Assessment of Ni/YSZ anodes prepared by
Transcription
Assessment of Ni/YSZ anodes prepared by
Solid State Ionics 146 (2002) 219 – 224 www.elsevier.com/locate/ssi Assessment of Ni/YSZ anodes prepared by combustion synthesis A. Ringuede´ a, D. Bronine b, J.R. Frade a,* b a Ceramics and Glass Engineering Department (UIMC), University of Aveiro, 3810-193 Aveiro, Portugal Institute of High Temperature Electrochemistry, Ural Division of Russian Academy of Sciences, S. Kovalevskoj 20, 620219 Ekaterinburg, Russia Received 23 August 2001; received in revised form 3 October 2001; accepted 4 October 2001 Abstract Homogeneous mixtures of nanocrystalline powders of (NiO + Ni)/YSZ were obtained by combustion synthesis, and used to prepare Ni/YSZ cermets for symmetrical cermet/YSZ/cermet cells. These cells were prepared by co-pressing, co-firing at 1450 C, and reduction in 10% H2 – 90% N2 at 800 C. The resulting Ni/YSZ cermets are porous and adherent to the electrolyte, and its metallic and ceramic components are uniformly distributed. Impedance spectroscopy was used to characterise these symmetrical cells in atmospheres containing H2 and H2O. The impedance spectra show that the electrode reactions comprise at least two processes with different relaxation frequencies. The low frequency contribution of the polarisation resistance is very dependent on the partial pressures of H2 and H2O. The contribution at higher frequency is mainly dependent on temperature. D 2002 Elsevier Science B.V. All rights reserved. Keywords: Ni; YSZ; Combustion synthesis 1. Introduction The electrode performance of Ni/YSZ cermets is very dependent on microstructural features, and thus processing methods [1,2]. The main factors include the grain size distributions of both components (Ni and YSZ) and the porosity. The microstructures must thus be improved to maximise the triple phase boundary, and the volume fraction of Ni must be sufficient to attain percolation. Koide et al. [9] estimated a typical percolation limit of about 30 vol.% of Ni. The lowest polarisation resistance was found for volume fractions of about 40 –50% Ni, which also suggests the importance of triple contacts. Results reported for alternative Ni/TZP cermets [3– 5] compare to those obtained for Ni/YSZ cermets. The role of triple contacts, and their effects on the mechanism of H2 oxidation have been demonstrated by pattern Ni electrodes deposited onto YSZ [6 –8]. The effective reaction sites appeared to be located in the nickel surface near triple contacts, and from the effects of the partial pressures of hydrogen (pH2) and water vapour ( pH2O) on the current density Misuzaki and coauthors [7] derived the following solution to describe the effects of pH2 and pH2O on the electrode conductivity: rE ¼ di=dE ¼ ½2F=ðRT Þfkkeq pH2 O þ ðk 0 =2Þ ðKeq pH2 Þ1=2 g ð1Þ * Corresponding author. Tel.: +351-234-370254; fax: +351234-425300. E-mail address: jfrade@cv.ua.pt (J.R. Frade). where keq is the equilibrium constant of reaction H2 + 1/2O2 () H2O. 0167-2738/02/$ - see front matter D 2002 Elsevier Science B.V. All rights reserved. PII: S 0 1 6 7 - 2 7 3 8 ( 0 1 ) 0 0 9 9 6 - 1 220 A. Ringuede´ et al. / Solid State Ionics 146 (2002) 219–224 Impedance spectroscopy also reveals that the electrochemical oxidation of H2 in Ni/YSZ cermets or Ni patterns deposited onto YSZ substrates may be complex, usually comprising two or three processes [2,9,10]. For example, Primdahl and Mogensen [2] used an equivalent circuit Rohm(RQ)1(RQ)2(RQ)3 to fit their results at temperatures in the range 850– 1000 C. Typical relaxation frequencies for the electrode contributions were in the ranges of 2 –5 kHz, 30 –100 Hz, and about 1 Hz, respectively. The contribution at highest frequencies is most sensitive to the microstructures and shows the highest temperature dependence. At high temperatures (e.g. 1000 C), the low frequency term may become the highest contribution of the polarisation resistance, at least for optimised cermet anodes [2]. This contribution shows strong dependence on anodic overpotential and on the partial pressures of H2 and/or H2O. The intermediate frequency term remains a minority contribution even for optimised cermets, and was not observed by other authors [10]. The values of polarisation resistance obtained by electrochemical impedance spectroscopy (EIS) may be significantly lower than results obtained by other methods such as galvanostatic current interruption (GCI), as reported by Jiang et al. [4,5,11]. The activation energy is also stronger for the polarisation resistance results obtained with impedance spectroscopy than for results obtained by GCI. However, the differences between the EIS and GCI results