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  • 1
    Online Resource
    Online Resource
    Springer Science and Business Media LLC ; 2022
    In:  International Journal of Intelligent Transportation Systems Research Vol. 20, No. 1 ( 2022-04), p. 330-355
    In: International Journal of Intelligent Transportation Systems Research, Springer Science and Business Media LLC, Vol. 20, No. 1 ( 2022-04), p. 330-355
    Abstract: To evaluate the generalities of acceptability of a proactive braking intervention system, which anticipates an imaginary pedestrian rushing out from occluded areas, and driving environmental dependencies, we conducted field operation tests (FOTs), where 146 elderly drivers participated at three evaluation sites with different urban characteristics. Analyses regarding the coexisting traffic participants illustrate driving environmental characteristics at each evaluation site. Evaluations via TMT-J, DSQ, and WSQ compare the characteristics of experimental participants. Based on these results as premises, we analyze questionnaire answers regarding the proposed system. As a result, we confirm the generalities that more than half of the participants at each evaluation site expressed a desire to introduce the proposed system into their own vehicle.
    Type of Medium: Online Resource
    ISSN: 1348-8503 , 1868-8659
    Language: English
    Publisher: Springer Science and Business Media LLC
    Publication Date: 2022
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  • 2
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    Online Resource
    Springer Science and Business Media LLC ; 2022
    In:  International Journal of Intelligent Transportation Systems Research Vol. 20, No. 1 ( 2022-04), p. 356-357
    In: International Journal of Intelligent Transportation Systems Research, Springer Science and Business Media LLC, Vol. 20, No. 1 ( 2022-04), p. 356-357
    Type of Medium: Online Resource
    ISSN: 1348-8503 , 1868-8659
    Language: English
    Publisher: Springer Science and Business Media LLC
    Publication Date: 2022
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  • 3
    In: Gene, Elsevier BV, Vol. 194, No. 2 ( 1997-7), p. 241-247
    Type of Medium: Online Resource
    ISSN: 0378-1119
    RVK:
    Language: English
    Publisher: Elsevier BV
    Publication Date: 1997
    detail.hit.zdb_id: 1491012-3
    SSG: 12
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  • 4
    In: Journal of The Electrochemical Society, The Electrochemical Society, Vol. 167, No. 4 ( 2020-02-20), p. 044513-
    Type of Medium: Online Resource
    ISSN: 1945-7111
    Language: Unknown
    Publisher: The Electrochemical Society
    Publication Date: 2020
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  • 5
    In: ECS Meeting Abstracts, The Electrochemical Society, Vol. MA2022-02, No. 42 ( 2022-10-09), p. 1561-1561
    Abstract: 1. Introduction Improvement in ORR activity of Pt-based catalysts for use in PEFCs of FCVs is crucial for cost reduction and widespread use [1]. We reported that surface modification of Pt and Pt-based catalysts with melamine molecules enhances ORR activity [2, 3] . However, it is predicted that the melamine is easily washed off by water generated at the cathode in PEFCs because melamine is soluble in water. In this study, organic salts composed of protonated melamine derivatives and bis (nonafluorobutanesulfonyl)imide were newly synthesized to suppress the washing-off effects. Pt and Pd@Pt core-shell catalysts were modified with the organic salts, and the ORR activity and the I-V performance were investigated. 2. Experimental Ketjen Black EC-600JD (KB, S BET : 1,345 m 2 /g, LION) and mesoporous carbon (MPC, CNovel MH-18 ® , S BET 1,334 m 2 /g, TOYO TANSO) were used as carbon supports for Pd@Pt core-shell and Pt catalysts, respectively. The Pt/Pd/KB core-shell catalyst was synthesized by a direct displacement reaction method [4] and the Pt/MPC catalyst was synthesized by an impregnation/thermal reduction method. The organic salts were synthesized by mixing equimolar melamine derivatives and Li bis (nonafluorobutanesulfonyl)imide in 0.1 M HNO 3 aqueous solution at 80 o C. Pt/Pd/KB catalyst was loaded onto a glassy carbon electrode and immersed in acetone containing 0.1 mM organic salts for 10 min. to modify the catalyst surface with the organic salts. CV of Pt/Pd/KB catalyst was recorded at 25 o C in Ar-saturated 0.1 M HClO 4 with a potential scan rate of 50 mV/s and LSV was measured by RDE method at 25 o C in O 2 -saturated 0.1 M HClO 4 with a potential scan rate of 10 mV/s at a rotation speed of 1,600 rpm. Pt/MPC catalyst was dispersed in acetone containing 20 wt.