Journal of Computer Chemistry, Japan
Online ISSN : 1347-3824
Print ISSN : 1347-1767
ISSN-L : 1347-1767
速報
Effect of Pore Size of Carbon Support on Electrode Reaction Activity of Catalyst Layer in Polymer Electrolyte Fuel Cell: Reactive Molecular Dynamics Simulations
Tetsuya NAKAMURARiku OTSUKIShuichi UEHARAYuta ASANOQian CHENYusuke OOTANINobuki OZAWAMomoji KUBO
著者情報
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2021 年 20 巻 4 号 p. 150-154

詳細
Abstract

For large output of polymer electrolyte fuel cells (PEFCs), the electrode reaction activity of the catalyst layer (CL) consisting of carbon supports, Pt nanoparticles, Nafion chains, and water should be improved. Experimentally, it is reported that when Ketjen black (KB) with meso pores is used as the carbon support, the output of PEFC increases and that the pore size of the KB support affects the electrode reaction activity of the Pt nanoparticles. Therefore, in the present study, to clarify the effect of pore size on the electrode reaction activity of the Pt nanoparticles, we constructed catalyst particle (CP) models in which the Pt nanoparticles are supported and Nafion chains are coated on the KB model and investigated the CP structures with a different pore size of the KB support by reactive molecular dynamics method. Regardless of the pore size, the Pt nanoparticles on the exterior of the pore are fully covered with the Nafion chains and the Pt nanoparticles in the interior of the pore are not covered with the Nafion chains. This result suggests that the Pt nanoparticles in the interior of the pore show high oxygen transport property that does not depend on the pore size. Furthermore, we evaluated the connectivity of the Nafion chains to H2O molecules absorbed on the Pt nanoparticles on the exterior and in the interior of the pores because the Nafion chains conduct the protons to the H2O molecules on the Pt nanoparticles. As the pore size increases, more Nafion chains penetrate the interior of the pore and contact with H2O molecules on the Pt nanoparticles, because more Nafion chains are vertically distributed above the larger pore. Finally, these results propose that both high oxygen transport property and high electrode reaction activity are achieved over the Pt nanoparticles in the interior of the large pore of the KB support because the oxygen diffusion in the pore is not blocked by the Nafion chains and the large pore size promotes the formation of a proton conducting path composed of the Nafion chains, H2O, and Pt nanoparticles.

1 Introduction

Fuel cells that use hydrogen fuel and emit no carbon dioxide, are strongly required to realize a clean energy society. Polymer electrolyte fuel cells (PEFCs) are utilized for vehicles at present and intended to be applied to large mobilities such as buses, trains, and ships. Thus, it is necessary to increase the output of PEFC, which is achieved by improving the electrode reaction activity of the catalyst layer (CL) in PEFC. The CL consists of carbon supports, Pt nanoparticles, ionomer, and water, and the activity for electrode reactions on the Pt nanoparticles such as oxygen reduction reaction (ORR) depends on the structure of the carbon support surface and the composition of ionomer and water in the CL. Then, many researchers have investigated the effect of the surface structure of the carbon supports on the electrode reaction activity of the Pt nanoparticles on the CL. For example, Yarlagadda et al. showed that the cathode CL with Ketjen black (KB) support has higher electrode reaction activity compared to that with carbon black supports without pores [1]. Moreover, the KB support with accessible pores was found to show higher electrode reaction activity than that with curved pores. Kobayashi et al. reported that in the case of the KB support with large pores at the cathode, the Pt nanoparticles in the large pores showed a higher effective surface area and a higher electrode reaction activity than those on other sites [2]. Therefore, elucidating the effect of the pore structure of the KB support on the electrode reaction activity of the CL and optimizing the carbon support structure will contribute to the improvement of the output of PEFC. In the present study, to improve ORR activity at the cathode, we analyzed the ionomer and water coverage over the Pt nanoparticles on KB support with different pore sizes to clarify the effect of the pore size on the electrode reaction activity of the Pt nanoparticles in the CL from a nanoscale perspective.