decrease with increasing water vapour partial pressure [11]. These findings were thus explained by assuming that extra water vapour is generated by the anodic reaction (in GCI conditions) causing a local increase in its partial pressure, and thus lowering one of the main contributions of the polarisation resistance. Impedance spectroscopy is thus often preferred to study the role of microstructural features and/or gas composition on the oxidation of H2 in Ni-based cermets. Partial oxidation of H2 may thus cause local increase of water vapour partial pressure, yielding some unexpected results obtained for the dependence of electrode conductivity (rE) in the range of low fractions of H2. For example, some results [7,11] indicate an increase in rE with decrease in H2, thus contradicting Eq. (1). Impedance spectroscopy results reported for Ni/TZP cermets show that the low frequency contribution of the polarisation resistance decreases with increasing %H2 whereas other contributions at higher frequency tend to increase [3]. Ni/YSZ cermets often degrade in working conditions, and this has been ascribed to decrease of porosity [1], and/or coarsening of Ni particles [12], causing decrease in electrode conductivity and increase in polarisation. Itoh et al. [1] demonstrated that a fraction of large YSZ particles might prevent coarsening and volume contraction of Ni/YSZ cermets, thus contributing to retain high conductivity and low polarisation. Current collecting might also play a major role on the measured polarisation resistance values, as found on comparing results obtained with collectors made of gold, platinum and nickel pastes [10]. These authors suggested that the degradation of the anode may be due to interdiffusion of the metal in the Ni/YSZ cermet and in the current collector, and suggested that the same metal should be used in the cermet and in the current collector. However, poor contact between the current collect and the cermet may also affect the results, as suggested by the differences between impedance spectra obtained with Ni mesh and Ni paste. The present work reports results obtained for Ni/ YSZ cermet anodes prepared by a combustion synthesis of the cermet powders to ensure a very homogeneous distribution of the metallic and ceramic components. These powders are suitable for co-firing the electrolyte and the cermet anode in a single step. 2. Experimental procedure A combustion synthesis method was used to obtain NiO/YSZ powders, as described elsewhere [13]. Nitrate precursors (ZrO(NO3)26H2O, Y(NO3)36H2O, O, and Ni(NO3)26H2O) were mixed in the required proportions and melted together with urea on a hot plate, and then introduced in a furnace at 600C, where the combustion reaction took place in less than 2 min. The rapid increase of temperature was monitored by inserting a thermocouple in the reacting melt. This short reaction time ensured homogeneity and yielded nanocrystalline mixtures of YSZ, NiO and traces of metallic Ni, as found by X-ray diffraction. Crystallite sizes of about 30– 40 nm were estimated from peak A. Ringuede´ et al. / Solid State Ionics 146 (2002) 219–224 broadening, and also from BET specific surface area (S) measurements, which were used to estimate the average diameter U = 6/(Sq), q being the powder density. The combustion synthesised cermet powders were used to obtain symmetrical cells cermet/YSZ/cermet. A relatively thick YSZ electrolyte pellet was pressed first, and thinner cermet layers were then co-pressed onto both surfaces of the YSZ pellet. These symmetrical cells were co-fired at 1450 C for 90 min, to densify the YSZ electrolyte layer, and to attain good adherence of the cermet layers (Fig. 1). The resulting cermet layers remained porous even at these relatively high firing temperatures. The nickel oxide in the cermet layers was reduced to metallic Ni in 90% N2 + 10% H2, at 800 C, yielding a porous cermet with homogeneous distribution of the metallic and ceramic components, as found by scanning electron microscopy (Fig. 1) and microprobe analysis. The solubility of nickel or nickel oxide in yttria stabilised zirconia is very low both in the as prepared powders and after reduction. The amount of cermet powder was adjusted to obtain porous Ni/YSZ layers with thickness of about 100 mm. The average grain sizes were under 1 mm for both components of the cermet (Ni and YSZ), and the pore size distribution is nearly bimodal with submicron and larger pores. One did not find significant ageing effects in N2 + H2 atmospheres, at temperatures in the range of 681– 900 C, and for up to 3 221 weeks. Fast degradation occurred only after exposition to methane with pH2O = 0.045 atm, due to carbon