% organic salt and acetone was slowly evaporated by using an evaporator to modify the catalyst with organic salt, and used for 1 × 1 cm 2 MEA tests. The MEA was fabricated by a decal method using Nafion ® membrane (25 µm in thickness) and a GDL (SGL). Nafion ® DE2020 was used as an ionomer for catalyst ink preparation (I/C: 0.83). The Pt loading of the cathode catalyst layer in the MEA was set to 0.1 mg-Pt/cm 2 . I-V performance of the MEA was evaluated at 80 o C, 75% RH. H 2 gas (418 NmL) and air (998 NmL) were supplied to the anode and the cathode, respectively, and the H 2 gas was pressurized to 150 kPa (ambient + 50 kPa) at the gas-outlet (H 2 utilization: 5% at a current density of 3.0 A/cm 2 ). 3. Results and Discussion Figure 1 shows molecular structure of an organic salt of [diethylmelamine+H] + [ bis (nonafluorobutanesulfonyl)imide] - ([DEM] + [NFSI] - ). The salt was synthesized in 0.1 M HNO 3 (pH 1) at 80 o C and was obtained in a solid state in the solution with a yield 〉 90%. CVs of Pt/Pd/KB catalyst and after modification with [DEM] + [NFSI] - are depicted in Figure 2. Hydrogen adsorption/ desorption waves observed in the potential range of 0.05-0.4 V were slightly suppressed by the modification, indicating that surface Pt active sites were partially occupied by the salt. Simultaneously, the onset potential for Pt-OH formation was positively shifted and the formation of Pt-oxygenated species was suppressed in the high potential range of 0.7-1.2 V, showing that the modified Pt surface retained more metallic state at high potentials. Figure 3 demonstrates LSVs of the Pt/Pd/KB catalyst and after modification with [DEM] + [NFSI] - . The LSV of the catalyst positively shifted by the modification and the ORR mass activity was enhanced from 1,223 to 2,234 A/g-Pt at 0.9 V. These results indicated that the modification of the Pt/Pd/KB catalyst with [DEM] + [NFSI] - was effective in enhancing ORR activity and the results are almost the same as the activity enhancement observed by melamine modification [3]. Figure 4 shows I-V performance of the MEA using Pt/MPC as the cathode catalyst. The cell voltage of the MEA using the modified Pt/MPC exceeded that using the unmodified catalyst in the whole current density region, indicating that ORR activity enhancement by the organic salt modification was also demonstrated in the MEA tests. Furthermore, the resistance and the diffusion overpotentials as well as the activation overpotential were all reduced by the modification with [DEM] + [NFSI] - . Thus, the organic salt could interact with ionomers or membrane and decrease the resistance and the diffusion overpotentials. This study was partly supported by NEDO, Japan. References [1] M. Suzuki, FCCJ, https://www.nedo.go.jp/content/100895111.pdf, June 2019, in Japanese. [2] M. Asahi et al ., J. Electrochem. Soc ., 166 , F498 (2019). [3] S. Yamazaki et al ., ACS Catal ., 10 , 14567 (2020). [4] N. Aoki et al ., J. Electrochem. Soc ., 1 67 , 044513 (2020). Figure 1
    Type of Medium: Online Resource
    ISSN: 2151-2043
    Language: Unknown
    Publisher: The Electrochemical Society
    Publication Date: 2022
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  • 6
    Online Resource
    Online Resource
    The Electrochemical Society ; 2014
    In:  ECS Meeting Abstracts Vol. MA2014-02, No. 21 ( 2014-08-05), p. 1134-1134
    In: ECS Meeting Abstracts, The Electrochemical Society, Vol. MA2014-02, No. 21 ( 2014-08-05), p. 1134-1134
