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Efficient NiFe-Layered Double Hydroxide Electrocatalyst Synthesized via a Solvent-Free Mechanochemical Method for Oxygen Evolution Reaction


Manuel Molina-Muriel, Sabrina Campagna Zignani, Sara Goberna-Ferrón, Antonio Ribera, Antonino Salvatore Aricò, Hermenegildo García

Available at: https://pubs.acs.org/doi/10.1021/acsomega.4c11115

Abstract

The growing concern over climate change and the reliance on fossil fuels has spurred interest in alternative energy processes, particularly electrochemical water splitting to produce hydrogen (H2). This study focuses on developing cost-effective and efficient oxygen evolution reaction (OER) electrocatalysts. We report a novel solvent-free mechanochemical method for synthesizing NiFe-layered double hydroxide (LDH), which demonstrates promising electrocatalytic properties for the OER. The mechanochemical synthesis, requiring only 1 h of solid reagent grinding, produces NiFe-LDH with structural features comparable to those obtained via traditional aqueous phase methods. The electrocatalyst was evaluated in a single cell with a membrane-electrode assembly configuration under alkaline conditions, exhibiting an overpotential of 221 mV at a current density of 10 mA·cm–2 and a Tafel slope of 103.1 mV·dec–1, indicating excellent OER kinetics and low energy barriers. Additionally, the catalyst demonstrated robust durability, maintaining a potential of around 1.55 V during a 35 h test at high current densities of 0.1 A·cm–2 and even 1.75 V at 1 A·cm–2. This work highlights the potential of NiFe-LDH synthesized by an energy-efficient, environmentally green, and scalable process for large industrial water-splitting applications, contributing to the advancement of sustainable hydrogen production technologies.

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Anion exchange membrane co-electrolysis of CO2 and water using CuOx nanoparticles-based gas diffusion electrode for the conversion of carbon dioxide into carbonaceous fuels

Sabrina Campagna Zignani, Alessandra Carbone, Vitaliano Chiodo, Susanna Maisano, Mariarosaria Pascale, Marta Fazio, Luca Riillo, Anna Ramunni, Charly Azra, Ervin Tal Gutelmacher, Antonino Salvatore Aricò

Available at https://doi.org/10.1016/j.cej.2025.163798

Abstract

Low temperature CO2 − water co-electrolysis was studied in a zero-gap cell based on an anion exchange membrane to produce synthetic fuels at suitable energy efficiency and current density thanks to a proper combination of specific materials, cell configuration and operating conditions. The electrochemical cell consisted of gas-diffusion electrodes containing non-precious electrocatalysts such as nanosized particles-based copper oxide for the cathode and Ni-Fe oxide-hydroxide for the anode. The stability of these electrocatalysts was favoured by a high internal operating pH assured through the recirculation of KOH at the anode. The CO2 stream was humidified at the operating cell temperature or higher before being fed to the cathode. The process was studied in terms of outlet stream composition, electrochemical performance, faradaic and voltage efficiency through galvanostatic operation at practical current densities, e.g. 0.3 A cm−2, combined to gas chromatographic analysis. Electrochemical diagnostics, such as polarization curves and ac-impedance spectroscopy combined to productivity data, allowed to derive an interpretation of the cell behaviour under different operating conditions revealing a paramount effect of the ionomer dispersion, added to the cathode, and the operating current density. A useful strategy was adopted to mitigate the precipitation of carbonates. Promising results were observed in terms of production of ethylene and syngas at suitable voltage and faradaic efficiencies. A possible reaction mechanism for the CO2 reduction under alkaline conditions was considered in relation to the formed products.

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Electrochemical CO2 Reduction: Commercial Innovations and Prospects

Swapnil VarhadeAvni GurujiChandani SinghGiancarlo CiceroMax García-MelchorJoost HelsenDeepak Pant

First published: 12 December 2024

Available at https://doi.org/10.1002/celc.202400512

Abstract

Sustainability is an imperative requirement in this era, with electrocatalytic power into fuels technologies emerging as a significant route toward sustainable chemistry. One of the focus areas within the chemical industry is capture of carbon dioxide (CO2) and its electrochemical reduction (eCO2RR) into economically viable commodities through the utilization of renewable sources. Despite some specific eCO2RR technologies being poised for market introduction, the development of a comprehensive technology for eCO2RR remains a challenge. While certain technologies targeting specific eCO2RR products are on the verge of deployment, substantial efforts are still necessary to transition and establish presence in the market over conventional technologies. This review highlights recent technological advancements, fundamental studies, and the persisting challenges from an industrial perspective. We take a deep dive into the research methodologies, strategies, challenges, and advancements in the development of applications for eCO2RR. Specifically, three eCO2RR products – CO, HCOOH, and C2H4 – as promising candidates for implementation are elaborated based on techno-economic considerations. Additionally, the review discusses the industrial blueprint for these products, aiming to streamline their path toward commercialization. The intent is to present the status of eCO2RR, offering insights into its potential transformation from a mere laboratory curiosity to a feasible technology for industrial chemical synthesis.

