多相多孔电极理论

Raymond B. Smith, M. Bazant
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引用次数: 127

摘要

由John Newman及其合作者开创的多孔电极理论,基于微观物理模型而不是经验电路近似,为电池循环行为提供了有用的宏观描述。该理论依赖于长度尺度的分离来描述电极中耦合到小活性物质颗粒内嵌入的传输。通常,活性材料被描述为固溶体颗粒,具有由浓度场驱动的输运和表面反应,并通过拟合开路电位纳入热力学。然而,这种方法具有基本的局限性,并且不适用于相分离材料,因为即使在平衡状态下,电压也是非均匀浓度曲线的一个紧急属性。在这里,我们提出了一个基于电化学非平衡热力学的“多相多孔电极理论”的通用理论框架,该框架由一个名为“MPET”的开源软件包实现。采用cahn - hilliard型相场模型对固体活性材料进行了描述,并给出了相应的界面反应动力学广义模型。在电解质相上实现了经典的浓溶液理论,在固溶活性材料的极限下用Butler-Volmer动力学恢复了Newman的多孔电极理论。更一般的,法拉第反应的量子力学模型也包括在内,如金属电极上电子转移的马库斯-赫什-奇德赛动力学,扩展到浓溶液。描述了完整的方程和数值算法,并给出了各种实例计算,以说明该软件与现有电池模型相比的新特性。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
Multiphase Porous Electrode Theory
Porous electrode theory, pioneered by John Newman and collaborators, provides a useful macroscopic description of battery cycling behavior, rooted in microscopic physical models rather than empirical circuit approximations. The theory relies on a separation of length scales to describe transport in the electrode coupled to intercalation within small active material particles. Typically, the active materials are described as solid solution particles with transport and surface reactions driven by concentration fields, and the thermodynamics are incorporated through fitting of the open circuit potential. This approach has fundamental limitations, however, and does not apply to phase-separating materials, for which the voltage is an emergent property of inhomogeneous concentration profiles, even in equilibrium. Here, we present a general theoretical framework for "multiphase porous electrode theory" implemented in an open-source software package called "MPET", based on electrochemical nonequilibrium thermodynamics. Cahn-Hilliard-type phase field models are used to describe the solid active materials with suitably generalized models of interfacial reaction kinetics. Classical concentrated solution theory is implemented for the electrolyte phase, and Newman's porous electrode theory is recovered in the limit of solid-solution active materials with Butler-Volmer kinetics. More general, quantum-mechanical models of Faradaic reactions are also included, such as Marcus-Hush-Chidsey kinetics for electron transfer at metal electrodes, extended for concentrated solutions. The full equations and numerical algorithms are described, and a variety of example calculations are presented to illustrate the novel features of the software compared to existing battery models.
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