    Abstract: Introduction Core/shell structured catalyst is a promising candidate for the decrease and it has been reported that ORR activity of the Pt shell can be enhanced with Pd core [1]. Recently, we have reported that the ORR activity of carbon supported Pd core/Pt shell structured catalyst (Pt/Pd/C) is improved after an accelerated durability test (ADT, 0.6-1.0 V vs . RHE at 80°C, 10,000 cycles) [2]. Morphology of the catalyst changed into a spherical shape and more than 50 % of the Pd core dissolved out after the ADT, which are considered to be important factors for the improvement of the ORR activity. However, since the Pd is also an expensive precious metal, inexpensive alternatives to the Pd core are the key for further cost reduction of the PEFCs. We selected Ag as the alternative, because it has a redox potential close to that of Pd in addition to its lower material cost. However, since Ag has the lowest melting point in precious metals, it is difficult to synthesize fine size Ag core. In this study, carbon supported AgPt alloyed catalyst (AgPt/C) was synthesized to obtain AgPt NP with a size less than 5 nm. Change in the ORR activity of the AgPt/C alloy catalyst with the ADT was studied. Experimental The C 17 H 35 COOAg and Pt(acac) 2 were dissolved into dibenzyl ether at 80°C and oleylamine (OAm) was added as a stabilizer. The solution was heated to 180°C under N 2 atmosphere and kept for 1 h while stirring [3]. The AgPt NPs were collected by centrifugation and washed with EtOH. The AgPt NPs were re-dispersed in n -hexane and stirred with a carbon support (Ketjen black EC300J) to obtained the AgPt/C catalyst. The AgPt/C catalyst was heat-treated at 400°C under 15 % H 2 /Ar for 1 h to remove OAm. The AgPt/C catalyst was characterized with TG-DTA, XRD, TEM, SEM-EDX and CV. ORR activity of the catalyst was measured with the RDE technique in O 2 saturated 0.1 M HClO 4 at 25°C. ADT was conducted with a rectangular wave potential cycling (0.6 V (3 s)-1.0 V (3 s), 10,000 cycles) in Ar saturated 0.1 M HClO 4 at 80°C. Results and Discussion The composition of an as-made AgPt/C catalyst was Ag 64 Pt 36 (in at.%) and the mean diameter was 3.6 nm. The mean diameter of the catalyst slightly increased to 4.7 nm after heat treatment at 400°C. XRD patterns of the AgPt/C catalysts are depicted in Fig. 1. The (220) diffraction showed an asymmetry peak with a swelling toward higher diffraction angle, suggesting the presence of Pt-rich portions in the AgPt NPs. Ag has a lower surface energy (1.3 J/m 2 ) than that of Pt (2.5 J/m 2 ), which could cause surface segregation of Ag after the heat treatment. CVs of the AgPt/C catalyst are demonstrated in Fig. 2. The Ag oxidation wave is observed at ca. 0.7 V in the first cycle. However, the oxidation wave disappeared and H UPD wave increased after repeated CV cycles. These fact indicate that Ag existed in the topmost surface of the as-made AgPt NPs and that Pt-rich shell was formed due to dissolution of the Ag after the repeated CV cycles. ADT of the AgPt/C catalyst was conducted at 80°C, by which the ECSA of the catalyst decreased from 40 to 16 m 2 /g-Pt. SEM-EDX compositional analysis revealed that Ag completely dissolved out during the ADT. TEM images of the AgPt/C catalysts are shown in Fig. 3. The small particle disappeared and morphology of the catalyst changed into spherical shape after ADT without a significant size change. After the ADT, the ORR specific activity of the AgPt/C catalyst was improved from 362 to 1163 μA/cm 2 , which was 3.3-fold of a commercial Pt/C catalyst, (TEC10E50E, TKK). Although the mass activity of the catalyst improved from 148 to 180 A/g-Pt after the ADT, the mass activity was inferior to that of the Pt/C catalyst (255 A/g-Pt). It is considered that the slight enhancement in mass activity of the AgPt/C catalyst is caused by a decrease of the Pt utilization efficiency due to the complete dissolution of Ag. Suppression of the Ag dissolution during the ADT is considered to be crucial for the enhancement of the ORR mass activity of the catalyst and some trials will be presented. Acknowledgement This work was supported by New Energy and Industrial Technology Development Organization, NEDO Japan. References [1] J. Zhang et al ., J. Phys. Chem. B , 108 , 10955 (2004). [2] H. Daimon et al ., 224 th ECS Meeting, Abstract #1404, San Francisco, USA (2013). [3] Z. Peng et al ., Adv. Funct. Mater ., 20 , 3734 (2010).
