The utilization of carbon dioxide (CO₂) as a C₁ building block has emerged as a promising strategy for sustainable chemical production. Among various CO₂-derived products, formate and formic acid are particularly attractive due to their roles as hydrogen carriers, fuel cell feedstocks, and industrial intermediates. Recent advances in Ru-based homogeneous catalysis have enabled efficient hydrogenation of bicarbonate, which was prepared from CO₂, in biphasic and triphasic systems. In this study, we employed a continuous stirred-tank reactor (CSTR) for the triphasic hydrogenation of KHCO₃ under high-pressure conditions (50 bar of H₂), and optimized the stirring conditions using a view cell to ensure efficient mixing. A kinetic model assuming a slow-reaction regime and incorporating the reverse reaction was developed, which accurately predicted the residence time–yield relationship and enabled high formate yields through residence-time optimization. Furthermore, the addition of tris(2,4-di-tert-butylphenyl)phosphite as an antioxidant effectively suppressed residual oxygen contamination, which is a known challenge in flow systems. Catalyst recycling and phase separation were successfully integrated into the flow setup, demonstrating the practicality and scalability of the process. These findings provide a rational framework for designing continuous triphasic hydrogenation systems and contribute to the development of resource-efficient chemical technologies based on CO₂ utilization.

Ammonia (NH₃) is vital for synthesizing fertilizers and has gained great attention as a carbon-free hydrogen carrier and a hydrogen-rich fuel. Electrochemical ammonia synthesis from nitrate in a water-fed polymer electrolyte membrane electrolyzer is an innovative approach to wastewater treatment. However, the major hurdles to practical implementation are competing hydrogen evolution reactions (HERs) and constrained catalytic efficiency. Herein, we demonstrate the use of polyvinylpyrrolidone (PVP)-modified ruthenium (Ru) nanoparticles as a strategy to drive the desired reaction of nitrate to ammonia. The particle size of Ru was controlled by PVP, enhancing the metal-utilization efficiency and the electrochemical active surface area. PVP modification was found to alter the electron density on Ru, suppressing the HER by increasing the energy barrier of hydrogen coupling to form H₂, while promoting absorbed hydrogen (H*) formation, facilitating the hydrogenation of intermediates to ammonia. Benefiting from the combined effects, PVP-10 wt % Ru/C achieved an ammonia production rate of 3800 μg·mg_Ru^–1·h^–1, compared to 590 μg·mg_Ru^–1·h^–1 for 40 wt % Ru/C at 2 V.

Single-atom catalysts, which consist of isolated metal sites immobilized on the support, have attracted significant attention in heterogeneous catalysis due to their high catalytic performance. The so-called strong electrostatic adsorption (SEA), in which a metal precursor is deposited onto an oxide support by electrostatic attraction, is widely employed to obtain single-atom catalysts in wet synthesis. In this work, we investigated the adsorption behavior of Re precursor, perrhenate, on anatase titania as an example of SEA studied by in situ attenuated total reflection infrared (ATR-IR) spectroscopy. The study confirms that the adsorption of perrhenate on titania is enhanced at a lower pH, which is consistent with a SEA model, and that the adsorption and desorption processes are reversible at pH 3.0. The ATR-IR spectroscopic kinetic analysis of the adsorption processes of perrhenate in nitric acid, assuming the Langmuir adsorption model, reveals that the kinetics of the perrhenate adsorption onto titania is influenced by the ionic strength. Furthermore, the adsorption mechanism of perrhenate changes depending on pH between 3.0 and 5.0. This study demonstrates that in situ ATR-IR spectroscopy is a powerful tool for the real-time monitoring and the kinetic study of SEA processes to design atomically engineered catalytic active sites.

Integrated CO₂ capture and reduction (CCR) using dual-function materials (DFMs) has emerged as a promising strategy for effective utilization of CO₂. A thorough understanding of the reaction mechanisms of CCR using the DFMs is important for enhancing their performances. In this study, Na/Al₂O₃ and Na/Cu/Al₂O₃ were compared to investigate the role of Na-based DFMs, particularly transition-metal-free DFMs, in facilitating CCR to CO. Fixed-bed experiments comprising of CO₂ capture and reduction phase were performed to examine their performances at various temperatures. The two DFMs exhibited similar behaviors during the CO₂ capture phase. In the subsequent reduction phase, the DFMs produced nearly equal amounts of CO, reaching 0.21 mmol/g, at temperatures exceeding 450 °C. By increasing the temperature to 500 °C, the CO production rates reached an identical level of 0.18 mmol/(min·g). Time-resolved in-situ spectroscopy confirmed the formation of carbonate species during the capture phase. Carbonates were further reduced to CO directly or via intermediate formate species in the reduction phase. The formation of formates was predominant on Na/Cu/Al₂O₃ at temperatures below 400 °C. However, at higher temperatures, the direct reductive decomposition of carbonates to form CO became the dominant pathway for both the DFMs. Elucidation of a more detailed mechanism of the direct reductive decomposition pathway is critical, particularly the role of Na sites during the reduction phase.

Green hydrogen plays a crucial role in decarbonization and the future of low-carbon society. Still, its transport/distribution and cost of production, mainly realized by electrolysis, are major hurdles. Liquid H₂ carriers reduce transport/distribution costs but add further expenses for their production. To address this challenge, we proposed a novel strategy for electrocatalytic production of a liquid organic hydrogen carrier with anodic valorization of the process. This review summarizes the state of the art and outlooks in this new concept. The electrocatalytic process is briefly introduced, and the main components are discussed. Subsequently, the electrocatalytic production of liquid organic hydrogen carriers and anodic oxidation from components to processes, together with the paired processes and reactors, are analyzed, highlighting challenges and prospects.

