Abstract

Redox studies on dense zirconia-doped ceria pellets were carried out by thermogravimetric investigations and dilatometry. Up to 1600 K reduction parameters determined by both methods correspond to each other. At higher temperatures, however, thermogravimetry overestimates the degree of reduction since mass loss is not only due to oxygen exsolution but also to selective evaporation of CeO2 whose vapour pressure is considerably higher than that of ZrO2. As a consequence surface segregation of zirconia occurs in (Ce,Zr)O2−δ pellets leading to a porous surface zone of Ce2Zr2O7 pyrochlore which gradually grows in thickness. Surface enrichment of zirconia is detrimental for splitting CO2 or H2O since re-oxidation temperatures of (Ce,Zr)O2−δ are known to be shifted towards lower temperatures with increasing ZrO2 content. Thus, very harsh reduction conditions should be avoided for the (Ce,Zr)O2−δ redox system. The kinetics investigations comprised the high temperature reduction step (T ≅ 1600 K) and the “low” temperature oxidation reaction with a carbon dioxide atmosphere (T ≅ 1000 K). The reduction kinetics (at around 1600 K and an oxygen activity of 7 × 10−4 in the gas phase) directly yield the (reduction) equilibrium exchange rate of oxygen in the order of 10−7 mol·O/(cm3·s) as the kinetics are surface controlled. The oxidation step at around 1000 K, however, occurs in the mixed control or in the diffusion control regime, respectively. From oxygen isotope exchange in combination with SIMS depth profiling oxygen exchange coefficients, K, and oxygen diffusivities, D, were determined for so-called equilibrium experiments as well as for non-equilibrium measurements. From the obtained values for K and D the (oxidation) equilibrium exchange rates for differently doped ceria samples were determined. Their dependency on the oxygen activity and the nature and the concentrations of a tetravalent dopant (Zr) and trivalent dopants (La, Y, Sm) could be semi-quantitatively rationalised on the basis of a master equation for the equilibrium surface exchange rate.

Highlights

  • Renewable energy technologies are crucial in view of global warming and limited fossil fuel resources

  • Redox studies on zirconia-doped ceria revealed selective sublimation of ceria from ceria–zirconia solid solutions when reduction temperatures are above 1600 K and gas pressures were low

  • Surface enrichment of zirconia is detrimental for splitting CO2 or H2 O since re-oxidation temperatures of (Ce,Zr)O2 − δ are known to be shifted towards lower temperatures with increasing ZrO2 content

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Summary

Introduction

Renewable energy technologies are crucial in view of global warming and limited fossil fuel resources. Virtually no nucleation barriers exist and only minor volume changes occur during the reduction/oxidation cycle From these reasons CeO2 -based redox materials are promising for reactive ceramic bodies (beads, foams, honeycomb structures). Redox kinetics of ceria-based materials is either controlled by surface exchange reactions or by bulk transport of oxygen. Conductivity relaxation studies which yielded only surface exchange coefficients but no diffusion coefficients (see, e.g., [36]) In this joint publication we will not review the literature on ceria in its entirety, but firstly we present some very recent findings on degradation via selective sublimation of ceria occurring in. An application of our phenomenological treatment of oxygen exchange kinetics is given as well as a first comparative study of oxygen exchange from an O2 atmosphere and from a CO2 atmosphere, respectively

Sample Preparation
O7 gradually δ parent
Revision of the Standard Picture of the Oxygen Exchange Kinetics
Reduction two un-doped
Oxygen Exchange from O2 Atmospheres
10. Schematic
12. Oxygen
Atmospheres
13. Visualization
Samples
14. During annealingO18will
15. Ionimage image for 16
Comparison of the Oxygen
17. Graphical
Conclusions
Schematic
Findings
Graphical
Full Text
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