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  • 1
    In: Electrochimica Acta, Elsevier BV, Vol. 401 ( 2022-01), p. 139494-
    Materialart: Online-Ressource
    ISSN: 0013-4686
    Sprache: Englisch
    Verlag: Elsevier BV
    Publikationsdatum: 2022
    ZDB Id: 1483548-4
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  • 2
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    The Electrochemical Society ; 2018
    In:  Journal of The Electrochemical Society Vol. 165, No. 7 ( 2018), p. A1288-A1296
    In: Journal of The Electrochemical Society, The Electrochemical Society, Vol. 165, No. 7 ( 2018), p. A1288-A1296
    Materialart: Online-Ressource
    ISSN: 0013-4651 , 1945-7111
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    Sprache: Englisch
    Verlag: The Electrochemical Society
    Publikationsdatum: 2018
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  • 3
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    Royal Society of Chemistry (RSC) ; 2016
    In:  Journal of Materials Chemistry A Vol. 4, No. 47 ( 2016), p. 18300-18305
    In: Journal of Materials Chemistry A, Royal Society of Chemistry (RSC), Vol. 4, No. 47 ( 2016), p. 18300-18305
    Materialart: Online-Ressource
    ISSN: 2050-7488 , 2050-7496
    Sprache: Englisch
    Verlag: Royal Society of Chemistry (RSC)
    Publikationsdatum: 2016
    ZDB Id: 2702232-8
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  • 4
    In: ECS Meeting Abstracts, The Electrochemical Society, Vol. MA2020-02, No. 38 ( 2020-11-23), p. 2454-2454
    Kurzfassung: Proton exchange membrane (PEM) based water electrolyzers are a promising technology for the large-scale production of hydrogen from renewable energy. The most efficient and durable catalysts for PEM water electrolysis are platinum to catalyze the hydrogen evolution reaction (HER) and iridium oxide to catalyze the oxygen evolution reaction (OER). While the currently rather high noble metal loadings (≈0.3-0.5 mg Pt /cm 2 and ≈1-3 mg Ir /cm 2 ) have only a minor impact on the overall water electrolyzer system cost [1], the large-scale global implementation of PEM water electrolysis would require a substantial reduction of the noble metal loadings due to the limited availability of Pt and Ir. This is easy to achieve for the Pt cathode catalyst, owing to its fast HER kinetics and the fact that a high dispersion of Pt is readily achieved with carbon-supported Pt (Pt/C). However, lowering the Ir loading below ≈0.5 mg Ir /cm 2 is not possible with currently available Ir catalysts (Ir black, nano-IrO 2 , or IrO 2 supported on a TiO 2 substrate), as it results in too thin, non-contiguous electrode layers with poor in-plane conductivity, owing to their low iridium packing density of ≈2.3 g Ir /cm 3 electrode (this is in contrast to ≈0.05-0.10 g Pt /cm 3 electrode for a typical Pt/C catalyst) [2]. Thus, to reach the long-term target of an Ir-specific power density of ≤0.01 g Ir /kW [2], novel catalysts with a lower iridium packing density are required, which could be achieved, e.g., by supporting iridium or iridium oxide nanoparticles on conductive supports or by other approaches [3] . A detailed analysis leading to this conclusion will be discussed in this presentation. The development and implementation of such novel catalysts also requires the evaluation of their long-term stability. Conventionally, this is either done by measurements in liquid electrolyte, typically using the rotating disk electrode (RDE) technique, or testing in an actual PEM electrolyzer. Unfortunately, recent studies revealed that the RDE based approach does not yield reliable catalyst durability data, since for yet unknown reasons, the catalyst life-times obtained by the RDE method are three to four orders of magnitude lower than what is observed in PEM electrolyzers [3, 4]. On the other hand, catalyst durability testing in a PEM electrolyzer requires very long measurement times, so that accelerated durability test protocols are necessary [5] . These aspects will also be discussed. References: [1] K. E. Ayers, N. Danilovic, R. Ouimet, M. Carmo, B. Pivovar, M. Bornstein; Annual Review of Chemical and Biomolecular Engineering 10 (2019) 219. [2] M. Bernt, A. Siebel, H. A. Gasteiger; J. Electrochem. Soc. 165 (2018) F305. [3] M. Bernt, A. Weiß, M. F. Tovini, H. El-Sayed, C. Schramm, J. Schröter, C. Gebauer, H. A. Gasteiger; Chem. Ing. Tech 92 (2020); https://doi.org/10.1002/cite.201900101. [4] H. A. El-Sayed, A. Weiß, L. F. Olbrich, G. P. Putro, H. A. Gasteiger; J. Electrochem. Soc. 166 (2019) F458. [5] A. Weiß, A. Siebel, M. Bernt, T. H. Shen, V. Tileli, H. A. Gasteiger; J. Electrochem. Soc. 166 (2019) F487.
