared and not the VOC concentration after adsorption.</caption><thead><tr><th>VOC (TiO<sub>2</sub> Hombikat)</th><th>VOC Adsorbed % Adsorbed</th><th>VOC Converted % Conversion</th><th>CO<sub>2</sub> % Mineralisation</th><th>MeCHO % by-Product</th></tr></thead><tbody><tr><td>C<sub>2</sub>H<sub>4</sub></td><td>&lt;1</td><td>48%</td><td>60%</td><td>/</td></tr><tr><td>EtOH</td><td>13%</td><td>88%</td><td>67%</td><td>11%</td></tr></tbody></table>

It is also crucial to highlight that some nonidentified by-products are formed but less extended compared to C₂H₄ degradation. The comparison of PCO of EtOH and ethylene shows that EtOH is more easily degraded than C₂H₄ but that both VOC are not entirely mineralised in the given conditions.

### 3.1.2. Impact of the Presence of Pt/TiO₂ on C₂H₄ and EtOH PCO

Results of PCO of C₂H₄ and EtOH in the presence of 1%Pt/TiO₂ Hombikat are reported in Table 3 and compared to those obtained without platinium in Table 2.

<table><caption>**Table 3.** % of conversion, mineralisation and by-product detected during PCO of C₂H₄ and C₂H₅OH in the presence of 1%Pt/TiO₂ Hombikat. Remarks: all % conversion, mineralisation and by-products are taken into account of the initial concentration of VOC disappeared and not the VOC concentration after adsorption.</caption><thead><tr><th>VOC (1%Pt/TiO<sub>2</sub> Hombikat)</th><th>% Transformed Under Dark</th><th>% Conversion</th><th>% Mineralisation</th><th>% CH<sub>3</sub>CHO</th></tr></thead><tbody><tr><td>C<sub>2</sub>H<sub>4</sub></td><td>&lt;1</td><td>48%</td><td>65%</td><td>/</td></tr><tr><td>EtOH</td><td>50%</td><td>95%</td><td>67%</td><td>13%</td></tr></tbody></table>

Pt loading on TiO₂ seems to have no or slight improvement in the conversion and mineralisation of C₂H₄ and et OH (Figure 3a,b). Specifically, the presence of Pt seems to improve the mineralisation of C₂H₄ and the conversion of EtOH slightly. However, a significant impact on the EtOH adsorption is observed in the presence of 1%Pt/TiO₂ (Figure 3c), approximately 50% compared to 13% in the absence of Pt with a slight increase of MeCHO formation, which may correspond to the slight improvement in C₂H₅OH conversion.

The impacts from the Pt on C₂H₄ oxidation at near ambient temperature is in agreement with the works of Zorn et al. [35,36] and with the observation of Fraters et al., showing that the effect of Pt nanoparticles on TiO₂ is mainly dependent on the nature of the substrate by working with propane and EtOH [28]. However, Pt has a negative impact on propane oxidation, an essential improvement of EtOH oxidation, and a more critical formation of acetaldehyde and mineralisation. They attributed this difference to the strong adsorption of EtOH on the TiO₂ surface, likely forming ethoxy groups and inhibiting oxygen activation over TiO₂. In this case, the presence of Pt enormously improved the EtOH adsorption but only slightly the formation of MeCHO. However, under irradiation at a temperature of about 40–45 °C induced by the lamp’s heat, only a slight improvement of EtOH oxidation is noted, while no improvement in CO₂ was observed. Likely, ethoxy groups are formed, as Fraters et al. [28] suggested, but seem to have only a little or no impact on photocatalysis at this temperature.

<figure><img src="image_5.png" /><figcaption>**Figure 3.** Comparison of the C₂H₄ (a) and EtOH (b) PCO in the presence of TiO₂ Hombikat and 1%Pt/TiO₂ under UV-A. Adsorption of EtOH and formation of CH₃COH in the dark in the presence of TiO₂ Hombikat and 1%Pt/TiO₂ (c).</figcaption></figure>
3.1.3. Impact of UV Light Type

The effect of UV-A and UV-C lamps is studied for the PCO of C₂H₄ and EtOH in the presence of TiO₂ and 1%Pt/TiO₂ (Figure 4).

<figure><img src="image_6.png" /><figcaption>**Figure 4.** Comparison of C₂H₄ and EtOH conversion and mineralisation and formation of CH₃COH in the presence of TiO₂ Hombikat and 1%Pt/TiO₂ under UV-A and UV-C. Remarks: The conversion and mineralisation of EtOH are calculated based on the initial concentration that disappeared.</figcaption></figure>

In the presence of unplatinised and platinised TiO₂, no improvement in the conversion of both VOC is obtained under UV-C, where a higher photon flux is emitted. A detrimental effect has even been observed in the degradation of C₂H₄. These behaviours are unlike the expected results. A higher photon generation should enable a higher (e⁻-h⁺) pair generation, improving conversion [30, 41–45], contradicting the study's findings. However, a higher percentage of mineralisation was observed in the presence of C₂H₄ and unplatinised TiO₂, suggesting the degradation of by-products under the UV-C lamp.

