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    Effects of Oxidant on Thermal Regeneration of Granular Activated Carbon

    Source: Journal of Environmental Engineering:;1994:;Volume ( 120 ):;issue: 001
    Author:
    Mark A. Waer
    ,
    Vernon L. Snoeyink
    DOI: 10.1061/(ASCE)0733-9372(1994)120:1(190)
    Publisher: American Society of Civil Engineers
    Abstract: The effect of oxidant type and flow rate were evaluated in a bench scale study using granular activated carbon (GAC) that had been loaded in a drinking water‐treatment plant and in the laboratory. The rate of regeneration of the GAC was found to be controlled by the rate of steam flow per unit GAC mass. The rate of regeneration increases with increasing steam flow in the range of steam flow rates used for commercial regeneration. At higher steam flow rates, the rate of reaction reaches a plateau value and is insensitive to changes in steam flow rate. Carbon dioxide has little, if any, effect on regeneration. Changing the inert gas flow rate used for fluidization of the GAC had no effect on the rate of regeneration at a fixed oxidant flow rate, even though it affected the oxidant partial pressure. Subbituminous GAC required higher temperatures than lignite GAC to regenerate to a specific apparent density in a fixed time period. Diffusion was not found to control the rate of regeneration. Different types of adsorbates used in a variety of studies were found to form chars of similar reactivity.
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      Effects of Oxidant on Thermal Regeneration of Granular Activated Carbon

    URI
    http://yetl.yabesh.ir/yetl1/handle/yetl/42031
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    • Journal of Environmental Engineering

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    contributor authorMark A. Waer
    contributor authorVernon L. Snoeyink
    date accessioned2017-05-08T21:11:16Z
    date available2017-05-08T21:11:16Z
    date copyrightJanuary 1994
    date issued1994
    identifier other%28asce%290733-9372%281994%29120%3A1%28190%29.pdf
    identifier urihttp://yetl.yabesh.ir/yetl/handle/yetl/42031
    description abstractThe effect of oxidant type and flow rate were evaluated in a bench scale study using granular activated carbon (GAC) that had been loaded in a drinking water‐treatment plant and in the laboratory. The rate of regeneration of the GAC was found to be controlled by the rate of steam flow per unit GAC mass. The rate of regeneration increases with increasing steam flow in the range of steam flow rates used for commercial regeneration. At higher steam flow rates, the rate of reaction reaches a plateau value and is insensitive to changes in steam flow rate. Carbon dioxide has little, if any, effect on regeneration. Changing the inert gas flow rate used for fluidization of the GAC had no effect on the rate of regeneration at a fixed oxidant flow rate, even though it affected the oxidant partial pressure. Subbituminous GAC required higher temperatures than lignite GAC to regenerate to a specific apparent density in a fixed time period. Diffusion was not found to control the rate of regeneration. Different types of adsorbates used in a variety of studies were found to form chars of similar reactivity.
    publisherAmerican Society of Civil Engineers
    titleEffects of Oxidant on Thermal Regeneration of Granular Activated Carbon
    typeJournal Paper
    journal volume120
    journal issue1
    journal titleJournal of Environmental Engineering
    identifier doi10.1061/(ASCE)0733-9372(1994)120:1(190)
    treeJournal of Environmental Engineering:;1994:;Volume ( 120 ):;issue: 001
    contenttypeFulltext
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