2 Method and Model

To investigate distributions of the Nafion chains and water molecules around Pt nanoparticles in the CL, we used our developed molecular dynamics simulator "Laich" [3]. ReaxFF developed by Duin et al. was used as the force field to handle bond generation and dissociation during electrode chemical reactions [4]. We calculated the charge of each atom by electron equilibration method [5]. To construct the KB model, six pores were created in an amorphous carbon sphere with a diameter of 20 nm. Matsuhashi, et al. showed that the pore size in the commercial KB particles of EC300J and ECP600JD is distributed in the range of 3.0-10.0 nm [6]. Then in this study, two models with different pore sizes of 4 and 6 nm were constructed. These pore sizes are in the range observed experimentally. The shape of the pore is a cone with a depth of 7.5-8.0 nm. To stabilize the KB models, the KB models were relaxed with the NVT ensemble at a temperature of 400 K for 5 ps. In addition, ten and four Pt nanoparticles with a diameter of 1 nm were put on the KB outer surface and inside pores, respectively. To promote the adhesion of Pt nanoparticles to the KB models, the Pt-supported KB models were relaxed with the NVT ensemble at a temperature of 400 K for 10 ps. Next, to stabilize the Pt-supported KB models, the Pt-supported KB models were relaxed with the NVT ensemble at a temperature of 300 K for 15 ps. The pore sizes of the KB models and Pt-supported KB models did not change before and after the relaxations. Then, the dangling bonds on the KB support were terminated with OH and H groups. Figure 1 presents the Pt-supported KB model with a pore of 6 nm in size. For an ionomer, a Nafion chain with equivalent content of 1150 g/mol and six side chains was used. The Nafion chains were coated over the Pt-supported KB model. The Pt-supported KB structure over which Nafion chains were coated is called catalyst particle (CP) model in this study. Ionomer/carbon ratio are 1.03 and 1.14 for the Pt-supported KB models with 4 and 6 nm pore sizes, respectively. To stabilize the CP structures, molecular dynamics calculations were performed at a temperature of 300 K for 100 ps in the NVT ensemble. In these calculations, there are no fixed parts.

Figure 1.

 Pt-supported KB model with the pore of 6 nm in size terminated with H and OH groups. The right blue box indicates an enlarged view of pores.

3 Results and Discussion

To clarify the effect of the pore size of the KB support on the coverage states of the Nafion chain and water molecules over the Pt nanoparticles, we compared two CP structures with a different pore size of 4 and 6 nm. Figure 2 (a) shows the CP model with pore sizes of 6 nm after MD calculation at 100 ps. We discuss the coverage states of water molecules and Nafion chains over the Pt nanoparticles on the exterior and in the interior of the pore of the KB supports marked by black and blue boxes as shown in Figure 2 (b), respectively. Figure 3 shows the comparison of coverage states of the Nafion chains and water molecules on the exterior and in the interior of the pore of the KB supports with different pore sizes. Here, the ideal coverage states of the Pt nanoparticles in the CL for high electrode reaction activity at the cathode are considered as followings: (i) not full coverage states of the Nafion chains over the Pt nanoparticle to allow smooth diffusion of oxygen molecules to the Pt nanoparticles for oxygen reduction reaction and (ii) a lot of contacts of the Nafion chains with H2O molecules adsorbed on the Pt nanoparticles for proton conduction to the Pt nanoparticles. Figures. 3 (a) and (b) show the coverage states of the Nafion chains over the Pt nanoparticles on the exterior of the pore of 4 and 6 nm in size, respectively. The Pt nanoparticles on both models are fully covered with the Nafion chains, indicating the low oxygen transport property because the oxygen diffusion to the Pt nanoparticles is blocked by the Nafion chains. Figure 3 (c) shows that Pt nanoparticles in the interior of the pore are not covered by the Nafion chains when the pore size is 4 nm, leading to high oxygen transport property. However, the Nafion chains do not connect with the H2O molecules on the Pt nanoparticles, indicating low proton conductivity. In the case of a pore size of 6 nm, Pt nanoparticles are not covered by the Nafion chains and the Nafion chains partially connect with the H2O molecules on the Pt nanoparticles in the interior of the pore (Figure 3 (d)). These results proposed that the coverage state of Pt nanoparticles as shown in Figure 3 (d) has both high electrode reaction activity and high oxygen transport property because protons can be conducted from the Nafion chains to the Pt surface and the oxygen diffusion is not blocked by the Nafion chains. To evaluate the connectivity of the Nafion chains to the H2O molecules on the Pt nanoparticles in the interior of the pore, the number of carbon atoms in the Nafion chains that penetrated the pores of the KB supports with different pore sizes were analyzed (Figure 4). Figure 4 shows that the carbon atoms of the Nafion chains penetrated more in the pore of 6 nm than those in the pore of 4 nm, indicating that the Nafion chains more easily penetrate the pore of 6 nm than that of 4 nm in size. Then, as the pore size increases, more Nafion chains penetrate the interior of the pore and contact with H2O molecules on the Pt nanoparticles.

