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TY-BM1型多介质膜一体化设备处理农村生活污水的效果

杨明 陈建 潘成荣 张雷 马洁晨 王琳 龚明杰 汪军

杨明,陈建,潘成荣,等.TY-BM1型多介质膜一体化设备处理农村生活污水的效果[J].环境工程技术学报,2023,13(2):648-653 doi: 10.12153/j.issn.1674-991X.20220077
引用本文: 杨明,陈建,潘成荣,等.TY-BM1型多介质膜一体化设备处理农村生活污水的效果[J].环境工程技术学报,2023,13(2):648-653 doi: 10.12153/j.issn.1674-991X.20220077
YANG M,CHEN J,PAN C R,et al.Effect of TY-BM1 multi-media membrane integrated equipment on rural domestic sewage treatment[J].Journal of Environmental Engineering Technology,2023,13(2):648-653 doi: 10.12153/j.issn.1674-991X.20220077
Citation: YANG M,CHEN J,PAN C R,et al.Effect of TY-BM1 multi-media membrane integrated equipment on rural domestic sewage treatment[J].Journal of Environmental Engineering Technology,2023,13(2):648-653 doi: 10.12153/j.issn.1674-991X.20220077

TY-BM1型多介质膜一体化设备处理农村生活污水的效果

doi: 10.12153/j.issn.1674-991X.20220077
基金项目: 安徽省现代农业产业技术体系建设专项资金
详细信息
    作者简介:

    杨明(1973—),男,高级工程师,硕士,研究方向为水环境综合治理工程,xms325@qq.com

    通讯作者:

    汪军(1982—),男,正高级工程师,研究方向为环境修复与污染控制,flypigging@hotmail.com

  • 中图分类号: X703

Effect of TY-BM1 multi-media membrane integrated equipment on rural domestic sewage treatment

  • 摘要:

    随着乡村振兴战略的深入推进和污水排放标准的日趋严格,对农村生活污水处理技术提出了更高要求。针对移动式生物膜技术进行优化改进,构建了组合式上向分流多介质生物膜工艺,以实际农村生活污水为处理对象,探究该技术处理效果及推广应用价值。结果表明,该工艺可高效利用污水中的碳源进行脱氮,在多介质膜池水力停留时间≥0.15 d、气水比≥3∶1及1.50倍硝化液回流条件下,实现无污泥回流条件下对污水中的悬浮物、总氮、氨氮、化学需氧量和总磷的去除,去除率分别达96.23%、47.33%、78.89%、79.38%和80.77%,出水水质优于GB 18918—2002《城镇污水处理厂污染物排放标准》的一级A标准。

     

  • 图  1  TY-BM1型多介质膜一体化污水设备工艺

    Figure  1.  TY-BM1 multi-media membrane integrated sewage equipment operation process

    图  2  装置的SS去除效果

    Figure  2.  SS removal effect of the device

    图  3  装置的CODCr去除效果

    Figure  3.  CODCr removal effect of the device

    图  4  装置对TP的削减效果

    Figure  4.  TP reduction effect of the device

    图  5  进水氮浓度

    Figure  5.  Influent nitrogen concentration

    图  6  装置对氮的削减效果

    Figure  6.  Nitrogen reduction effect of the device

    表  1  装置各单元参数

    Table  1.   Parameters of each unit of the device

    单元池体规格
    (长×宽×高)/m
    运行
    水深/m
    HRT/d水力负荷/
    〔m3/(m2·d)〕
    曝气量/
    (L/min)
    厌氧池0.40×0.30×0.700.600.07~0.242.50~8.30
    缺氧池0.40×0.40×0.700.600.10~0.321.88~6.25
    多介质生
    物膜池
    0.50×0.50×0.700.600.15~0.501.2~4.005.00±2.50
    沉淀池0.50×0.40×0.700.500.10~0.291.46~5.00
    下载: 导出CSV

    表  2  装置进、出水水质

    Table  2.   Fluctuation of water quality of influent and effluent of the equipment mg/L 

    项目SS浓度TN浓度NO3 -N浓度NH4 +-N浓度CODCrTP浓度
    进水174.38±5.7322.43±0.290.14±0.0418.98±0.3499.91±2.312.36±0.02
    出水6.13±1.2011.67±0.195.95±0.073.99±0.1219.8±1.650.42±0.01
    GB 18918—2002一级A标准≤10≤15≤5≤50≤0.50
    下载: 导出CSV
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