    Materialart: Online-Ressource
    ISSN: 2151-2043
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    Verlag: The Electrochemical Society
    Publikationsdatum: 2020
    ZDB Id: 2438749-6
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  • 5
    In: ECS Meeting Abstracts, The Electrochemical Society, Vol. MA2018-02, No. 4 ( 2018-07-23), p. 179-179
    Kurzfassung: High energy Li-Ion batteries rely on the pairing of a transition metal oxide cathode with a graphite anode. Pushing the upper cut-off voltage and state of charge (SOC) to higher values, the cycle-life of the battery is drastically reduced. Besides electrochemical electrolyte oxidation leading to poor coulombic efficiencies and a large growth of cell impedance, leaching of transition metal ions from the cathode active materials is one of the major obstacles to increase the power density of the cell without change of active materials. While the capacity loss which can be ascribed to the overall loss of active material is minor, cell aging is largely aggravated by liberated transition metal ions present in the electrolyte, as they diffuse through the separator and deposit on the graphite anode due to its low potential. A severe impedance growth of the anode and loss of active lithium by chemical delithiation of the graphite has been observed by many studies. Especially for manganese, the amount of active lithium loss has been found to be a multifold higher than the total amount of manganese ions present in the electrolyte and deposited onto the graphite anode, indicating a catalytic role of transition metal ions on active lithium loss (1). Comparisons of the transition metal leaching behavior for different cathode active materials is missing so far, as studies vary widely in test procedures (potential range, SOC) and environment (electrolyte and temperature). We herein present operando analysis of the intrinsic stability of several cathode active materials upon charge to high SOC and potential with our unique spectroscopic cell enabling spatially resolved operando X-ray absorption spectroscopy, monitoring the concentration and oxidation state of transition metals in the electrolyte and in the graphite anode (2, 3). Aside layered mixed transition metal oxide materials (Li 1+w [Ni x Co y Mn z ] 1-x O 2 ) also the spinel structure is tested to better understand the effect of crystal destabilization at high SOC. The formerly standard layered oxide NCM111 (x=y=z=0.33) was already studied earlier, focusing on manganese dissolution (3). In this talk we present time and potential resolved analysis of all transition metals released from NCM111 (see Fig. 1) in comparison to a nickel-rich NCM811 (x=0.8, y=z=0.1), a lithium- and manganese-rich layered oxide material (HE-NCM; w=0.17, x=0.22, y=0.12, z=0.66 (4)) and the high-voltage spinel LiNi 0.5 Mn 1.5 O 4 , (LNMO). This data allows conclusions on the extent of the two major causes for transition metal leaching from oxide based cathode materials: chemical decomposition induced by protic electrochemical electrolyte oxidation products (5) and crystal lattice destabilization of layered transition metal oxides caused by high degrees of delithiation (high SOC). References J. A. Gilbert, I. A. Shkrob and D. P. Abraham, Journal of The Electrochemical Society , 164 , A389 (2017). Y. Gorlin, A. Siebel, M. Piana, T. Huthwelker, H. Jha, G. Monsch, F. Kraus, H. A. Gasteiger and M. Tromp, Journal of the Electrochemical Society , 162 , A1146 (2015). J. Wandt, A. Freiberg, R. Thomas, Y. Gorlin, A. Siebel, R. Jung, H. A. Gasteiger and M. Tromp, J. Mater. Chem. A , 4 , 18300 (2016). B. Strehle, K. Kleiner, R. Jung, F. Chesneau, M. Mendez, H. A. Gasteiger and M. Piana, Journal of The Electrochemical Society , 164 , A400 (2017). M. Metzger, B. Strehle, S. Solchenbach and H. A. Gasteiger, Journal of The Electrochemical Society , 163 , A798 (2016). Acknowledgements Financial support for S. S. and B. S. by the BASF SE through