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18 TH INTERNATIONAL CONFERENCE ON COMPOSITE MATERIALS MULTI-SCALE MODLING AND OPTIMIZATION OF STRUCTURALLY INTEGRATED LITHIUM-ION BATTERIES S. Golmon 1 , C. DeLuca 1 , M. Dunn 2 , and K. Maute 1,2 * 1 Department of Aerospace Engineering Sciences,


  1. 18 TH INTERNATIONAL CONFERENCE ON COMPOSITE MATERIALS MULTI-SCALE MODLING AND OPTIMIZATION OF STRUCTURALLY INTEGRATED LITHIUM-ION BATTERIES S. Golmon 1 , C. DeLuca 1 , M. Dunn 2 , and K. Maute 1,2 * 1 Department of Aerospace Engineering Sciences, University of Colorado, Boulder, USA 2 Department of Mechanical Engineering, University of Colorado, Boulder, USA * Corresponding author(maute@colorado.edu) Keywords : Multi-scale Model, Electrochemistry, Stress-Diffusion Coupling, Homogenization, Finite Elements, Design Optimization, Adjoint Sensitivity Analysis (Li) in the anode is oxidized into Li + and electrons. 1 Introduction Batteries play an increasingly important role for a The electrons flow through the external circuit to the broad range of technologies. Applications range cathode while the ions enter the electrolyte and are from powering small wireless sensors and smart carried by diffusion and migration to the cathode, phones to storing larger amount of energy for where they are reduced. This process is reversed electric cars and providing buffers for wind farms when the battery is charged. In Li + batteries, the electrodes are composed of and photovoltaic plants. There is a growing demand for more reliable, higher energy density, longer porous active insertion compounds, binders, and lifetime, batteries. Conventionally, batteries are conductive additives, with a solid or gel-like (liquid) designed to provide a single function: to store electrolyte filling the pores. The active material particles swell upon Li + intercalation. Depending on energy. The battery cell is shielded from mechanical loads by enclosure in a stiff containment and the the material, this swelling can range from 6.5% for integration of batteries into structural components, Mn 2 O 4 cathode material to 300% to 400% for Si subsystems, and devices is mainly driven by thermal anode materials and leads to stresses in both the management requirements. However, for a broad active material particle as well as the entire battery range of applications, such as aircraft and cars, a cell. The stresses can lead to cracking of the multi-functional battery design with load-bearing electrode particles which may cause parts of the capabilities is a promising concept to reduce the cracked particles to be electrically and ionically weight and increase the payload capacity of the isolated and thus may lead to capacity fade. overall system [1] . Two distinct length scales can be identified at which In this paper we are concerned with modeling and phenomena relevant for the electrochemical and designing multi-functional batteries, focusing on the mechanical performance of a battery cell occur. The fundamental interactions between electrochemical transport of ions and electrons across the electrodes and structural performance of Lithium ion (Li + ) and separator are macroscopic, likewise the batteries. This class of batteries features among the mechanical deformation of the battery cell. The highest theoretical energy storage density, but is plagued with significantly shorter lifetimes when A compared to other battery chemistries. The performance and degradation of Li + batteries strongly depend on both electrochemical and e e Li + mechanical phenomena which are strongly coupled. Li + e e In particular these coupling phenomena need to be considered when integrating Li + batteries into Li + e Li + e structural composites. Li + e e Rechargeable batteries consist of anodic and cathodic electrodes and current collectors, as shown anode separator cathode in Fig. 1. A separator prevents contact of the Figure 1: Battery cell. electrodes. When the battery is discharged, lithium

  2. µ characteristic length scale is at the order of 100 m . the size of the particle decreases. Surface stress effects need to be considered when optimizing the The macroscopic phenomena are strongly size of electrode particles in order to avoid non- interconnected with the response of a single active physical solutions for particle sizes at the order of material particle. Micro-scale phenomena include nano-meters. Meso-scale homogenization methods the transport of Li across the particle surface and are used to account for the interactions between the within the particle as well as its mechanical particles and bridge macro and micro scales. We deformation. The characteristic microscopic length model macro- and micro-scale phenomena using a scale depends on the particle size and ranges from a multi-scale finite element approach which is few nano meters up to ~10 m µ . described in detail in Golmon et al. [5]. In this paper we present a multi-scale modeling and analysis approach for predicting the behavior of 3 Design optimization framework structurally integrated batteries. We embed this Improved performance of the battery can be approach into a design optimization framework to achieved by altering the design and discharge study the optimal layout of electrodes. The parameters of the battery. Manipulation of macro- optimization studies allow assessing the trade-off scale parameters such as the discharge rate, between mechanical and electro-chemical electrode thickness, and porosity, as well as micro- performance. scale parameters such as the size and shape of the 2 Multi-scale modeling particles in the electrode can affect the overall behavior of the battery and the level of the internal The behavior of Li + batteries is an interesting multi- stresses. Because the battery problem involves scale, multi-physics problem involving nonlinear multiple length scales and the interaction of transient transient coupled electrochemical and mechanical multi-physics phenomena, designing by intuition is phenomena at macro and micro scales. Owing to the difficult. Therefore we have developed a wide range of characteristic lengths at which these computational design optimization approach which − 9 − 4 phenomena occur (10 − 10 m ) directly resolving combines the multi-scale finite element battery cell all length scales leads to an impractically large model described above with mathematical computational burden. Instead, we use a multi-scale optimization schemes to drive the cell design [6]. modeling approach [2] and assume a separation of Much of the previous work on optimization of length scales between macro and micro scales. For batteries has focused on battery pack design, the class of problems considered in this study, a considering thermal and power management [7,8]. separation of time scales is not necessary as Li To enhance the battery performance at the cell level, transport occur at similar paces at both the macro- Battery cell design was considered for example in and micro-scale. [9,10,11]. All of the above design studies rely Our approach extends the electrochemical battery primarily on intuition, experience, and parameter model developed by Doyle et al. [3]which uses sweeps but do not employ a formal design porous electrode theory to account for micro-scale optimization approach, capable of handling large effects. At the macro-scale, Li + transport, electric numbers of constraints and design variables. potentials, and mechanical deformations across the In this study we apply a computational framework entire battery cell are considered. We extend this for optimizing the transient, nonlinear behavior of macro-scale model to account for elastic and structurally integrated batteries in order to improve inelastic deformations due to external mechanical the electrochemical and mechanical performance by loads and electrochemical eigenstrains. At the manipulating a potentially large number of micro-scale, the response of a single electrode macroscopic and microscopic design parameters [6]. particle is considered. Here we adopt the coupled In the following we demonstrate the capabilities of stress-diffusion model of Zhang et al. [4], account our optimization framework to find the optimal for electrochemical surface reactions, and include porosity and particle size distributions in surface stress effects. As we will show later, functionally graded electrodes. This design classical continuum mechanical models suggest that optimization problem is solved by a nonlinear particle stresses due to Li intercalation decrease as programming method. This method requires the

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