    Type of Medium: Online Resource
    ISSN: 2151-2043
    Language: Unknown
    Publisher: The Electrochemical Society
    Publication Date: 2014
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  • 7
    Online Resource
    Online Resource
    The Electrochemical Society ; 2013
    In:  ECS Meeting Abstracts Vol. MA2013-02, No. 15 ( 2013-10-27), p. 1497-1497
    In: ECS Meeting Abstracts, The Electrochemical Society, Vol. MA2013-02, No. 15 ( 2013-10-27), p. 1497-1497
    Abstract: Abstract not Available.
    Type of Medium: Online Resource
    ISSN: 2151-2043
    Language: Unknown
    Publisher: The Electrochemical Society
    Publication Date: 2013
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  • 8
    Online Resource
    Online Resource
    The Electrochemical Society ; 2014
    In:  ECS Meeting Abstracts Vol. MA2014-02, No. 21 ( 2014-08-05), p. 1063-1063
    In: ECS Meeting Abstracts, The Electrochemical Society, Vol. MA2014-02, No. 21 ( 2014-08-05), p. 1063-1063
    Abstract: Introduction Core-shell structured catalyst is a promising candidate for the decrease in usage amount of an expensive Pt cathode catalyst for PEFCs. Adzic and his co-workers demonstrated that carbon supported Pd core-Pt shell structured catalyst (Pt/Pd/C) exhibits higher ORR performance relative to that of a commercial Pt/C catalyst [1] and that the Pd core dissolves out during an accelerated durability test (ADT) using potential cycling [2] . We have recently reported that ORR activity of the Pt/Pd/C catalyst synthesized with a modified Cu under potential deposition (Cu-UPD) and a Pt replacement processes is enhanced with the ADT performed at 80°C [3, 4]. After the ADT, morphology of the Pt/Pd/C catalyst changed into spherical shape and mean diameter of the catalyst decreased associated with an oxidative dissolution of the Pd core. It was presumed that the enhancement of the ORR activity was caused from decrease in number of low-coordinated Pt atoms by rearrangement of the surface Pt atoms with the ADT. Interestingly, the core-shell structure was retained even after the ADT. In this study, carbon supported PtPd alloy catalyst (PtPd/C) was prepared through one-pot synthesis and change in the ORR activity of the catalyst by the ADT at 80°C was investigated in comparison with that of the Pt/Pd/C catalyst. Experimental Pt/Pd/C catalyst was synthesized with modified Cu-UPD and Pt replacement processes [3]. Carbon supported Pd core (Pd/C, 4.2 nm, 30 wt.%) was dispersed 0.05 M H 2 SO 4 containing 0.01 M CuSO 4 and stirred under Ar atmosphere with co-existence of Cu mesh, by which Cu shell was formed on the Pd core surface. Then, the Cu mesh was removed and K 2 PtCl 4 was added to replace the Cu shell with the Pt one, giving the Pt/Pd/C catalyst. PtPd/C alloy catalyst was prepared with one-pot reduction method. H 2 PtCl 6 and Na 2 PdCl 4 were dissolved into DI water and pH of the solution was adjusted at 3.5 by NaOH, followed by addition of a carbon support (Ketjen black EC 300J). The solution was stirred at 60°C in air and NaBH 4 was added in drop-wise, forming the PtPd/C alloy catalyst [5]. Catalysts were characterized with TG, XRD, XRF, TEM, TEM-EDX and CV. ORR activities of the catalysts were evaluated with RDE technique in O 2 saturated 0.1 M HClO 4 at 25°C. ADT was conducted using a rectangular wave potential cycling (0.6 V (3 s)-1.0 V (3 s) vs . RHE, 10,000 cycles) in Ar saturated 0.1 M HClO 4 at 80°C. Results and Discussion XRD patterns of the catalysts are shown in Fig. 1. All samples exhibited characteristic diffraction patterns of fcc structure. In PtPd/C catalyst, composition was Pt 51 Pd 49 (in at.