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Electrolysis of CO2 and H2O

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Electrolysis of CO2 and H2O ( electrolysis-co2-and-h2o )

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Chapter 5. Aspects of Metal-YSZ Electrode Kinetics 110 That is, halving the internal resistance of the cell leads to approximately the same capital cost reduction as doubling the durability. With low enough resistance (high enough throughput), electrolysis using solid oxide cells could be economical with only a short (perhaps 1 year) operating life. A better understanding of metal-YSZ electrode kinetics (oxidation and reduction of H2/H2O and CO/CO2 at metal-YSZ interfaces) could reveal pathways to significantly improving the performance and durability of solid oxide cells. In this chapter the electrochemistry at the metal-YSZ (electrode-electrolyte) interface is studied in detail. Geometrically simplified ―model‖ metal wire electrodes pressed down upon polished YSZ pellet electrolytes were employed. This point-contact cell geometry is intended to serve as an ideal ―model‖ electrode that represents a single interface of the thousands of ceramic and metal particles that make up the typical three-dimensional composite electrode of a technological solid oxide cell, to isolate the true nature of the electrochemistry (catalytic and electrochemical processes) from the additional properties that arise from a complex three-dimensional microstructure (gas transport and current distribution in porous structures, and heterogeneous interfaces and particle sizes). It also provides a well-defined three-phase boundary (TPB) at the interface. In the present study, the test conditions – the gas composition, the temperature, and the polarization of the electrodes – were varied systematically to examine how the electrochemical measurements varied, to facilitate studying the electrode rate-limiting processes. A number of workers have studied H2 oxidation at Ni/YSZ by performing electrochemical impedance spectroscopy and/or polarization sweeps at systematically-varied conditions. This study is unique in the application of test conditions relevant to steam and CO2 electrolysis (e.g. high partial pressures of H2O and CO2 and cathodic polarizations) to point-electrode characterization. In fact, gas atmospheres with high pH2O and pCO2 like 50% H2 + 50% H2O and 50% CO + 50% CO2 should be included in fuel cell tests as well because they are relevant to cell operation – with high reactant conversion during either electrolysis or fuel cell operation, the negative-electrode should on average be in a gas atmosphere of something close to 50% fuel + 50% oxidized products (with more fuel near the inlet and more oxidized products near the outlet). Despite all the work that has been done (reviewed in the next section), the detailed kinetics of the electrode reactions are not well known [1, 2]. Little work has been done comparing the same reactions using different metals, even though this may be a good way to examine the kinetics of reactions occurring at the metal/YSZ interface. Therefore, an additional parameter, which is uncommon in most studies, was the variation of the metal material itself – by comparing the same reactions using different metals (Ag, Au, Cu, Ni, Pd, and Pt) under identical conditions, the similarities and differences of the electrochemical responses between

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