its Research Network on Electrochemistry and Batteries is gratefully acknowledged. XAS data were gathered at the European Synchrotron Radiation Facility (ESRF) and SOLEIL Synchrotron (France).We are grateful to Dr. Debora Motta Meira at the ESRF, Grenoble (France) for providing assistance in using beamline BM 23 as well as Dr. Emiliano Fonda for assistance on the SAMBA beamline at SOLEIL Synchrotron. Fig. 1: Transition metal dissolution of an NCM111 (5.5 mAh/cm 2 )//C 6 cell upon cycling in the conventional potential range (0-6.5 h: 60% SOC until ≈4.2 V Li ) and upon high degrees of delithiation (7-11 h: ≈100% SOC until 5.1 V Li ) measured in our operando XAS cell using glass fiber separators and standard LP57 electrolyte (1 M LiPF 6 in EC:EMC [3:7]) at 25 °C. The concentration of transition metal ions within the graphite electrode (filled symbols) and in the electrolyte (hollow stars, shown as electrolyte share in the graphite pores [concentration measured in the separator multiplied by the porosity of the graphite anode] ) is monitored operando. Figure 1
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    ISSN: 2151-2043
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    Verlag: The Electrochemical Society
    Publikationsdatum: 2018
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  • 6
    In: ECS Transactions, The Electrochemical Society, Vol. 64, No. 3 ( 2014-08-18), p. 1069-1080
    Kurzfassung: In this study, we provide an overview regarding our recent finding on the mechanism, activity and particle size effect for the hydrogen oxidation and evolution reaction (HOR/HER) on Pt-group metal electrodes, under both acid and alkaline conditions. We show that there is an activity decrease of about two orders of magnitude when going from acid to base conditions on electrodes which are able to form a H-UPD layer like Pt, Ir, Pd and Rh. Similarities in the HOR/HER process between acid and base conditions have been found: the rate determining step, which has been identified by means of electrochemical impedance spectroscopy measurements to be the Volmer reaction, remains the same and there is no particle size dependency on the reactivity of Pt electrodes. In the light of these finding, Volcano plots of the HOR/HER activities in acid and base have been proposed.
    Materialart: Online-Ressource
    ISSN: 1938-5862 , 1938-6737
    Sprache: Unbekannt
    Verlag: The Electrochemical Society
    Publikationsdatum: 2014
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  • 7
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    Springer Science and Business Media LLC ; 2017
    In:  MRS Advances Vol. 2, No. 8 ( 2017-02), p. 439-444
    In: MRS Advances, Springer Science and Business Media LLC, Vol. 2, No. 8 ( 2017-02), p. 439-444
    Materialart: Online-Ressource
    ISSN: 2059-8521
    Sprache: Englisch
    Verlag: Springer Science and Business Media LLC
    Publikationsdatum: 2017
    ZDB Id: 2858562-8
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  • 8
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    The Electrochemical Society ; 2017
    In:  ECS Meeting Abstracts Vol. MA2017-02, No. 37 ( 2017-09-01), p. 1648-1648
    In: ECS Meeting Abstracts, The Electrochemical Society, Vol. MA2017-02, No. 37 ( 2017-09-01), p. 1648-1648
    Kurzfassung: Proton exchange membrane water electrolysis (PEM-WE) is a suitable technology for producing hydrogen via electricity generated from renewable but fluctuating energy sources, such as wind or solar energy. Due to their modest activity but sufficiently high stability in the acidic environment of a PEM system, iridium oxides (IrO x ) are the most commonly used catalysts for the oxygen evolution reaction (OER). 