December 1 - 6, 2024
Boston, Massachusetts
Symposium Supporters
2024 MRS Fall Meeting & Exhibit
EN01.04.03

Plasmon Photocatalysis for Sunlight-Powered Reduction of CO2 to CO—The Impact of Photothermal Heating of the Catalyst Bed on Reactor and Process Design

When and Where

Dec 3, 2024
9:15am - 9:30am
Hynes, Level 3, Room 300

Presenter(s)

Co-Author(s)

Pascal Buskens1,2,Francesc Sastre1,Jonathan van den Ham1,Man Xu1,3,Nicole Meulendijks1,Jelle Rohlfs1,Anthony Sanderse1,Roberto Habets1,Pau Martínez Molina1

TNO1,Hasselt University2,Delft University of Technology3

Abstract

Pascal Buskens1,2,Francesc Sastre1,Jonathan van den Ham1,Man Xu1,3,Nicole Meulendijks1,Jelle Rohlfs1,Anthony Sanderse1,Roberto Habets1,Pau Martínez Molina1

TNO1,Hasselt University2,Delft University of Technology3
To transition from the current fossil-based chemical industry to a climate neutral one, both the use of renewable energy and sustainable feedstock are essential. Here, we present the use of CO<sub>2</sub> as sustainable feedstock and sunlight as renewable energy source for the photocatalytic conversion of CO<sub>2</sub> to CO. Combined with green hydrogen, this provides access to renewable syngas, which is pivotal for the decarbonisation of industry.<sup>1</sup><br/>Various technologies are explored for CO<sub>2</sub> conversion to CO, including approaches driven by electrical or thermal energy. We selected photochemical conversion using sunlight, since it provides following advantages: (i) high energy efficiency with minimized conversion and transportation losses, (ii) high process selectivity with minimized need for energy and cost intensive downstream processing, (iii) ease of scaling up and down (numbering up) making a good fit with small, medium and large sized CO<sub>2</sub> sources, (iv) steep learning curves and fast cost reductions expected based on technology modularity, (v) decentralized and potentially off-grid production, and (vi) low carbon footprint for direct use of sunlight.<sup>2</sup><br/>The catalyst we developed for sunlight-powered production of CO is plasmonic Au/TiO<sub>2</sub>. This was prepared by deposition-precipitation of Au on anatase, and we achieved a Au loading of 3.12% w/w (ICP-AES).<sup>3,4</sup> The average size of the Au nanoparticles was 1.6 nm (lognormal distribution), and their (111) lattice planes were perfectly alligned with the (101) TiO<sub>2</sub> planes. The catalyst displayed a strong plasmonic absorption in the visible, with a maximum in the wavelength range between 500 nm and 600 nm. We demonstrated that under illumination with sunlight (irradiance up to 14.4 kW/m<sup>2</sup>), CO was produced at high selectivity of 98% without external heating of the reactor. In comparative dark experiments at similar catalyst bed temperature (~200<sup>○</sup>C), only CH<sub>4</sub> was produced. Under optimized conditions, we achieved a CO production rate of 429 mmol/g<sub>Au </sub>per hour, and reached an apparent quantum efficiency of 4.7%.<sup>3</sup> When studying the CO production rate as function of solar irradiance, we obtained an exponential relationship indicating the presence of a photothermal contributor.<sup>3,4</sup> To quantitatively distinguish between photothermal heating and non-thermal contributors, we performed experiments using a tailored fiber Bragg grating-based fiber optic sensor (FBG-FOS) for <i>in operando</i> temperature monitoring. We previously demonstrated this concept for off-line measurements only.<sup>5 </sup>The FBG-FOS enabled us to obtain temperature data during catalysis at various depths inside the catalyst bed: at the surface (0 mm), and at 0.15 mm, 0.30 mm and 0.50 mm depth. We observed substantial temperature gradients inside the catalyst bed during catalysis, with the highest temperature achieved at the surface of the catalyst bed. These temperature gradients are caused by the fact that more than 90% of the light was absorbed in the top 100 µm of the catalyst bed, as determined by UV-vis-NIR spectrophotometry. The temperature gradient remained intact due to the low thermal conductivity of the catalyst powder bed.<br/>To complete photochemical reaction systems for sunlight-powered chemical production, additional components such as reactors, solar concentrators and sensors for on-line process monitoring are required.<sup>6</sup> We designed a complete system for sunlight-powered reduction of CO<sub>2</sub> to CO, and validated it using natural sunlight as energy source. We will particularly highlight the impact of photothermal heating on reactor and process design.<br/><br/>[1] <i>ChemSusChem</i> <b>2024</b>, e202400059.<br/>[2] <i>Sustainable Energy Technologies and Assessments</i><b> </b><b>2024</b>,<i> 65</i>, 103768.<br/>[3] <i>ChemCatChem</i> <b>2021</b>, <i>13</i>, 4507.<br/>[4] <i>Chem. Asian J. </i><b>2023</b>, <i>18</i>, e202300405.<br/>[5] <i>ChemPhotoChem</i> <b>2022</b>, <i>6</i>, e202100289.<br/>[6] <i>ChemSusChem </i><b>2024</b>, <i>17</i>, e202301405.

Keywords

photochemical

Symposium Organizers

Virgil Andrei,
Rafael Jaramillo, Massachusetts Institute of Technology
Rajiv Prabhakar,
Ludmilla Steier, University of Oxford

Session Chairs

Virgil Andrei
Rajiv Prabhakar

In this Session