deposition. The Autolab spectrometer (ECO Chimie) was used to characterise the cermet/YSZ/cermet cells in wet hydrogen or wet N2 + H2 atmospheres, and in the temperature range 681– 884 C. Impedance spectroscopy with a frequency range 10 3 – 104 Hz was sufficient to detect the relevant contributions of the electrode processes. Ni mesh current collectors were used to avoid using different metals in the anode and for current collecting [10]. A YSZ oxygen sensor was used to monitor the oxygen partial pressure, and the values of water vapour partial pressure were adjusted by bubbling gases through water at known temperatures. The nominal water vapour partial pressure was estimated by assuming that equilibrium is attained in these conditions. However, the oxygen partial pressure measurements indicate that the true values of water vapour partial pressure differ from the nominal values. Corrected values of water vapour partial pressure were thus estimated as follows: pH2 O ¼ keq pH2 ðpO2 Þ1=2 ð2Þ where keq is the equilibrium constant of reaction H2 + 1/2O2 () H2O. 3. Results and discussion Fig. 1. SEM microstructures of cermets obtained from combustion synthesised powders. Figs. 2 and 3 show impedance spectra obtained for cermet/YSZ/cermet cells. The ohmic resistance of the electrolyte RYSZ corresponds to a local minimum in the high frequency range, or the intercept of the electrode arc in the upper limit of the frequency range. At relatively low temperatures (Fig. 2), the spectra nearly reduce to a single somewhat depressed electrode and asymmetrical arc, with peak frequency in a typical range of 20 – 50 Hz. However, this peak frequency tends to increase with temperature, and attains values of about 1 kHz at temperatures close to 900 C (Fig. 3), as usually found for the contribution with strongest temperature dependence [2]. In addition, these high temperature spectra show a low frequency process at frequencies in the range of 1– 10 Hz. This low frequency contribution is dependent on 222 A. Ringuede´ et al. / Solid State Ionics 146 (2002) 219–224 Fig. 2. Impedance spectra obtained with symmetrical cermet/YSZ/ cermet cells in H2 at 681 C and with water vapour partial pressure of about 0.045 atm, and at 761 C with water vapour partial pressure of about 0.049 atm. the partial pressures of H2 and water vapour, and is much less dependent on temperature, as reported by other authors [2]. The Nyquist plots of the spectra obtained for the present Ni/YSZ cermet anodes did not show the intermediate frequency contribution reported by Primdhal and Mogensen [2]. Alternative representations of the impedance data [14,15] were thus also used to assess if the spectra included any additional contribution. The modulus representation tends to show the contributions with very small capacitance, as reported in the literature [14], and thus fails to show any relevant additional contribution with much higher capacitance, and thus lower relaxation frequency (Fig. 4). The admittance representation, log(A00) versus log( f ), confirms that typical spectra reduce to two main contributions. Fig. 3. Impedance spectra obtained with symmetrical cermet/YSZ/ cermet cells, at 884 C and for the following conditions: 15% H2, with water vapour partial pressure pH2O = 0.031 atm (circles); 100% H2 with water vapour partial pressure pH2O = 0.043 atm (triangles). Fig. 4. Alternative admittance plots of the results shown in Fig. 3 to demonstrate that the electrode processes reduce to two contributions. The contribution of the polarisation resistance at relatively high frequencies Rmf predominates at relatively low temperatures and conceals the low frequency resistance contribution Rlf. Actually, the deviations from a single arc (Fig. 2) occur mainly in the high frequency side, suggesting an additional contribution, at still higher frequencies. However, this interpretation is debatable and other interpretations may be found for similar deviations in the high frequency (left) side of impedance spectra. Note also that the intermediate frequency contribution found by Primdahl and Mogensen [2] should correspond to deviations in the right side of the Nyquist plots. For symmetrical cells, the overall electrode behaviour comprises contributions of both electrodes, and the polarisation resistance for a single electrode thus reduces to Rp=(R1 + R2)/2, where R1 and R2 represent the two electrode contributions of impedance spectra [10]. The fitting parameters extracted from the impedance spectra were thus used to obtain the moderately high and low frequency terms of a single cermet electrode, Rmf = R1/2 and Rlf = R2/2. Only at the highest temperatures could one obtain results for the