1 However, recent studies revealed a strong correlation between the OER activity and the stability of IrO x depending on its surface morphology and hydration state (i.e., between highly crystalline thermal IrO 2 and amorphous, hydrous oxides). Bulk IrO 2 provides the best compromise regarding long lifetime requirements, since its OER activity decreases with inreaseing IrO x crystallinity, whereas its stability improves 2,3 . Recent studies from our lab revealed that IrO x can easily be reduced to metallic iridium (Ir) when IrO x based membrane electrode assemblies (MEAs) are held at open circuit voltage (OCV) in a PEM-WE, where crossover H 2 from the cathode side reduces the surface of the IrO x catalyst at the anode. This reduction step is indicated by the formation of H-UPD features in the recorded cyclic voltammograms (CVs). Interestingly, the polarization curve recorded directly after this reduction shifts towards lower cell voltages, corresponding to an improved OER activity ( Figure 1 ). Moreover, in a subsequent CV (recorded after the latter polarization curve), the H-UPD features disappeared while the characteristic oxide formation and reduction peaks evolved, pointing towards a change of the catalyst surface properties to a state closer to less crystalline, hydrous IrO x . Considering the fact, that hydrous IrO x exhibits less stability 4 and that this partial IrO x reduction and re-oxidation can occur during cycles of extended OCV periods, these findings must be considered as potential degradation mechanism in PEM-WE operation. During the lifetime of an electrolyzer, especially if coupled with a fluctuating power supply, operation interruptions can be expected to occur frequently, thereby altering the form of the IrO x . Therefore, we apply an accelerated test protocol cycling between operation and OCV periods to investigate this degradation mechanism further as well as the effect of potential mitigation strategies. Acknowledgements : This work was funded by the Bavarian Ministry of Economic Affairs and Media, Energy and Technology through the project ZAE-ST (storage technologies) and by the German Ministry of Education and Research (funding number 03SFK2V0, Kopernikus-project P2X). References   (1) C. Rozain, E. Mayousse, N. Guillet and P. Millet, Appl. Catal. B , 182 , 123 (2016) (2) T. Reier, D. Teschner, T. Lunkenbein, A. Bergmann, S. Selve, R. Kraehnert, R. Schlögl, and P. Strasser, J. Electrochem. Soc. , 161 , F876 (2014). (3) S. Cherevko, T. Reier, A. R. Zeradjanin, Z. Pawolek, P. Strasser, and K. J. J. Mayrhofer, Electrochem. Commun. , 48 , 81 (2014). (4) S. Geiger, O. Kasian, B. R. Shrestha, A. M. Mingers, K. J. J. Mayrhofer and S. Cherevko, J. Electrochem. Soc. , 163 , F3132–F3138 (2016) Figure 1 Polarization curves (A) at initial state (black) and after the reduction step (blue); IV plots were recorded galvanostatically at 80 °C and ambient pressure on a MEA (Nafion 212) with 5 cm² active area, fed with 5 mLmin -1 liquid H 2 O to the anode. HFR values estimated from impedance spectra recorded during the IV plots are displayed in (B). Figure 1
    Materialart: Online-Ressource
    ISSN: 2151-2043
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    Verlag: The Electrochemical Society
    Publikationsdatum: 2017
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  • 9
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    The Electrochemical Society ; 2015
    In:  ECS Meeting Abstracts Vol. MA2015-01, No. 2 ( 2015-04-29), p. 243-243
    In: ECS Meeting Abstracts, The Electrochemical Society, Vol. MA2015-01, No. 2 ( 2015-04-29), p. 243-243
    Kurzfassung: The improvement of the energy density of current Li-Ion batteries and the development of novel, post-Li-Ion energy storage devices is largely hindered by a poor understanding of the cell chemistry and degradation mechanisms which ultimately lead to a low cycle life and/or poor rate capability. For example, some controversy still exists regarding the formation of Li 2 S and is related to the fact that intermediates can’t be easily characterized due to their low stability. In-situ speciation using common characterization techniques including X-ray diffraction (XRD) [1, 2] and