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Physicochemical properties of short-side-chain perfluorosulfonic acid membranes at elevated temperatures

Harilal, Yi-Lin Kao, Chao Pan, David Aili, Qingfeng Li
Available at: https://doi.org/10.1016/j.ssi.2024.116747

Abstract

Water and CO2 electrolysis at elevated temperatures in cells equipped with short-side-chain perfluorosulfonic acid membranes could potentially allow for new approaches to tuning catalyst kinetics and selectivity, but the membrane characteristics under such conditions remains to be described. In this work, a short-side-chain perfluorosulfonic acid membrane (Aquivion) is characterized at temperatures up to 150 °C and high humidification levels with respect to tensile behavior, ionic conductivity, permeability of hydrogen and methanol, and stability. The membrane is found to retain mechanical robustness at temperatures up to at least 130 °C while dehydration at temperatures above 100 °C under ambient pressure results in a significant conductivity decay. The densification of the membrane matrix at temperatures above the boiling point of water under varied pressures leads to reduced hydrogen and methanol permeability. Pressurization up to 5 bars effectively mitigates the conductivity decay due to the presence of liquid water but also results in increased permeability. The membrane stability test, as characterized by hydrogen crossover measurements, shows that humidification is a harsher stressor than temperature in the studied range.

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Closing the Carbon Cycle – Demonstrating Back-Up Power Production from E-Fuels in Gensets and Recycling of the Engine Exhaust Gas

Moser, Peter and Stahl, Knut and Wiechers, Georg, Closing the Carbon Cycle – Demonstrating Back-Up Power Production from E-Fuels in Gensets and Recycling of the Engine Exhaust Gas (September 26, 2024). Available at SSRN: https://ssrn.com/abstract=5016150 or http://dx.doi.org/10.2139/ssrn.5016150

Abstract

For the first time the concept of back-up power production by combustion of a fuel blend using e-Fuels in a stationary engine (electric output 200 kW) and feeding back the exhaust gas of the engine upstream of an amine-based CO2 capture plant (capture capacity 7.2 t/day CO2 at a capture rate of 90%) was demonstrated at RWE’s Innovation Center at Niederaussem, Germany. The captured CO2 will be later the feedstock for the large 1 MW ECO2Fuel demonstrator to produce carbonaceous e-Fuels, which can again be used in the engine genset, closing the carbon loop. As the exhaust gas has an attractive high temperature level of >400°C that is typically for combined heat and power applications also the potential of the heat reuse and efficiency enhancement was investigated. The analysis and evaluation comprised especially the effect of the changes in the flue gas composition by the exhaust gas recycling (increased O2 and reduced CO2 concentration) on the capture plant performance (specific heat demand for the solvent regeneration, emissions; solvent CESAR1) and the potential of the set-up for combined heat and power applications.

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Advancing Renewable Energy: CO₂ Conversion to Synthetic Fuels

Researchers Sabrina C. Zignani and Antonino S. Aricò have made significant strides in the field of renewable energy with their latest study on CO₂ conversion to synthetic fuels. Utilizing a flow cell reactor with copper and silver-based cathodes, they demonstrate improved selectivity and efficiency in converting carbon dioxide into valuable chemicals, including ethylene, ethanol, and propanol. This innovative approach holds promise for sustainable fuel production, contributing to efforts in reducing atmospheric CO₂ and combating climate change. 

Abstract

As a result of electrochemical conversion of carbon dioxide (CO2), value-added chemicals like as synthetic fuels and chemical feedstocks can be produced. In the current state of the art, copper-based materials are most widely used being the most effective catalysts for this reaction. It is still necessary to improve the reaction rate and product selectivity of CuOx for electrochemical CO2 reduction reaction (CO2RR). The main objective of this work was synthesized and evaluate the copper oxide electrocatalyst combined with silver (CuO 70% Ag 30%) for the conversion of carbon dioxide into synthetic fuels. The catalysts have been prepared by the oxalate method and assessed in a flow cell system. The results of electrochemical experiments were carried out at room temperature and at different potentials (-1.05 V–0.75 V vs. RHE in presence of 0.1 M KHCO3) and gas and liquid chromatographic analysis are summarized. The CuOx-based electrodes demonstrated the selective of ~ 25% at -0.55 V for formic acid (HCOOH) and over CuO -Ag and selective of ethylene at ~ 20% over CuOx at -1.05 V. Other products were formed as ethylene, ethanol, and propanol (C2H4, EtOH, PrOH) at more positive potentials. On the other hand, carbon monoxide, acetate, ethylene glycol, propinaldehyde, glycoaldehyde and glyoxal (CO, CH3COO, C2H6O2, C3H6O, C2H4O2, C2H2O2) have been formed and detected. Based on the results of these studies, it appears that the formation of synthetic fuels from CO2 at room temperature in alkaline environment can be very promising.

For more detailed insights, read the full study here.

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Alkaline electrolysis using CuOx cathode for the conversion of carbon dioxide into liquid fuels

Abstract

Electrochemical reduction of CO2 is an effective method for storing intermittent renewable energy. This could result in fuel additives and chemical feedstocks such as alcohols. A challenge of electrochemical alcohol production is the transfer of electrons and protons, as well as the formation of C–C bonds. As of now, copper-based materials are the most commonly used and effective catalysts. Although CuOx is considered a promising catalyst for electrochemical CO2 reduction reactions (CO2RR), significant improvements in product selectivity are still needed. This paper presents some results obtained using copper oxide as a cathode, combined with 33% of ionomer, nickel iron as anode, and membrane Fumatech as electrolyte. As a result of physico-chemical experiments, morphological measurements of the cathode, electrochemical experiments carried out with a complete zero-gap cell operating under alkaline conditions, and gas-chromatographic (GC) analyses of the cathode outlet stream, we determined that methyl formate, ethanol, and propanol were mainly obtained at a rate of 116.3 μmol gcat−1h−1 during operation at 2.2 V.

Zignani, S.C., Lo Faro, M., Carbone, A. et al. Alkaline electrolysis using CuOx cathode for the conversion of carbon dioxide into liquid fuels. Mater Renew Sustain Energy 12, 141–146 (2023). https://doi.org/10.1007/s40243-023-00235-6