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    Design of Rapid Fixed‐Bed Adsorption Tests for Nonconstant Diffusivities

    Source: Journal of Environmental Engineering:;1987:;Volume ( 113 ):;issue: 002
    Author:
    John C. Crittenden
    ,
    John K. Berrigan
    ,
    David W. Hand
    ,
    Ben Lykins
    DOI: 10.1061/(ASCE)0733-9372(1987)113:2(243)
    Publisher: American Society of Civil Engineers
    Abstract: A rapid small‐scale column test (RSSCT) that uses a smaller adsorbent particle is used to simulate a five‐month pilot plant adsorption study in several days. The RSSCT is a small‐scale physical model of a full‐scale fixed‐bed such that it gives a performance identical to the full‐scale plant when the effluent profiles are plotted as the bed volumes are fed. A mathematical model that, includes axial dispersion, intraparticle pore and surface diffusion, and liquid‐phase mass transfer resistance is used to scale down the RSSCT from the pilot plant operation without extensive isotherm and kinetic data. This study presents evidence that the surface diffusivities are not necessarily constant with adsorbent particle radius and presents general scaling equations for use under these conditions.
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      Design of Rapid Fixed‐Bed Adsorption Tests for Nonconstant Diffusivities

    URI
    http://yetl.yabesh.ir/yetl1/handle/yetl/34287
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    • Journal of Environmental Engineering

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    contributor authorJohn C. Crittenden
    contributor authorJohn K. Berrigan
    contributor authorDavid W. Hand
    contributor authorBen Lykins
    date accessioned2017-05-08T20:59:02Z
    date available2017-05-08T20:59:02Z
    date copyrightApril 1987
    date issued1987
    identifier other%28asce%290733-9372%281987%29113%3A2%28243%29.pdf
    identifier urihttp://yetl.yabesh.ir/yetl/handle/yetl/34287
    description abstractA rapid small‐scale column test (RSSCT) that uses a smaller adsorbent particle is used to simulate a five‐month pilot plant adsorption study in several days. The RSSCT is a small‐scale physical model of a full‐scale fixed‐bed such that it gives a performance identical to the full‐scale plant when the effluent profiles are plotted as the bed volumes are fed. A mathematical model that, includes axial dispersion, intraparticle pore and surface diffusion, and liquid‐phase mass transfer resistance is used to scale down the RSSCT from the pilot plant operation without extensive isotherm and kinetic data. This study presents evidence that the surface diffusivities are not necessarily constant with adsorbent particle radius and presents general scaling equations for use under these conditions.
    publisherAmerican Society of Civil Engineers
    titleDesign of Rapid Fixed‐Bed Adsorption Tests for Nonconstant Diffusivities
    typeJournal Paper
    journal volume113
    journal issue2
    journal titleJournal of Environmental Engineering
    identifier doi10.1061/(ASCE)0733-9372(1987)113:2(243)
    treeJournal of Environmental Engineering:;1987:;Volume ( 113 ):;issue: 002
    contenttypeFulltext
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