low frequency term Rlf with typical values in the range of 0.2 V cm2, except possibly in very dry atmospheres and/or for low partial pressures of H2. The high frequency contribution is the most sensitive to changes in temperature, with an activation energy in the range 1.12– 1.15 eV (Fig. 5), which is significantly higher than the value of 0.8 eV found by Primdahl and A. Ringuede´ et al. / Solid State Ionics 146 (2002) 219–224 Fig. 5. Temperature dependence of the polarisation resistance and its main contribution (in the moderately high frequency range) obtained in H2. Slight changes in water vapour partial pressure occurred and are shown dashed. Mogensen [2]. Jiang and Ramprakash [5] reported similar values for the polarisation resistance of Ni/ TZP cermet anodes obtained by the current interruption method. However, higher values of activation energy were reported for results obtained under low overpotential, and much higher activation energy (1.69 eV) was reported for the polarisation resistance results obtained by impedance spectroscopy. On extrapolating the results obtained for Rmf, and assuming that Rlf remains nearly unchanged, one obtains a prediction for the polarisation resistance of about Rp = 0.2 V cm2 at 1000 C, in atmosphere of H2 with values of water vapour partial pressure in the range of 0.04– 0.05; this is close to the best results reported for optimised cermet microstructures [2], and also much better than reported by other authors [10]. Further improvements might still be attained by lowering the relatively high thickness of our cermets (about 100 mm), and possibly also by optimising other microstructural features. These changes are mainly related to the high frequency (microstructural) contribution of the polarisation resistance. The results obtained for different %H2 at 884 C are shown in Fig. 6. The low frequency term Rlf drops significantly with increasing %H2 but the dependence is stronger than predicted by Eq. (1). These differences may be partly due to the increase in water vapour partial pressure when the %H2 decreases from 100% to about 20% (also shown in Fig. 6). Fig. 7 223 Fig. 6. Dependence of the low and high frequency contributions of the polarisation resistance on the %H2 in H2 + N2 + H2O atmospheres. clearly demonstrates the effects of water vapour content, in agreement with Eq. (1). The main effect is exerted on the low frequency contribution Rlf, as reported in the literature [2,7]. The results in Figs. 6 and 7 also suggest that the moderately high frequency contribution of the polarisation resistance increases slightly with increasing %H2 and decreases with increasing water vapour partial pressure. Similar trends have been reported in the literature, namely references [2] for the effects of water vapour and for the effects of hydrogen [3]. Fig. 7. Values of the low and high frequency contributions of the polarisation resistance obtained for H2 with variable water vapour partial pressure. 224 A. Ringuede´ et al. / Solid State Ionics 146 (2002) 219–224 However, Jiang and Badwal [3] argued that changes in oxygen partial pressure might be the true reason for the changes in Rmf observed on varying the %H2 at constant nominal water vapour content. [2] [3] 4. Conclusions Powders obtained by combustion synthesis are suitable to prepare Ni/YSZ cermet electrodes for symmetrical cells, cermet/YSZ/cermet. These cells can be prepared by co-pressing and co-firing the different layers of these cells. High temperature co-firing did not spoil the microstructure of the cermets, which retain relatively good electrochemical performance in atmospheres containing H2 and H2O. The electrode reactions comprise two main processes. At relatively low temperatures, the overall behaviour is determined by the high frequency contribution of the polarisation resistance. This contribution shows significant temperature dependence with activation energy slightly above 1.1 eV. The low frequency contribution of the polarisation resistance is much less dependent on temperature but is very dependent on the partial pressures of H2 and water vapour. The values of moderately high frequency contribution of the polarisation resistance obtained in the present work are somewhat higher than reported for optimised cermets. This indicates that one must seek further improvements by optimising the cermet microstructures (e.g. by lowering their thickness and/or the firing temperatures). [4] [5] [6] [7] [8] [9] [10] [11] [12] Acknowledgements [13] This work was supported by the EC (project TMRX-CT93-0130). [14] References [15] [1] H. Itoh, T. Yamamoto, M. Mori, T. Horita, N. Sakai, H. 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