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    Please use this identifier to cite or link to this item: http://140.128.103.80:8080/handle/310901/21564


    Title: Using sequencing batch biofilm reactor (SBBR) to treat ABS wastewater
    Authors: Chang, C.-N.a, Chen, H.R.a, Huang, C.H.a, Chao, A.b
    Contributors: Department of Environmental Science and Engineering, Tunghai University
    Keywords: ABS wastewater;ORP;Real-time operation;SBBR system
    Date: 1999-10-17
    Issue Date: 2013-05-15T09:02:03Z (UTC)
    Publisher: New York, NY, USA
    Abstract: Ratio of total Kjeldahl Nitrogen to COD for ABS (acrylnitrile, butadiene and styrene) wastewater is in a range of 0.12-0.17, which is significantly higher than that needed for optimal growth of an activated sludge. In this work, an automated Sequencing Batch Biofilm Reactor (SBBR) system at lab- scale is applied to reduce the amount of ABS; this system is controlled by an on-line monitoring of oxidation-reduction potential (ORP). A comparison of the operation efficiency for the lab-scale SBBR operated with the control of fix-time method and ORP-based real-time automatic method is presented. The results show that the system ORP can be used as an available parameter for achieving a real-time operation and control of the lab-scale SBBR. It is found that the reaction time is reduced of 11.1-55.2% if an ORP-based real- time control is used, instead of the fixed-time control. Also, the SBBR system is made more efficient and cost-effective.

    Ratio of total Kjeldahl Nitrogen to COD for ABS (acrylnitrile, butadiene and styrene) wastewater is in a range of 0.12-0.17, which is significantly higher than that needed for optimal growth of an activated sludge. In this work, an automated Sequencing Batch Biofilm Reactor (SBBR) system at lab-scale is applied to reduce the amount of ABS; this system is controlled by an on-line monitoring of oxidation-reduction potential (ORP). A comparison of the operation efficiency for the lab-scale SBBR operated with the control of fix-time method and ORP-based real-time automatic method is presented. The results show that the system ORP can be used as an available parameter for achieving a real-time operation and control of the lab-scale SBBR. It is found that the reaction time is reduced of 11.1-55.2% if an ORP-based real-time control is used, instead of the fixed-time control. Also, the SBBR system is made more efficient and cost-effective.
    Relation: Water Science and Technology
    Volume 41, Issue 4-5, 2000, Pages 433-440
    Appears in Collections:[環境科學與工程學系所] 會議論文

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