Moreover, with both catalysts, the UV-C lamp improves the formation of MeCHO. The difference observed between the behaviour of C₂H₄ and EtOH under UV-C is not due to the double bond in C₂H₄, which could favour photochemistry over photocatalysis. In fact, the PCO of C₂H₆ has the same behaviour as C₂H₄, where its conversion is less efficient in the presence of UV-C irradiation (Figure 5). Therefore, the absence of an increase in the efficiency under UV-C could be explained by the limitation of the catalyst activation by UV-C due to its lower penetration in the velvet glass compared to UV-A due to the nature of support which is in Quartz and can absorb UV-C and not UV-A.
In the case of Pt/TiO₂, the conversion and mineralisation are less impacted, probably due to the catalyst's darker grey colour limiting the penetration of both UV. These are just hypotheses; further study is required on the UV lamp effect.

<figure><img src="image_7.png" /><figcaption>**Figure 5.** Photocatalytic degradation of ethane (C₂H₆) in the presence of TiO₂ UV-100 (Hombikat) under UV-A and UV-C.</figcaption></figure>

## 3.2. Photothermal Catalytic Test (PTCO)

The impact of temperature on C₂H₄ and EtOH degradation is studied using TiO₂ UV-100 (Hombikat) unplatinized (Figure 6) and platinised (1% Pt/TiO₂) (Figure 7). It is important to note that when the lamp is on, the temperature in the reactor is approximately 50 °C. So, the initial PTCO temperature of 50 °C corresponds to PCO since it is due to the heat from the UV lamp solely without any external heating source.

<figure><img src="image_8.png" /><figcaption>**Figure 6.** Impact of temperature in the presence of UV-A or UV-C or absence of light on conversion (a,b) and mineralisation (c,d) of C₂H₄ (a,c) and EtOH (b,d) in the presence of TiO₂ Hombikat.</figcaption></figure>
<figure><img src="image_9.png" /><figcaption>**Figure 7.** Impact of temperature in the presence of UV-A or UV-C or absence of light on conversion (a,b) and mineralisation (c,d) of C₂H₄ (a,c) and EtOH (b,d) and on the formation of MeCHO (e) in the presence of 1%Pt/TiO₂ Hombikat.</figcaption></figure>

In the presence of unplatinised TiO₂, whether under UV (UV-A or UV-C) or in the dark, temperature does not affect the conversion of C₂H₄ and EtOH (Figure 6a,b). Moreover, while temperature does not affect mineralisation under UV-A and UV-C during the EtOH degradation (Figure 6d) and under UV-A during the C₂H₄ degradation, there is a significant reduction in mineralisation of C₂H₄ observed under UV-C (Figure 6b). This lower activity could be resulted from the formation of the precursor of polymer such as propylene or butene favoured with temperature [46–49] and under UV-C irradiation [50,51].

A different behaviour is observed when 1% Pt is present on TiO₂. In the presence or absence of UV, a significant increase in C₂H₄ and EtOH conversion is observed (Figure 7a,b), and to a lesser extent in the mineralisation (Figure
7c,d). In the dark, the conversion of C₂H₄ is already increased from a few % at 50 °C and continues to increase to more than 80% at 120 °C while the mineralisation increases from 60% to 75%. In the case of EtOH, the conversion is improved from 47% to 74% while the mineralisation increases from about 3% to 11%.

Based on the comparison study between platinised and unplatinised catalysts, platinised catalyst exhibits better efficiency than the unplatinised one under illumination at increasing temperature, reaching the highest C₂H₄ conversion and CO₂ mineralisation of 88% and 83%, respectively, at 124 °C. In the dark, the unplatinised catalyst does not display any activity but platinised one demonstrates catalytic oxidation through thermal catalysis as temperature increases. Until 90 °C, its conversion efficiency is lower than unplatinised one exposed to UV-A, then its performance increases, while its CO₂ mineralisation increases with the temperature. Therefore, it is evident that 1% Pt/TiO₂ causes the catalyst to exhibits both photo and thermal catalytic activity, producing a photothermal catalyst.

Like C₂H₄ PTCO, Pt with 1%Pt on TiO₂ increases the catalyst's performance in the EtOH PTCO at a similar temperature range. Platinised catalysts exhibit thermal-assisted photocatalysis, where the reaction is driven mainly by light, with heat assisting it [33]. It is because unplatinised catalysts have better activity under UV irradiance than platinised catalysts in the dark, indicating that heat boosts photocatalysis rather than driving it simultaneously, as in C₂H₄ PTCO. Another significant observation is that platinised catalysts produce more MeCHO without UV irradiation than the unplatinised ones. It is mainly due to the thermal catalytic oxidation observed during the formation of MeCHO by the Pt catalyst in the dark. However, under UV irradiation, its formation is limited (Figure 7e).