Ultraviolet-visible spectroscopy (UV-VIS) [3, 4] was previously attempted but yet unable to yield a clear understanding of intermediates involved in the electrochemical conversion of sulfur to Li 2 S during discharge of the battery. This is mainly due to the fact that they detect either solid or liquid species but not both at the same time. X-ray absorption spectroscopy (XAS) eliminates these restrictions and thus provides a powerful tool for monitoring compositional changes during operation of a battery. Different sulfur species exhibit characteristic features, dependent on their chemical composition, in the x-ray absorption near-edge structure (XANES) at the S K-edge, exploited in previous studies [5-8]. However, a drawback in these previous measurements was the data collection geometry in which the x-ray beam was penetrating the cell through the backside of the sulfur electrode. In this work, we introduce a novel spectro-electro­chemical cell which allows direct observation of intermediates in the separator and use it to explore the influence of the electrolyte solvent’s dielectric constant on the conversion of polysulfides to Li 2 S by comparing solvents with a low-dielectric constant (DOL:DME, 1:1 v/v) and a high-dielectric constant (DMAC), the first discharge curves of which are shown in Figure 1. Figure 1: Galvanostatic discharge curves measured in operando mode at a C-rate of 0.1 h -1 using either DOL-DME (1:1 v/v) or DMAC, each containing 1M LiClO 4 and 0.5M LiNO 3 . Our operando XAS measurements show that the formation of Li 2 S is faster in DOL:DME compared to DMAC, and also suggest that Li 2 S 2 species is present at the end of discharge in DOL:DME. Furthermore, contrary to other reports, we do not detect any elemental sulfur at the end of discharge [5]. References: [1] N. A. Cañas, S. Wolf, N. Wagner and K. A. Friedrich, J. Power Sources , 226 , 313 (2013). [2] S. Walus, C. Barchasz, J.-F. Colin, J.-F. Martin, E. Elkaim, J.-C. Lepretre and F. Alloin, Chem. Commun. , 49 , 7899 (2013). [3] R. Bonnaterre and G. Cauquis, J. Chem. Soc., Chem. Commun. , 293 (1972). [4] N. A. Cañas, D. N. Fronczek, N. Wagner, A. Latz and K. A. Friedrich, J. Phys. Chem. C , 118 , 12106 (2014). [5] M. Cuisinier, P.-E. Cabelguen, S. Evers, G. He, M. Kolbeck, A. Garsuch, T. Bolin, M. Balasubramanian and L. F. Nazar, J. Phys. Chem. Lett. , 4 , 3227 (2013). [6] M. E. Fleet and X. Liu, Spectrochim. Acta B , 65 , 75 (2010). [7] T. A. Pascal, K. H. Wujcik, J. Velasco-Velez, C. Wu, A. A. Teran, M. Kapilashrami, J. Cabana, J. Guo, M. Salmeron, N. Balsara and D. Prendergast, J. Phys. Chem. Lett. , 5 , 1547 (2014). [8] M. U. M. Patel, I. Arčon, G. Aquilanti, L. Stievano, G. Mali and R. Dominko, ChemPhysChem , 15 , 894 (2014). Figure 1
    Materialart: Online-Ressource
    ISSN: 2151-2043
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    Verlag: The Electrochemical Society
    Publikationsdatum: 2015
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  • 10
    In: ECS Meeting Abstracts, The Electrochemical Society, Vol. MA2018-01, No. 30 ( 2018-04-13), p. 1721-1721
    Kurzfassung: The independence from Platinum-Group-Metal (PGM) is one of the major goals towards the commercialization of Proton Exchange Membrane Fuel Cells (PEMFCs), due to the limited availability of PGM and their considerable loading on the Oxygen-Reduction-Reaction (ORR), increasing their cost contribution to the overall system. On the other hand, the challenges for PGM-free ORR catalysts are an activity approaching that of Pt and a long-term operational stability in the strong acidic environment of a PEMFC. Low-cost FeNC catalysts fulfill the high activity requirement, but they still face fast degradation in acidic environment [1, 2]. On the contrary, pure valve-metal oxides as non-PGM ORR catalysts need a significant improvement in ORR activity and H 2 O yield but they are very promising in terms of stability during PEMFC operation [3, 4]. The aim of this