Abstract:Note: Determination of effective gas diffusion coefficients of stainless steel films with differently shaped holes using a Loschmidt diffusion cell Astrath, N. G. C.; Shen, J.; Astrath, F. B. G.; Zhou, J.; Huang, C.; Yuan, X. Z.; Wang, H.; Navessin, T.; Liu, Z. S.; Vlajnic, G.; Bessarabov, D.; Zhao, X.Note: Determination of effective gas diffusion coefficients of stainless steel films with differently shaped holes using a Loschmidt diffusion cell In this work, an in-house made Loschmidt diffusion cell is used … Show more
“…Using a Loschmidt cell, bulk binary diffusion coefficients of O 2 -N 2 were precisely measured under the experimental conditions of different temperatures (25-80 • C) and relative humidity values (0-80%) [18]; the EGDCs of gas diffusion layers of PEM fuel cells were also studied at different temperatures [11]. Moreover, the measured EGDC of a porous sample of a stainless steel film with simple straight pores was found to be in good agreement with the result of numerical computation of threedimensional mass diffusion through the sample [19], exhibiting the usefulness of the Loschmidt cell in studying porous material.…”
Section: Introductionsupporting
confidence: 60%
“…Zhang et al [9] used a Wicke-Kallenbach diffusion cell to measure the EGDC of a catalyst monolith washcoat. A closedtube method with a Loschmidt diffusion cell is considered as one of the most reliable methods to determine binary diffusion coefficients of gases [16][17][18][19]. Using a Loschmidt cell, bulk binary diffusion coefficients of O 2 -N 2 were precisely measured under the experimental conditions of different temperatures (25-80 • C) and relative humidity values (0-80%) [18]; the EGDCs of gas diffusion layers of PEM fuel cells were also studied at different temperatures [11].…”
This article appeared in a journal published by Elsevier. The attached copy is furnished to the author for internal non-commercial research and education use, including for instruction at the authors institution and sharing with colleagues.Other uses, including reproduction and distribution, or selling or licensing copies, or posting to personal, institutional or third party websites are prohibited. In this work, using an in-house made Loschmidt diffusion cell, we measure the effective coefficient of dry gas (O 2 -N 2 ) diffusion in cathode catalyst layers of PEM fuel cells at 25 • C and 1 atmosphere. The thicknesses of the catalyst layers under investigation are from 6 to 29 m. Each catalyst layer is deposited on an Al 2 O 3 membrane substrate by an automated spray coater. Diffusion signal processing procedure is developed to deduce the effective diffusion coefficient, which is found to be (1.47 ± 0.05) × 10 −7 m 2 s −1 for the catalyst layers. Porosity and pore size distribution of the catalyst layers are also measured using Hg porosimetry. The diffusion resistance of the interface between the catalyst layer and the substrate is found to be negligible. The experimental results show that the O 2 -N 2 diffusion in the catalyst layers is dominated by the Knudsen effect. Crown
“…Using a Loschmidt cell, bulk binary diffusion coefficients of O 2 -N 2 were precisely measured under the experimental conditions of different temperatures (25-80 • C) and relative humidity values (0-80%) [18]; the EGDCs of gas diffusion layers of PEM fuel cells were also studied at different temperatures [11]. Moreover, the measured EGDC of a porous sample of a stainless steel film with simple straight pores was found to be in good agreement with the result of numerical computation of threedimensional mass diffusion through the sample [19], exhibiting the usefulness of the Loschmidt cell in studying porous material.…”
Section: Introductionsupporting
confidence: 60%
“…Zhang et al [9] used a Wicke-Kallenbach diffusion cell to measure the EGDC of a catalyst monolith washcoat. A closedtube method with a Loschmidt diffusion cell is considered as one of the most reliable methods to determine binary diffusion coefficients of gases [16][17][18][19]. Using a Loschmidt cell, bulk binary diffusion coefficients of O 2 -N 2 were precisely measured under the experimental conditions of different temperatures (25-80 • C) and relative humidity values (0-80%) [18]; the EGDCs of gas diffusion layers of PEM fuel cells were also studied at different temperatures [11].…”
