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    Microfiltration of a Dental Wastewater for Hg Removal: Clinic Demonstration

    Source: Journal of Environmental Engineering:;2004:;Volume ( 130 ):;issue: 001
    Author:
    Brian E. Reed
    ,
    Michael D. Bagby
    ,
    Ronald L. Vaughan, Jr.
    DOI: 10.1061/(ASCE)0733-9372(2004)130:1(12)
    Publisher: American Society of Civil Engineers
    Abstract: Hollow fiber (HF) and tubular membranes were installed at a dental clinic and used to treat dental wastewater (DWW) over a six-month period. Both membranes rejected the vast majority of the Hg (Tubular: 99% rejection and permeate Hg=20.8 μg/L; HF: 97% rejection and permeate Hg=6.6 μg/L). Permeate Hg concentration and flux were not adversely affected by concentrating the DWW indicating that the system can be operated indefinitely. Biological growth blocked the openings of the HF lumens necessitating frequent maintenance. The tubular membrane with its large channel diameter (2.53 cm versus 1 mm for the HF) did not experience channel blockage. Given the small volume of DWW that is produced at a dental facility (≈3 L/d), the packing density and footprint of the membrane unit are not a major concern, thus, HF module offers no real advantage over the tubular module. Additionally, the increase maintenance that is required with the HF module is a distinct disadvantage making the tubular module better suited for dental facilities.
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      Microfiltration of a Dental Wastewater for Hg Removal: Clinic Demonstration

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    http://yetl.yabesh.ir/yetl1/handle/yetl/59597
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    • Journal of Environmental Engineering

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    contributor authorBrian E. Reed
    contributor authorMichael D. Bagby
    contributor authorRonald L. Vaughan, Jr.
    date accessioned2017-05-08T21:41:36Z
    date available2017-05-08T21:41:36Z
    date copyrightJanuary 2004
    date issued2004
    identifier other%28asce%290733-9372%282004%29130%3A1%2812%29.pdf
    identifier urihttp://yetl.yabesh.ir/yetl/handle/yetl/59597
    description abstractHollow fiber (HF) and tubular membranes were installed at a dental clinic and used to treat dental wastewater (DWW) over a six-month period. Both membranes rejected the vast majority of the Hg (Tubular: 99% rejection and permeate Hg=20.8 μg/L; HF: 97% rejection and permeate Hg=6.6 μg/L). Permeate Hg concentration and flux were not adversely affected by concentrating the DWW indicating that the system can be operated indefinitely. Biological growth blocked the openings of the HF lumens necessitating frequent maintenance. The tubular membrane with its large channel diameter (2.53 cm versus 1 mm for the HF) did not experience channel blockage. Given the small volume of DWW that is produced at a dental facility (≈3 L/d), the packing density and footprint of the membrane unit are not a major concern, thus, HF module offers no real advantage over the tubular module. Additionally, the increase maintenance that is required with the HF module is a distinct disadvantage making the tubular module better suited for dental facilities.
    publisherAmerican Society of Civil Engineers
    titleMicrofiltration of a Dental Wastewater for Hg Removal: Clinic Demonstration
    typeJournal Paper
    journal volume130
    journal issue1
    journal titleJournal of Environmental Engineering
    identifier doi10.1061/(ASCE)0733-9372(2004)130:1(12)
    treeJournal of Environmental Engineering:;2004:;Volume ( 130 ):;issue: 001
    contenttypeFulltext
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