Figure 2.

 (a) Overall view of the CP model using Pt-supported KB model with the pore of 6 nm in size and (b) cross-sectional view at the position of the red box in Figure 2 (a). Black and blue boxes indicate the Pt nanoparticles on the exterior and in the interior of the pore, respectively.

Figure 3.

 Coverage states of the Nafion chains and water molecules over the Pt nanoparticle on the exterior of the pore of (a) 4 nm and (b) 6 nm in size, and in the interior of the pore of (c) 4 nm and (d) 6 nm in size. In (c) and (d), blue boxes in the upper right Figures are enlarged.

Figure 4.

 Time evolution of the number of carbon atoms in the Nafion chain penetrating the pore when the pore is 4 and 6 nm in size.

Furthermore, to discuss the reason why more Nafion chains penetrate the larger pore, we analyzed the angle distributions of the Nafion chains above the pore of 4 and 6 nm in size. The angle (θ) is defined as the angle between a and b in Figure 5 (a). a   is from the center of the gravity of the Nafion chains to the tip of the Nafion chains and b is from the center of the gravity of the Nafion chains to the center of the KB support. In addition, we subtracted 90° from θ and took the absolute value to evaluate the orientation of the Nafion chains above the pore. The large and small angles indicate the vertical and horizontal orientations of the Nafion chains to the pore, respectively. The angles of the Nafion chains distributed within 2 nm from the KB support surface were evaluated and these were classified into 15 ° (Figure 5 (b)). In the case of the pore of 6 nm in size, the Nafion chain over the angle of 45 ° or more is larger than that of 4 nm in size, indicating the dominant distribution of the vertical Nafion chains. Here, the horizontal Nafion chains block the entrance of the pore and cannot penetrate the pore. Therefore, the larger the pore size is, the more Nafion chains above the pore are vertically distributed toward the pore and can easily penetrate the pore.

Figure 5.

 (a) Definition of the angle of the Nafion chains toward the pore and (b) angle distributions of the Nafion chains toward the pore when the pore is 4 and 6 nm in size.

These results suggest that both high oxygen transport property and high electrode reaction activity are achieved over the Pt nanoparticles in the interior of the large pore of the KB support because the oxygen diffusion in the pore is not blocked by the Nafion chains and the large pore size promotes the formation of a proton conducting path composed of the Nafion chains, H2O, and Pt nanoparticles.

4 Conclusion

To clarify the effect of the pore size of the KB support on the electrode reaction activity of the CL in PEFC, we investigated the coverage states of the Nafion chains and water molecules over the Pt nanoparticles on the KB support with the pore of 4 and 6 nm in size using reactive molecular dynamics method. Regardless of the pore size, the Pt nanoparticles on the exterior of the pore are fully covered with the Nafion chains and the Pt nanoparticles in the interior of the pore are not covered with the Nafion chains. This result suggests that the Pt nanoparticles in the interior of the pore are not blocked by the Nafion chains for oxygen diffusion, indicating high oxygen transport property that does not depend on the pore size. To evaluate the connectivity of the Nafion chains to the H2O molecules on the Pt nanoparticles in the interior of the pore, the number of carbon atoms in the Nafion chains that penetrated the pores of the KB supports with different pore sizes were analyzed. As the pore size increases, more Nafion chains penetrated the interior of the pore and contacted with H2O molecules on the Pt nanoparticles. We also proposed that this is because the Nafion chains above the large pore can vertically distribute toward the pore. Finally, these results propose that both high oxygen transport property and high electrode reaction activity are achieved over the Pt nanoparticles in the interior of the large pore of the KB support because the oxygen diffusion in the pore is not blocked by the Nafion chains and the large pore size promotes the formation of a proton conducting path composed of the Nafion chains, H2O, and Pt nanoparticles.

Acknowledgment

This research was supported by the FC Platform Program (Grant No. JPNP20003): Development of design-for-purpose numerical simulators for attaining long life and high performance project (FY 2020–FY 2022) conducted by the New Energy and Industrial Technology Development Organization (NEDO), Japan. We acknowledge Center for Computational Materials Science, Institute for Materials Research, Tohoku University for the use of supercomputing system MASAMUNE-IMR (202012-SCKXX-0502).

Reference
 
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