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   <dc:title>Modeling of Electrodialytic Treatment of Lithium-Ion Batteries</dc:title>
   <dc:creator>Paz-García, Juan Manuel</dc:creator>
   <dc:creator>Villén-Guzmán, María Dolores</dc:creator>
   <dc:creator>Cerrillo-González, María del Mar</dc:creator>
   <dc:creator>Gómez-Lahoz, César</dc:creator>
   <dc:creator>Vereda-Alonso, Carlos</dc:creator>
   <dc:creator>García-Delgado, Rafael Antonio</dc:creator>
   <dc:creator>García-Herruzo, Francisco</dc:creator>
   <dc:creator>Rodríguez-Maroto, José Miguel</dc:creator>
   <dc:subject>Pilas de litio</dc:subject>
   <dcterms:abstract>Lithium-ion batteries are currently present in most portable electronic devices and their use is rapidly growing in the field of electric vehicles and renewable energy storage. Many components in lithium-ion batteries are toxic and/or environmentally hazardous. Furthermore, some of them are expensive and listed as critical materials in terms of supply-chain risk. Therefore, the need to improve the recycling techniques for lithium-ion batteries is becoming a priority.&#xd;
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Herein, we describe and present a model for the electrodialytic treatment of disposed lithium-ion batteries. Electrodialysis is a separation process based on the use of electric fields and ion-selective membranes. The electrodialytic cell can be designed in different configurations, to enhance the selective extraction of the target products. In a standard electrodialytic cell, the treated matrix is separated from the anode and the cathode compartments by means of anion- and cation-exchange membranes respectively. However, depending on the ionic charge and the specific chemistry of the matrix, different cell designs can be used. &#xd;
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In the present work, different possible configurations are explored for the optimization of the extraction of key valuable components from spent lithium-ion batteries, taking into account the chemical properties of the system depending on the chosen extracting agent and cell configuration. The model presented here is based on a set of differential and algebraic equations consisting of a Nernst-Planck based continuity equations for each of the chemical species involved in the process, coupled with the electroneutrality and the local chemical equilibrium conditions. &#xd;
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The numerical solution is performed using COMSOL Multiphysics, and the simulation results are compared with experimental data for model validation.</dcterms:abstract>
   <dcterms:dateAccepted>2019-02-08T10:25:09Z</dcterms:dateAccepted>
   <dcterms:available>2019-02-08T10:25:09Z</dcterms:available>
   <dcterms:created>2019-02-08T10:25:09Z</dcterms:created>
   <dcterms:issued>2019-02-08</dcterms:issued>
   <dc:type>conference output</dc:type>
   <dc:identifier>https://hdl.handle.net/10630/17273</dc:identifier>
   <dc:language>eng</dc:language>
   <dc:relation>25th Topical Meeting of the International Society of Electrochemistry - New electrochemical processes for energy and the environment</dc:relation>
   <dc:relation>Toledo</dc:relation>
   <dc:relation>mayo de 2019</dc:relation>
   <dc:rights>open access</dc:rights>
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