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    A Modeling Study of Discharging Li-O2 Batteries With Various Electrolyte Concentrations

    Source: Journal of Electrochemical Energy Conversion and Storage:;2020:;volume( 018 ):;issue: 001
    Author:
    Wang, Fangzhou
    ,
    Li, Xianglin
    ,
    Hao, Xiaowen
    ,
    Tan, Jianyu
    DOI: 10.1115/1.4046931
    Publisher: The American Society of Mechanical Engineers (ASME)
    Abstract: The mass transfer in the cathode electrode plays an important role in operating Li-O2 batteries. In this study, a two-dimensional, transient, and isothermal model is developed to investigate the mass transfer in discharging Li-O2 batteries. This model simulates the discharge performance of Li-O2 batteries with various electrolyte concentrations (0.1−1.0M) at various current densities (0.1, 0.3, and 0.5 mA/cm2). The O2 diffusivity and the ionic conductivity and diffusivity of Li+ are altered as the bis(trifluoromethane)sulfonimide lithium salt (LiTFSI) concentration in the electrolyte of tetraethylene glycol dimethyl ether (TEGDME) changes. The distributions of O2, Li+, and lithium peroxide (Li2O2) in the cathode electrode after discharge are calculated using this model. Modeling results show that when the concentration decreases from 0.5 to 0.25M, the discharge capacity of Li-O2 sharply drops at various current densities. The mass transfer of Li+ determines the discharge capacity of Li-O2 batteries with dilute electrolytes (≤0.25 M). In contrast, the O2 supply is dominant regarding the discharge capacity when the electrolyte concentration is larger than 0.5M. The highest discharge capacity (e.g., 6.09 mAh at 0.1 mA/cm2) is achieved using 0.5M electrolyte since it balances mass transfer of O2 and Li+.
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      A Modeling Study of Discharging Li-O2 Batteries With Various Electrolyte Concentrations

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    http://yetl.yabesh.ir/yetl1/handle/yetl/4274162
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    contributor authorWang, Fangzhou
    contributor authorLi, Xianglin
    contributor authorHao, Xiaowen
    contributor authorTan, Jianyu
    date accessioned2022-02-04T14:41:05Z
    date available2022-02-04T14:41:05Z
    date copyright2020/05/11/
    date issued2020
    identifier issn2381-6872
    identifier otherjeecs_18_1_011009.pdf
    identifier urihttp://yetl.yabesh.ir/yetl1/handle/yetl/4274162
    description abstractThe mass transfer in the cathode electrode plays an important role in operating Li-O2 batteries. In this study, a two-dimensional, transient, and isothermal model is developed to investigate the mass transfer in discharging Li-O2 batteries. This model simulates the discharge performance of Li-O2 batteries with various electrolyte concentrations (0.1−1.0M) at various current densities (0.1, 0.3, and 0.5 mA/cm2). The O2 diffusivity and the ionic conductivity and diffusivity of Li+ are altered as the bis(trifluoromethane)sulfonimide lithium salt (LiTFSI) concentration in the electrolyte of tetraethylene glycol dimethyl ether (TEGDME) changes. The distributions of O2, Li+, and lithium peroxide (Li2O2) in the cathode electrode after discharge are calculated using this model. Modeling results show that when the concentration decreases from 0.5 to 0.25M, the discharge capacity of Li-O2 sharply drops at various current densities. The mass transfer of Li+ determines the discharge capacity of Li-O2 batteries with dilute electrolytes (≤0.25 M). In contrast, the O2 supply is dominant regarding the discharge capacity when the electrolyte concentration is larger than 0.5M. The highest discharge capacity (e.g., 6.09 mAh at 0.1 mA/cm2) is achieved using 0.5M electrolyte since it balances mass transfer of O2 and Li+.
    publisherThe American Society of Mechanical Engineers (ASME)
    titleA Modeling Study of Discharging Li-O2 Batteries With Various Electrolyte Concentrations
    typeJournal Paper
    journal volume18
    journal issue1
    journal titleJournal of Electrochemical Energy Conversion and Storage
    identifier doi10.1115/1.4046931
    page11009
    treeJournal of Electrochemical Energy Conversion and Storage:;2020:;volume( 018 ):;issue: 001
    contenttypeFulltext
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    DSpace software copyright © 2002-2015  DuraSpace
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