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Electrochemical Properties of Porous Metals Manufactured by Lost Carbonate Sintering

机译:失碳酸盐烧结制备多孔金属的电化学性能

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摘要

Porous metals have recently attracted much attention in both academia and industry. They have many potential applications ranging from light weight structure, thermal management and sound absorption, because of their unique structural, mechanical, thermal and acoustic properties. Open-cell porous metal can be an ideal material for electrochemical applications due to its high surface area, permeability and electric conductivity. The electro-active surface area of porous electrodes is the most important factor in electrochemical applications, such as fuel cells, because it largely determines the current density in the electrode. However, most research to date on the surface area of porous metals has been focused on the geometric and real surface areas. Very little research has been conducted to study the electro-active surface area. The mass transfer coefficient of a solid electrode is a very important factor in flow cell applications, such as flow battery and wastewater treatment, because high mass transfer coefficient means high reaction performance. However, very little research has been carried out on the mass transfer coefficient of open-cell porous metal manufactured by the space-holder method. The main objective of this study is to investigate the electrochemically relevant structural properties of porous Cu and Ni fabricated by the Lost Carbonate Sintering (LCS) process, which is a cost-effective process for manufacturing open-cell porous metals with controlled porosity, pore size and pore shape. In this project, the geometric, electro-active and real surface areas of porous Cu and Ni have been measured by quantitative stereology, cyclic voltammetry (peak current) and cyclic voltammetry (double layer capacitance) methods, respectively. The mass transfer coefficient of porous Ni has been measured by linear sweep voltammetry, using a purpose-built flow cell. The tortuosity of porous Cu has been measured by a diffusion method, using a purpose-built diaphragm cell. The geometric, electro-active and real surface areas of porous metal are due to the contributions from the primary porosity, the primary and secondary porosities, and the surfaces of metal particles, respectively. The geometric, electro-active and real surface areas of porous Cu and Ni samples with pore sizes 75-1500 µm and porosities 0.53-0.81 were in the ranges of 18-110 cm-1, 24-369 cm-1 and 700-1200 cm-1, respectively. Both the geometric and electro-active surface area increased with porosity and decreased with pore size. The real surface area decreased with porosity but the effect of pore size was not pronounced. The values of electro-active surface area of LCS porous metal can be similar to and often greater than those of the existing porous metals, e.g. incofoam Ni. The mass transfer coefficient of porous Ni with pore sizes 250-1500 µm and porosities 0.63-0.81 at different flow rates from 0.24 ml/s to 2.8 ml/s was in the range of 0.0035-0.0727 cm/s. Both the limiting current and mass transfer coefficient increased with flow rate and had the maximum values at a porosity of around 0.65-0.70. The maximum limiting current decreased and the maximum mass transfer coefficient increased with pore size. Compared with a smooth Ni plate at the same flow velocity, the mass transfer coefficient of the LCS porous Ni was increased by up to 9 times. The enhancement is due to the Ni particles providing a rough surface for the cell walls and the tortuous pore structure resulting in a high level of fluid turbulence. The tortuosity of the porous Cu samples, with pore sizes 250-1500 µm and porosities 0.56-0.84, was in the range of 1.33-1.78. It increased with pore size and decreased with porosity, agreeing with an empirical formula for porous media. This research has successfully applied cyclic voltammetry to the measurement of electro-active surface area of porous metals for the first time. It is the first systematic study of the structural properties of relevance to electrochemical applications of porous metals manufactured by LCS process.
机译:多孔金属最近在学术界和工业界都引起了很多关注。由于它们独特的结构,机械,热和声学特性,它们在轻质结构,热管理和吸声方面具有许多潜在的应用。开孔多孔金属由于其高的表面积,渗透性和导电性而可以是用于电化学应用的理想材料。多孔电极的电活性表面积是电化学应用(例如燃料电池)中最重要的因素,因为它在很大程度上决定了电极中的电流密度。但是,迄今为止,大多数有关多孔金属表面积的研究都集中在几何和实际表面积上。很少进行研究以研究电活性表面积。固体电极的传质系数是流通池应用(例如液流电池和废水处理)中非常重要的因素,因为高传质系数意味着高反应性能。然而,关于通过空间保持器方法制造的开孔多孔金属的传质系数的研究很少。这项研究的主要目的是研究通过失碳酸盐烧结(LCS)工艺制备的多孔铜和镍的电化学相关结构性能,这是一种经济有效的方法,用于制造孔隙率,孔径可控的开孔多孔金属和孔的形状。在该项目中,分别通过定量立体学,循环伏安法(峰值电流)和循环伏安法(双层电容)方法测量了多孔Cu和Ni的几何,电活性和实际表面积。多孔镍的传质系数已使用专用流通池通过线性扫描伏安法进行了测量。多孔Cu的曲折度已经通过使用专用隔膜电池的扩散法进行了测量。多孔金属的几何,电活性和实际表面积分别是由于主要孔隙率,主要和次要孔隙率以及金属颗粒表面的贡献所致。孔径为75-1500 µm,孔隙率为0.53-0.81的多孔Cu和Ni样品的几何,电活性和实际表面积在18-110 cm-1、24-369 cm-1和700-1200范围内cm-1。几何表面积和电活性表面积均随孔隙率增加而随孔径减小。实际表面积随孔隙率而减小,但是孔径的影响并不明显。 LCS多孔金属的电活性表面积的值可以类似于并且通常大于现有的多孔金属的电活性表面积例如。镍泡沫镍在0.24ml / s至2.8ml / s的不同流速下,孔径为250-1500μm且孔隙率为0.63-0.81的多孔Ni的传质系数在0.0035-0.0727cm / s的范围内。极限电流和传质系数都随着流速的增加而增加,并且在孔隙率约为0.65-0.70时具有最大值。随着孔尺寸的增加,最大极限电流减小,最大传质系数增大。与相同流速下的光滑镍板相比,LCS多孔镍的传质系数提高了9倍。增强是由于镍颗粒为细胞壁提供了粗糙的表面,并且曲折的孔结构导致了高水平的流体湍流。孔径为250-1500 µm,孔隙率为0.56-0.84的多孔Cu样品的曲折度为1.33-1.78。它随孔径增大而随孔隙率减小,与多孔介质的经验公式一致。这项研究已成功地将循环伏安法首次应用于多孔金属电活性表面积的测量。这是对与通过LCS工艺制造的多孔金属的电化学应用相关的结构性质的首次系统研究。

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    Diao K;

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