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    Kinetics of Adsorption on Activated Carbon: III. Natural Organic Material

    Source: Journal of Environmental Engineering:;1987:;Volume ( 113 ):;issue: 004
    Author:
    Joachim Fettig
    ,
    Heinrich Sontheimer
    DOI: 10.1061/(ASCE)0733-9372(1987)113:4(795)
    Publisher: American Society of Civil Engineers
    Abstract: Adsorption kinetics of a fulvic acid (FA) were investigated in detail. Based on experimental equilibrum data, the mixture was subdivided into two pseudocomponents with different adsorbabilities and one nonadsorbable fraction. Thus the impact of the initial concentration on the overall isotherm could be described well. However, equilibrium data of the FA after preadsorption were poorly predicted. Minicolumn experiments allowed for the determination of external mass transfer coefficients of the adsorbable pseudocomponents. The results also yielded an estimation of the effective diffusivity and the average molecular size of the FA in the bulk liquid phase. Intraparticle diffusivities were evaluated from batch kinetic experiments. The overall concentration change with time was well described by the film‐homogeneous diffusion model, while the behavior of the pseudocomponents could be described more closely by the filmheterogeneous diffusion model. The applicability of the models to predict a minicolumn breakthrough curve is discussed.
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      Kinetics of Adsorption on Activated Carbon: III. Natural Organic Material

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    https://yetl.yabesh.ir/yetl1/handle/yetl/34820
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    contributor authorJoachim Fettig
    contributor authorHeinrich Sontheimer
    date accessioned2017-05-08T20:59:52Z
    date available2017-05-08T20:59:52Z
    date copyrightAugust 1987
    date issued1987
    identifier other%28asce%290733-9372%281987%29113%3A4%28795%29.pdf
    identifier urihttp://yetl.yabesh.ir/yetl/handle/yetl/34820
    description abstractAdsorption kinetics of a fulvic acid (FA) were investigated in detail. Based on experimental equilibrum data, the mixture was subdivided into two pseudocomponents with different adsorbabilities and one nonadsorbable fraction. Thus the impact of the initial concentration on the overall isotherm could be described well. However, equilibrium data of the FA after preadsorption were poorly predicted. Minicolumn experiments allowed for the determination of external mass transfer coefficients of the adsorbable pseudocomponents. The results also yielded an estimation of the effective diffusivity and the average molecular size of the FA in the bulk liquid phase. Intraparticle diffusivities were evaluated from batch kinetic experiments. The overall concentration change with time was well described by the film‐homogeneous diffusion model, while the behavior of the pseudocomponents could be described more closely by the filmheterogeneous diffusion model. The applicability of the models to predict a minicolumn breakthrough curve is discussed.
    publisherAmerican Society of Civil Engineers
    titleKinetics of Adsorption on Activated Carbon: III. Natural Organic Material
    typeJournal Paper
    journal volume113
    journal issue4
    journal titleJournal of Environmental Engineering
    identifier doi10.1061/(ASCE)0733-9372(1987)113:4(795)
    treeJournal of Environmental Engineering:;1987:;Volume ( 113 ):;issue: 004
    contenttypeFulltext
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