%) and (220) diffraction peak angle was close to that of the Vegard’s law (dotted blue arrow), indicating that Pt and Pd are well-mixed and form alloy particle. In Pt/Pd/C catalyst, (220) diffraction peak angle did not change after Pt shell formation and peak symmetry was retained. TG and XRF analyses showed that the Pt shell formed on the Pd core surface corresponds to 1.1 times of Pt monolayer. TEM images of the catalysts are depicted in Fig. 2. In PtPd/C catalyst, small size PtPd NPs disappeared after ADT and mean diameter of the catalyst increased. On the contrary, morphology of Pt/Pd/C catalyst changed into a spherical shape with ADT and mean diameter decreased. XRF compositional analysis revealed that 41 % and 70 % Pd were dissolved out from the PtPd/C and the Pt/Pd/C catalyst, respectively, after the ADT. Figure 3 summarizes ORR mass activity of the catalysts in comparison with that of a commercial Pt/C catalyst (TEC10E50E, TKK). Initial PtPd/C catalyst showed the highest ORR mass activity due to its high specific activity. After ADT at 80°C, ORR mass activity of Pt/Pd/C catalyst was largely enhanced (3.0-fold of Pt/C catalyst). Interestingly, TEM-EDX analysis indicated that core-shell structure was retained even after the ADT, which suggests that the core-shell structure is stable although more than 50 % of the Pd core dissolved out with ADT. ORR mass activity of the PtPd/C alloyed catalyst could be enhanced with suppression of large decrease in electrochemical surface area with ADT. Acknowledgement This work was supported by NEDO Japan. References [1] A. U. Nilekar et al ., Top. Catal ., 46 , 276 (2007). [2] K. Sasaki et al ., Angew. Chem. Int. Ed ., 49 , 8602 (2010). [3] Y. Ikehata et al ., 224 th ECS Meeting, Abstract #1497, San Francisco, USA (2013). [4] H. Daimon et al ., 224 th ECS Meeting, Abstract #1404, San Francisco, USA (2013). [5] K. Okuno et al ., 81 st Japanese Electrochemical Society Meeting, Abstract PFC05, Osaka, Japan (2014).
    Type of Medium: Online Resource
    ISSN: 2151-2043
    Language: Unknown
    Publisher: The Electrochemical Society
    Publication Date: 2014
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  • 9
    Online Resource
    Online Resource
    The Electrochemical Society ; 2013
    In:  ECS Meeting Abstracts Vol. MA2013-02, No. 15 ( 2013-10-27), p. 1520-1520
    In: ECS Meeting Abstracts, The Electrochemical Society, Vol. MA2013-02, No. 15 ( 2013-10-27), p. 1520-1520
    Abstract: Abstract not Available.
    Type of Medium: Online Resource
    ISSN: 2151-2043
    Language: Unknown
    Publisher: The Electrochemical Society
    Publication Date: 2013
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  • 10
    Online Resource
    Online Resource
    The Electrochemical Society ; 2015
    In:  ECS Meeting Abstracts Vol. MA2015-02, No. 37 ( 2015-07-07), p. 1396-1396
    In: ECS Meeting Abstracts, The Electrochemical Society, Vol. MA2015-02, No. 37 ( 2015-07-07), p. 1396-1396
    Abstract: Introduction Reduction of the amount of expensive Pt cathode catalyst in PEFCs is essential for their worldwide commercialization. Core-shell structured catalyst, in which Pt monolayer (Pt ML ) shell is formed on non-Pt metal core surface, is one of the key technologies. Furthermore, it has been reported that ORR activity of the Pt ML shell is enhanced when Pd nanoparticles are used as core materials [1, 2]. Recently, we developed a new process for the Pt shell formation which needs no precise potential control and is suitable for scale-up synthesis of the core-shell structured catalyst (modified Cu-UPD/Pt replacement [3] ). We further demonstrated that the ORR mass activity of a carbon supported Pd core-Pt shell structured catalyst (Pt/Pd/C) synthesized by the new process is drastically enhanced with an accelerated durability test (ADT) performed at 80°C [3]. The ORR activity enhancement is considered to be due to a rearrangement of the surface Pt atoms and a decrease in number of low-coordinated Pt atoms associated with oxidative dissolution of Pd from the core nanoparticles. In this study, Pt/Pd/C catalysts with different Pt shell coverages are synthesized via the modified Cu-UPD/Pt replacement process and the influence of the Pt shell coverage on the ORR activity of the catalysts after ADT was investigated. Experimental Pt/Pd/C catalysts were synthesized with the modified Cu-UPD/Pt replacement process [3]. Carbon supported Pd core particles (Pd/C, Pd size: 4.2 nm, Pd loading: 30 wt.