This article appeared in a journal published by Elsevier. The attached copy is furnished to the author for internal non-commercial research and education use, including for instruction at the authors institution and sharing with colleagues.Other uses, including reproduction and distribution, or selling or licensing copies, or posting to personal, institutional or third party websites are prohibited. In this work, using an in-house made Loschmidt diffusion cell, we measure the effective coefficient of dry gas (O 2 -N 2 ) diffusion in cathode catalyst layers of PEM fuel cells at 25 • C and 1 atmosphere. The thicknesses of the catalyst layers under investigation are from 6 to 29 m. Each catalyst layer is deposited on an Al 2 O 3 membrane substrate by an automated spray coater. Diffusion signal processing procedure is developed to deduce the effective diffusion coefficient, which is found to be (1.47 ± 0.05) × 10 −7 m 2 s −1 for the catalyst layers. Porosity and pore size distribution of the catalyst layers are also measured using Hg porosimetry. The diffusion resistance of the interface between the catalyst layer and the substrate is found to be negligible. The experimental results show that the O 2 -N 2 diffusion in the catalyst layers is dominated by the Knudsen effect. Crown
“…produces an equivalent diffusion coefficient, , that represents the heterogeneous diffusion through the bulk gas and the sample. Following the procedure used in previous studies, the resistance network method may be applied between the oxygen probe (3) and sliding gate interface (5) in Figure in order to solve for the effective diffusion coefficient of the porous sample. The equivalent diffusive resistance, R eq , is the sum of the diffusive resistance through the binary gas, R binary , and the sample, R eff …”
Section: Discussionmentioning
confidence: 99%
“…or, where l is the thickness of the porous sample. The validity of solving for R eff with the resistance network method has not been discussed in previous studies . Dong et al demonstrates that the method is only accurate within a specific range of Fourier numbers where t is the characteristic time, or the length of time the experiment is run for (see Figure ).…”
Section: Discussionmentioning
confidence: 99%
“…The Loschmidt cell must be modified to measure gas diffusion through porous media by allowing a sample to be placed near the midpoint of the long tube. A schematic of the apparatus used in this study is provided in Figure , whose design is an evolution of the modified Loschmidt cell in literature . Different gas species are contained in the upper and lower chambers of the cell separated by a sliding gate (5a), in this study nitrogen and oxygen, respectively.…”
Gas diffusion through porous media is critical for the high current density operation of a polymer electrolyte membrane fuel cell, where the electrochemical reaction becomes rate limited by the diffusive flux of reactants. Precise knowledge of the diffusivity through various components in a fuel cell is necessary for accurate modeling and analysis. However, many experimental measurements of diffusivity in literature have high measurement uncertainty. In this study, an improvement to the accuracy of the Loschmidt cell method is presented for measuring the diffusivity through materials with a submillimeter thickness. The diffusivity through various gas diffusion layers (GDLs) is measured, and the relative differences between GDLs are explained using scanning electron microscopy and the method of standard porosimetry. The experimental results from this study and others in current literature are used to develop a generalized correlation for the diffusibility as a function of porosity in the through-plane direction of GDLs.
The in-plane effective diffusion coefficients in gas diffusion layers typically usedin fuel cell electrodes were measured as a function of compression and hydrophobic polymerloading. This method was based on the transient diffusion of oxygen from air into an initiallynitrogen purged porous sample and has proven to be accurate, fast, and straightforward.As anticipated, with higher compressions and higher PTFE loadings, effective diffusivitydecreased, as a result of less pore space available for transport and because tortuosityincreased. When plotted against compressed porosity, the effective diffusivity of untreatedand treated materials for a given type of sample collapsed on top of each other, despitethe simultaneous impact of PTFE loading and compression. [...
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