Herein we report general methods allowing the synthesis of various perfluoroalkylated corannulenes with a specific substitution pattern. Variable temperature NMR spectroscopic investigations revealed dynamic behavior which was analyzed by line shape analysis. The activation parameters of these dynamic processes were determined. For a tetrasubstituted compound it was possible to observe through space scalar coupling. The packing motifs were elucidated by X-ray crystallography, showing that the substitution pattern as well as the size of substituents strongly influence intermolecular π-stacking. The reduction potentials of the perfluoroalkylated compounds were determined by cyclic voltammetry.
Metal-based gas diffusion electrodes are utilized in chlor-alkali electrolysis or electrochemical reduction of carbon dioxide, allowing the reaction to proceed at high current densities. In contrast to planar electrodes and predominantly 2D designs, the industrially required high current densities can be achieved by intense contact between the gas and liquid phase with the catalytically active surfaces. An essential asset for the knowledge-based design of tailored electrodes is therefore in-depth information on electrolyte distribution and intrusion into the electrode's porous structure. Lab-based and synchrotron radiography allow for monitoring this process operando. Herein, we describe the development of a cell design that can be modularly adapted and successfully used to monitor both the oxygen reduction reaction and the electrochemical reduction of CO2 as exemplary and currently very relevant examples of gas-liquid reactions by only minor modifications to the cell set-up. With the reported cell design, we were able to observe the electrolyte distribution within the gas diffusion electrode during cell operation in realistic conditions.
One of the challenges of high-temperature polymer electrolyte
membrane
fuel cells is the poisoning of the Pt catalyst with H3PO4. H3PO4 is imbibed into the routinely
used polybenzimidazole-based membranes, which facilitate proton conductivity
in the temperature range of 120–200 °C. However, when
leached out of the membrane by water produced during operation, H3PO4 adsorbs on the Pt catalyst surface, blocking
the active sites and hindering the oxygen reduction reaction (ORR).
The reduction of H3PO4 to H3PO3, which occurs at the anode due to a combination of a low
potential and the presence of gaseous H2, has been investigated
as an additional important contributing factor to the observed poisoning
effect. H3PO3 has an affinity toward adsorption
on Pt surfaces even greater than that of H2PO4
–. In this work, we investigated the poisoning
effect of both H3PO3 and H3PO4 using a half-cell setup with a gas diffusion electrode under
ambient conditions. By means of in situ X-ray absorption spectroscopy,
it was possible to follow the signature of different species adsorbed
on the Pt nanoparticle catalyst (H, O, H2PO4
–, and H3PO3) at different
potentials under ORR conditions in various electrolytes (HClO4, H3PO4, and H3PO3). It was found that H3PO3 adsorbs in a pyramidal
configuration P(OH)3 through a Pt–P bond. The competition
between H3PO4 and H3PO3 adsorption was studied, which should allow for a better understanding
of the catalyst poisoning mechanism and thus assist in the development
of strategies to mitigate this phenomenon in the future by minimizing
H3PO3 generation by, for example, improved catalyst
design or adapted operation conditions or changes in the electrolyte
composition.
The modularity of molecular catalysts enables the tuning of both active site and peripheral units to maximize functionality, thus rendering them as ideal model systems to explore fundamental concepts in catalysis. Hydrophobicity is often regarded as an undesirable aspect that hinders their dissolution in aqueous electrolytes. In contrast, we modified established Co terpyridine catalysts with hydrophobic perfluorinated alkyl side chains and took advantage of their hydrophobic character by utilizing them not as dissolved species in an aqueous electrolyte but at the gas-liquid-solid interfaces on a gas diffusion electrode (GDE) applied towards the electrochemical reduction of CO2. We found that the self-assembly of these perfluorinated units on the GDE surface results in a catalytic system selective for CH4 production, whereas every other Co terpyridine catalyst reported before was only selective for CO or formate. An array of mechanistic and operando spectroscopic investigations suggests a mechanism in which the pyridine units function as proton shuttles that deliver protons to the dynamic hydrophobic pocket in which CO2 reduction takes place. Finally, optimizing the system by integrating fluorinated carbon nanotubes as a hydrophobic conductive scaffold leads to a Faradaic efficiency for CH4 production above 80% at rates above 10 mA/cm2, thus far unprecedented for a molecular electrocatalytic system.
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