%, Ishifuku Metal Industry) were ultrasonically dispersed in 50 mM H 2 SO 4 containing 10 mM CuSO 4 and the solution was stirred with co-existence of a metallic Cu sheet at 5°C under Ar atmosphere. After stirred for 5 h, the Cu sheet was removed and K 2 PtCl 4 with different concentrations was added to obtain the Pt/Pd/C catalysts with different Pt shell coverages. The Pt/Pd/C catalysts were characterized by TG, XRF, XRD, TEM, TEM-EDX, CV and XAFS. The ORR activity of the Pt/Pd/C catalysts was evaluated with the RDE technique in O 2 saturated 0.1 M HClO 4 at 25°C. The ADT was conducted using a rectangular wave potential cycling (0.6 V (3 s)-1.0 V (3 s) vs . RHE) in Ar saturated 0.1 M HClO 4 at 80°C for 1,000 cycles. Results and discussion The compositions of the two Pt/Pd/C catalysts synthesized with different K 2 PtCl 4 concentrations were Pt 21 Pd 79 and Pt 30 Pd 70 (atomic %) and their Pt shell thicknesses were calculated to be 0.6 and 1.0 ML, respectively (hereafter called Pt 0.6 ML /Pd/C and Pt 1.0 ML /Pd/C). CVs of the Pt/Pd/C catalysts are shown in Fig. 1. In the potential range of 0.05-0.1 V vs . RHE, hydrogen absorption/desorption peaks, which are characteristics of Pd, were observed and these peaks were stronger in the Pt 0.6 ML /Pd/C catalyst, indicating that the Pt shell coverage is lower in the Pt 0.6 ML /Pd/C catalyst. TEM images of the Pt 0.6 ML /Pd/C catalysts are shown in Fig. 2. Small catalyst particles disappeared and the morphology changed into spherical shape after ADT. TEM-EDX analysis revealed that composition of the Pt 0.6 ML /Pd/C and Pt 1.0 ML /Pd/C catalysts changed to Pt 48 Pd 52 and Pt 50 Pd 50 , respectively, after ADT. Suppose that the Pt shell does not dissolve during ADT, the Pd core dissolution in the Pt 0.6 ML /Pd/C and Pt 1.0 ML /Pd/C catalysts are estimated as 71% and 57%, respectively. Changes in ORR mass activity of the Pt/Pd/C catalysts after ADT are summarized in Fig. 3 together with a carbon supported Pt reference catalyst (Pt/C, Pt size: 2.8 nm, Pt loading: 46 wt.%, TEC10E50E, TKK). The ORR mass activities of both Pt/Pd/C catalysts were enhanced after ADT and the enhancement was higher for the Pt 0.6 ML /Pd/C catalyst (2.6-fold of the Pt/C catalyst). As described above, the Pd core dissolution by the ADT is larger in the Pt 0.6 ML /Pd/C catalyst (71%), which is due to the lower Pt shell coverage in the catalyst (Fig. 1).  Since the ORR activity enhancement of the Pt/Pd/C catalyst during ADT arises from rearrangement of the Pt shell associated with the Pd core dissolution, it is considered that the lower Pt shell coverage in the Pt 0.6 ML /Pd/C catalyst is, the more the Pd core dissolution and the rearrangement of the Pt shell is enhanced. The micro-structural change of the Pt/Pd/C catalysts after ADT will be presented at the meeting. Acknowledgement This work was supported by New Energy and Industrial Technology Development Organization (NEDO), Japan. References [1] J. Zhang et al ., J. Phys. Chem. B , 108 , 10955 (2004). [2] A. U. Nilekar et al ., To p Catal ., 46 , 276 (2007). [3] M. I naba and H. Daimon, J. Jpn. Petrol. Inst. , 58 (2), 55-63 (2015). Figure 1
    Type of Medium: Online Resource
    ISSN: 2151-2043
    Language: Unknown
    Publisher: The Electrochemical Society
    Publication Date: 2015
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