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Electrochemical reduction of NOx - DTU Orbit

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1 Introduction<br />

study by Gür et al. 23 , but since these studies were made in the absence <strong>of</strong> oxygen, they were <strong>of</strong><br />

little relevance for <strong>NOx</strong> removal in oxygen containing atmospheres, i.e. at conditions realistic for<br />

exhaust gasses. In a review <strong>of</strong> the application <strong>of</strong> ceramic membranes Cicero et al. reported in 1990<br />

the Helipump Corporation had developed an electrochemical membrane which could remove <strong>NOx</strong><br />

in the presence <strong>of</strong> up to 8% O2 24 . The electrochemical membrane/cell had an yttria stabilized<br />

zirconia electrolyte and transition metal based electrodes, and was reported to remove up to 91%<br />

<strong>NOx</strong> 24 , but unfortunately no further details were given on the experiments conducted and the<br />

electrode materials used. In 1995 Reinhardt et al. performed studies <strong>of</strong> the reaction between O2,<br />

NO and NO2 on LSM electrodes with yttria stabilized zirconia (YSZ) electrolyte and found the O2<br />

exchange reaction on the LSM was very slow below 600 °C, while addition <strong>of</strong> 1000-3000 ppm NO<br />

increased the current densities significantly in oxygen containing atmosphere due to reactions<br />

with NO2 on the electrode surface 25 . Hibino et al. reported in 1994-1995 experiments on <strong>NOx</strong><br />

conversions in oxidizing atmosphere on YSZ based cells with Pd electrodes 26, 27 , and later the<br />

studies were expanded to include Rh, Au, and Pt 28 . The results by Hibino et al. showed Pd was the<br />

best electrode material at 800 °C, and in the presence <strong>of</strong> 1500 ppm NO and 3% O2 15% NO<br />

conversion could be obtained with current efficiency ≈1% 28 . Furthermore it was shown by Hibino<br />

et al. both <strong>NOx</strong> conversion and current efficiency decreased dramatically with increasing O2<br />

content, and the use <strong>of</strong> AC voltage rather than DC voltage would decrease the degradation <strong>of</strong> the<br />

electrochemical cell 28 . Walsh et al. studied the NO <strong>reduction</strong> at a slighter lower temperature range<br />

compared to Hibino et al., namely at 500-600 °C rather than 700-800 °C, and studied Ir and Pt<br />

electrodes on YSZ electrolytes 29, 30 . On the Ir electrodes Walsh et al. demonstrated the selectivity<br />

towards <strong>NOx</strong> <strong>reduction</strong> compared to O2 <strong>reduction</strong> increased with decreasing temperature 29 , while<br />

on the Pt electrodes it was demonstrated the NO conversion increased with NO concentration,<br />

polarisation and temperature 30 . Bredikhin et al. also studied <strong>NOx</strong> conversion in an electrochemical<br />

cell with YSZ electrolyte and Pt electrodes, but in the work by Bredikhin et al. the Pt cathode was<br />

covered by a Ni-YSZ or LSCF(La1-xSrxFe1-yCoyO3)-YSZ electrode layer and a strong dependency <strong>of</strong> the<br />

<strong>NOx</strong> conversion on the microstructure <strong>of</strong> this layer was found 31, 32 . While the studies described so<br />

far all used a precious metal electrode, apart from the work briefly reported by Cicero et al. 24 , the<br />

cylic voltammetry studies made by Hansen et al. in 2000 indicated that transition metal oxides<br />

without addition <strong>of</strong> noble metals could be used for electrochemical <strong>NOx</strong> <strong>reduction</strong>, and especially<br />

LSM15 appeared promising 33-35 . It was also demonstrated by Hansen et al. the redox properties <strong>of</strong><br />

6

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