contribution is to combine the intrinsic high ORR activity of Fe with the stability of valve-metal oxides, via partial substitution of Zr 4+ with Fe 3+ in the ZrO 2 structure [5]. The formation of a solid solution of oxides of the two aliovalent-metals should also provide oxygen vacancies or uncoordinated metal sites at the oxide surface, hypothesized to be correlated to an increased ORR activity of valve-metal oxides [6, 7] . In this study, to obtain Fe-substituted ZrO 2 we used a homogeneous mixture of the two metals at the molecular level, by employing two soluble organometallic precursors, i. e., zirconium (IV) tetra-tert-butyl dichloro phthalocyanine (ZrCl 2 Pc(tBu) 4 ) and iron(II) tetra-tert-butyl phthalocyanine (FePc(tBu) 4 ). Graphitized Ketjen-Black carbon is first impregnated with the precursors and then heat-treated as described in [8, 9]. XRD and TEM characterization show that our catalysts consist of ZrO 2 particles of about 3 nm (Fe-substituted) and 7 nm (pure ZrO 2 ). Mössbauer spectroscopy reveals that the Fe moieties are isolated and in Fe 3+ electronic configuration at high spin, typical of an oxidic environment. This is confirmed by soft XAS data at the Fe L-edge and XPS data, pointing to the desired Fe x Zr 1-x O 2-δ phase. We already published an evaluation of the ORR mass activity of Fe x Zr 1-x O 2-δ in comparison to Fe-only and ZrO 2 -only catalysts, using a thin-film rotating (ring) disk electrode (RRDE) setup [9]. Using the preferred catalyst Fe 0.07 Zr 0.93 O 2-δ , the variation of its mass activity and selectivity as a function of the loading is further discussed, with a H 2 O 2 yield even lower in comparison to an FeNC catalyst [10]. The catalyst mass activity and its Arrhenius analysis in a single PEMFC at ≈0.4 mg cat /cm² is compared to the RDE results (Figure 1) [11]. The Arrhenius analysis resulted in an ORR activation energy of 16 kJ/mol (RDE) and 18 kJ/mol (PEMFC) at 0.4 V RHE , significantly lower than our best pure-ZrO 2 catalyst reported (21 kJ/mol from RDE and 29 kJ/mol from PEMFC data) [4]. Stability tests and loading optimization of nanometric Fe x Zr 1-x O 2-δ will be the future outlook. Acknowledgements: This work was supported by the Bayerische Forschungsstiftung (Project ForOxiE², AZ 1143-14). References: [1] M. Lefèvre, J. P. Dodelet, ECS Transactions 2012 , 45(2) , 35-44. [2] B. Piela, T. S. Olson, P. Atanassov, P. Zelenay, Electrochimica Acta 2010 , 55 , 7615-7621. [3] A. Ishihara, S. Yin, K. Suito, N. Uehara, Y. Okada, Y. Kohno, K. Matsuzawa, S. Mitsushima, M. Chisaka, Y. Ohgi, M. Matsumoto, H. Imai, K. Ota, ECS Transactions 2013 , 58 , 1495-1500. [4] T. Mittermeier, P. Madkikar, X. Wang, H. A. Gasteiger and M. Piana, J. Electrochem. Soc. 2016 , 163 , F1543-F1552. [5] D. Sangalli, A. Lamperti, E. Cianci, R. Ciprian, M. Perego, A. Debernardi, Phys. Rev. B 2013 , 87 , 085206. [6] A. Ishihara, M. Tamura, Y. Ohgi, M. Matsumoto, K. Matsuzawa, S. Mitsushima, H. Imai, K.-i. Ota, J. Phys. Chem. C , 2013 , 117 , 18837–18844. [7] Y. Ohgi, A. Ishihara, K. Matsuzawa, S. Mitsushima, K.-i. Ota, M. Matsumoto, H. Imai, J. Electrochem. Soc. 2013 , 160 , F162-F167. [8] P. Madkikar, X. Wang, T. Mittermeier, A. H. A. Monteverde Videla, C. Denk, S. Specchia, H. A. Gasteiger, M. Piana, J. Nanostruct. Chem. 2017 , 7 , 133-147. [9] P. Madkikar, T. Mittermeier, H. A. Gasteiger, M. Piana, J. Electrochem. Soc. 2017 , 164(7) , F831-F833. [10] A. Bonakdarpour, M. Lefevre, R. Yang, F. Jaouen, T. Dahn, J.-P. Dodelet, J. R. Dahn, Electrochem. Solid-State Lett. 2008 , 11(6) , B105-B108. [11] P. Madkikar, D. Menga, G. Harzer, T. Mittermeier, F. E. Wagner, M. Merz, S. Schuppler, P. Nagel, A. Siebel, H. A. Gasteiger, M. Piana, manuscript in preparation . Figure 1
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    ISSN: 2151-2043
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    Verlag: The Electrochemical Society
    Publikationsdatum: 2018
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