Carbon dioxide capture and reduction (CCR) process emerges as an efficient catalytic strategy for CO₂ capture and conversion to valuable chemicals. K-promoted Cu/Al₂O₃ catalysts exhibited promising CO₂ capture efficiency and highly selective conversion to syngas (CO + H₂). The dynamic nature of the Cu-K system at reaction conditions complicates the identification of the catalytically active phase and surface sites. The present work aims at more precise understanding of the roles of the potassium and copper and the contribution of the metal oxide support. While γ-Al₂O₃ guarantees high dispersion and destabilisation of the potassium phase, potassium and copper act synergistically to remove CO₂ from diluted streams and promote fast regeneration of the active phase for CO₂ capture releasing CO while passing H₂. A temperature of 350℃ is found necessary to activate H₂ dissociation and generate the active sites for CO₂ capture. The effects of synthesis parameters on the CCR activity are also described by combination of ex-situ characterisation of the materials and catalytic testing.

Electrochemical ammonia (NH₃) synthesis from nitrate (NO₃⁻) offers a promising greener alternative to the fossil-fuel-based Haber-Bosch process to support the increasing demand for nitrogen fertilizers while removing environmental waste. Previous studies have mainly focused on designing catalysts to promote the direct conversion (NO₃⁻ → NH₃) while suppressing the two-step pathway (NO₃⁻ → NO₂⁻ → NH₃). We hypothesize that efficient nitrate reduction is possible on simple catalysts by instead promoting the two-step reaction and using chemical reactor principles in a membrane electrode assembly, despite NO₂⁻ intermediates. Here, we use an unmodified copper catalyst and control reactivity through current density, flow rate, and electrolyte recycling. Balancing the electrolyte flow rate with current density results in ideal residence times for NO₂⁻, allowing for 91% FE_NH3 in a 5 cm² electrolyzer with a NO₃⁻ to NH₃ partial current of 1.8 A. This work shows that traditional engineering principles can substantially boost the NO₃ reduction reaction, even for simple catalysts.

To introduce promotional H₂O effects for both CH₄ rate and C₂ selectivity, the OH radical formation, catalyzed through H₂O activation with O₂ surface species, was critical for modeling selective Mn-K₂WO₄/SiO₂ catalysts. Based on our reported experimental evidence, which demonstrates the formation of H₂O₂ through surface alkali peroxide intermediate, the elementary reactions that account for the OH-mediated pathway were added into the microkinetic model. The advanced model adeptly replicated the promotional H₂O effects on both OCM rate and selectivity. The data from a low-pressure microkinetic study were treated isothermally, and extended for near-industrially relevant pressures up to 901 kPa. Thermal visualization using an infrared camera found substantial temperature increases at undiluted high-pressure conditions which caused C₂ selectivity to drop significantly. When the furnace temperatures were decreased after ignition, side reactions after O₂ depletion (e.g., hydrocarbon reforming) were suppressed, obtaining 13.7 (11.8) % yields at 19.9 % CH₄ conversion with 68.6 (59.1) % selectivities for C_2-4 (C₂) at 901 kPa. The temperature was found to be the determining factor of C₂ yield which was perturbed by varying space velocity or CH₄/O₂ ratios. The optimum temperature for high-pressure conditions was predicted as 885 °C at 901 kPa. The study provides mechanistic and industrially relevant understandings for further OCM catalyst design and system application.

Operando methodologies are widely used in heterogenous catalysis to understand unique state of catalyst materials emerging under specific reaction conditions and to establish catalyst structure-activity relationships. Recent studies highlight the importance of combining multiple operando techniques (multimodal approach) to gain complementary information as well as looking into chemical and material gradients and spatial variations on the reactor scale. In this work, we developed an operando UV–vis diffuse reflectance spectroscopy (DRS) setup compatible with a common fixed-bed tubular reactor. The design is based on optical calculations, validation experiments and signals considerations. A spatial resolution of 1 mm along the axial direction of the reactor was successfully demonstrated and combined with a time resolution of seconds with good signal to noise. CO oxidation over Pt/Al₂O₃ was performed as a proof of principle experiment demonstrating the capabilities of the new setup. The information gained by the space-resolved operando UV–vis DRS was combined with other space-resolved operando studies such as diffuse reflectance infrared Fourier transform spectroscopy (DRIFTS), gas sampling and temperature profiling. The study shows that the nature of active sites (Pt redox state) and thus the reaction mechanism alter with reaction temperature and also in space. Spatiotemporal UV–vis DRS is also demonstrated, showing the capability for transient studies with space-resolution.

The influence of nanostructures and interaction of Sn and Ir in oxygen evolution catalysts in a polymer electrolyte membrane electrolyzer were investigated. For this aim, two synthesis methods, namely, the one-step solution combustion method and the precipitation-deposition method with sodium borohydride reduction, were evaluated to prepare distinct nanostructures. Sn addition to Ir-based oxygen evolution reaction catalysts has been reported to yield materials with higher activity; however, in our case, this was observed only for Sn/Ir catalysts prepared by the precipitation-deposition method. The nanolayer of Sn/SnO₂ deposited over metallic Ir particles was identified to enhance the interfacial contacts, resulting in synergistic interactions. By deconvolution of the polarization curves into constituting contributions, the performance improvement was attributed to the higher exchange current density of the Sn/Ir powder as a consequence of a higher number of surface reaction sites created by the Sn-Ir interactions.