Therefore, the study's results agree with several studies indicating Pt loading increases the photocatalyst's performance in PTCO conversion of C₂H₄ [35,36] and EtOH [26,37], provided that the temperature is higher than about 70-80 °C. These works show that photocatalysis and thermal catalysis drive the reaction simultaneously. However, the word "synergy" used in some publications [12,33,52] dealing with photothermocatalysis does not correspond to our results. Indeed, in this case, the activity is not greater than the contribution from photo-oxidation over TiO₂ plus thermal oxidation over Pt. Is there a synergy in the studies of photothermocatalysis due to the different types of mechanism (plasmonic localised heating, thermal vibration of molecules and non-radiative relaxation in semiconductors) or to the type of reaction used (inert atmosphere against air in our reaction)? It would be fascinating to explore this behaviour further.

## 4. Conclusions

The photocatalytic degradation (PCO) and photo-thermocatalytic degradation (PTCO) of C₂H₄ and EtOH are studied using glass velvet impregnated using TiO₂ UV-100, with or without 1% Pt under UV-A or UV-C irradiation. Significant differences in the adsorption of volatile organic compounds (VOCs) in the absence of light, as well as variations depending on the presence of Pt on TiO₂, are observed. While C₂H₄ is little adsorbed onto either catalyst, EtOH shows notable adsorption, especially on 1%Pt/TiO₂ (50%) and to a lesser extent on non-platinised TiO₂ (13%). Adsorption is dissociative in both cases, forming acetaldehyde in the presence of 1%Pt/TiO₂.

Under PCO UV-A irradiation, EtOH is converted approximately two times faster than C₂H₄ in the presence of TiO₂, although their mineralisation is relatively similar. Approximately 60 to 70 ppmv of these VOCs are mineralised under our specific flux and light power conditions. The presence of 1% Pt on TiO₂ seems to have only little effect on VOCs' photocatalytic conversion and mineralisation.

Under PCO UV-C, although its photon flux is higher, neither the conversion nor the mineralisation of VOCs is improved on Pt or non-Pt TiO₂. Unexpectedly, the conversion of C₂H₄ is even halved under UV-C while its mineralisation is improved, indicating a preference for the degradation of by-products formed under UV-C. This behaviour is also observed during the degradation of ethane, suggesting that the presence of a double bond on C₂H₄ is not the cause of this efficiency decrease. This behaviour in the presence of PCO UV-C compared to PCO UV-A could be explained by the lower penetration of UV-C compared to UV-A. In the case of 1%Pt/TiO₂, the conversion and mineralisation are less impacted, probably due to the darker grey colour of the catalyst limiting the penetration of both UV types. These are just hypotheses; further study is required on the effect of UV lamps.

Under PTCO in the presence of TiO₂, temperature appears to have no beneficial effect on converting C₂H₄ and EtOH. It even has a detrimental impact on C₂H₄ mineralisation under UV-C, attributed to the formation of precursors of polymers such as propylene or butene favored by temperature and UV-C. A different behavior is observed when 1%Pt is present on TiO₂. So, the presence of Pt in TiO₂ appears essential for PTCO reaction. Through thermal catalysis, Pt enables the elimination and mineralisation of C₂H₄ from around 50 °C, while it mainly promotes the adsorption of EtOH and, to a lesser extent, the formation of acetaldehyde. Due to the catalytic properties of Pt, the disappearance of these two VOCs, and to a lesser extent, their mineralisation, is improved under "photothermocatalysis". However, can
we speak of the synergy between photocatalysis and catalysis? Isn't it simply the addition of these two types of reactions that we call “photothermocatalysis”? It is also important to emphasise that at 120 °C, these two reactions are equally effective, and beyond this temperature, photonic activation loses its interest. However, it is important to highlight the impact of temperature in the presence of Pt/TiO₂ under UV-C, which helps to avoid the decrease in efficiency probably due to its impact on the formation of polymer precursor. This impact will need to be further explored in the future.

**Author Contributions:** Conceptualization, Chantal Guillard; Methodology, Chantal Guillard and Frederic Dappozze; Validation, Chantal Guillard; Formal Analysis, Ravinraj A. Ovannan and Frederic Dappozze; Investigation, Ravinraj A. Ovannan.; Data Curation, Chantal Guillard; Writing - Original Draft Preparation, Ravinraj A. Ovannan.; Writing - Review & Editing, Chantal Guillard; Visualization, Chantal Guillard.; Supervision, Chantal Guillard; Funding Acquisition, Chantal Guillard",

**Ethics Statement:** Not Applicable

**Informed Consent Statement:** Not Applicable

**Funding:** This research received no external funding

**Declaration of Competing Interest:** The authors declare that they have no known competing financial interests or personal relationships that could have appeared to influence the work reported in this paper

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