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短程反硝化强化脱氮的影响因素及其耦合工艺应用进展

薛同站 全志道 李卫华 杨厚云 闫祥宇 杨欣蕾

薛同站,全志道,李卫华,等.短程反硝化强化脱氮的影响因素及其耦合工艺应用进展[J].环境工程技术学报,2024,14(2):663-671 doi: 10.12153/j.issn.1674-991X.20230621
引用本文: 薛同站,全志道,李卫华,等.短程反硝化强化脱氮的影响因素及其耦合工艺应用进展[J].环境工程技术学报,2024,14(2):663-671 doi: 10.12153/j.issn.1674-991X.20230621
XUE T Z,QUAN Z D,LI W H,et al.Influencing factors of partial denitrification to enhance nitrogen removal and its coupled process application progress[J].Journal of Environmental Engineering Technology,2024,14(2):663-671 doi: 10.12153/j.issn.1674-991X.20230621
Citation: XUE T Z,QUAN Z D,LI W H,et al.Influencing factors of partial denitrification to enhance nitrogen removal and its coupled process application progress[J].Journal of Environmental Engineering Technology,2024,14(2):663-671 doi: 10.12153/j.issn.1674-991X.20230621

短程反硝化强化脱氮的影响因素及其耦合工艺应用进展

doi: 10.12153/j.issn.1674-991X.20230621
基金项目: 国家自然科学基金项目(51978003);国家重点研发计划项目(2020YFC1908600);安徽高校自然科学研究项目(2022AH050258)
详细信息
    作者简介:

    薛同站(1972—),男,副教授,研究方向为环境污染控制与废物资源化利用,xtongzan@126.com

    通讯作者:

    全志道(1998—),男,硕士研究生,研究方向为环境污染控制与废物资源化利用,1073063806@qq.com

  • 中图分类号: X703

Influencing factors of partial denitrification to enhance nitrogen removal and its coupled process application progress

  • 摘要:

    短程反硝化(PD)工艺作为脱氮的前端工艺以其效率高、能耗低以及温室气体排放量少等优点而备受青睐,成为近年来研究热点。短程反硝化耦合厌氧氨氧化(PD/A)工艺是一种新型生物脱氮工艺,不仅在氮循环中发挥着重要作用,而且在节能和环保方面具有很高的经济和实用价值。基于已有研究成果,介绍了PD工艺的研究现状,分析了不同接种污泥对PD工艺启动的影响;从磁效应、碳源、碳氮比(C/N)以及铁炭比等方面进行评述,揭示了关键影响因子对PD工艺强化脱氮过程中微生物群落结构、关键酶活性和细胞代谢途径的影响机理;浅析了PD/A工艺不同耦合形式的特点,对耦合工艺处理城市生活污水、养殖废水和垃圾渗滤液等实际废水的研究与应用进展进行总结;最后,展望了PD/A工艺在污水脱氮处理方面的前景,并结合现有研究提出了PD/A工艺处理垃圾渗滤液的潜在工程应用方案,认为克服PD工艺的影响因素及优化PD/A的参数以提升工艺运行的高效性和稳定性是未来研究的重点方向。

     

  • 图  1  PD/A反应机理

    Nar—硝酸盐还原酶;Nir—亚硝酸盐还原酶;HZO—联氨氧化酶;HH—联氨水解酶;PDB—短程反硝化细菌;AnAOB—厌氧氨氧化细菌。

    Figure  1.  PD/A reaction mechanism

    图  2  铁元素参与氮转化过程

    Feammox—铁还原氨氧化;NDFO—铁型反硝化。

    Figure  2.  Nitrogen conversion process involving iron elements

    图  3  PN+PD/A处理垃圾渗滤液工艺流程

    Figure  3.  PN+PD/A process flow chart of landfill leachate treatment

    表  1  不同碳源下${\rm NO}_2^-{\text{-N}} $的积累情况

    Table  1.   Accumulation of ${\rm NO}_2^-{\text{-N}} $ of different carbon sources

    碳源类型 碳源 接种污泥 运行条件 进水${\rm NO}_3^-{\text{-N}} $
    浓度/(mg/L)
    ${\rm NO}_3^-{\text{-N}} $
    去除率/%
    NAR/% 功能菌属 数据来源
    小分子碳源 乙酸钠 污水处理厂二沉池污泥 SBR反应器,
    温度为25 ℃,
    pH为9.0,C/N为2.5
    60 84.91 87.01 Thauera 文献[29]
    葡萄糖 污水处理厂缺氧池污泥 SBR反应器,
    pH为6.8~7.2,C/N为11
    25 99 97 Competibacter
    Thaurea
    文献[30]
    乙醇 实验室培养良好的污泥 SBR反应器,
    不控制温度,
    C/N为1.77
    800 99.3 99 Thaurea 文献[31]
    甘油 以甘油为碳源培养的污泥 SBR反应器,
    温度为17~27 ℃,
    pH为7.0~7.5
    40 >90 87.3 Saccharibacteria 文献[32]
    大分子碳源 淀粉 污水处理厂澄清池污泥 SBR反应器,
    温度为28~30 ℃,
    C/N为6.4
    40 98 81.1 Dechloromonas
    Thauera
    文献[33]
    复杂碳源 城市污水+少量
    乙酸钠
    实验室培养良好的污泥 SBR反应器,
    温度为26 ℃,
    C/N为3.0
    40 97.9 85.6 Brocadia 文献[9]
    污泥发酵液 实验室缺氧污泥 SBR反应器,
    温度为18~23℃,
    C/N为4.0
    30 99 80 文献[34]
    垃圾渗滤液+
    生活污水
    ASBR反应器,
    温度为20~22 ℃,
    pH为7.0~7.5,C/N为3.2
    40±5 92 70 Thauera
    文献[35]
    下载: 导出CSV

    表  2  PD/A工艺的实际应用

    Table  2.   Practical application of PD/A process

    污水种类 污水特性 污泥
    类型
    处理
    工艺
    运行条件 ${\rm NH}_4^+{\text{-N}} $
    去除率/
    %
    ${\rm NO}_3^-{\text{-N}} $
    去除率/
    %
    NAR/% TN
    去除率/
    %
    功能菌属 数据来源
    城市生活
    污水
    低C/N 短程反硝化污泥 分离式
    PD/A
    SBR反应器,
    UASB反应器,
    HRT为2.0~2.3 h,
    温度为14.8~28.2 ℃
    92.8 95.8 80 91.2 Thauera、
    Jettenia
    Brocadia
    文献[51]
    短程硝化
    悬浮污泥
    PN/A-EPD/A工艺 一体式固定膜
    序批式反应器
    (IFAS-SBR),
    温度为(30±1)℃,
    HRT为12 h
    90 77.4 90.1 Brocadia
    Competibacter
    文献[52]
    养殖废水 高COD、
    高氨氮
    厌氧氨氧化污泥、反硝化污泥 一体式
    PD/A
    UASB反应器,
    温度为30 ℃,
    pH为8.0,
    HRT为24 h
    93.13 89.42 Thauera
    Brocadia
    文献[53]
    反硝化污泥、
    厌氧污泥
    一体式
    PD/A
    UASB反应器,
    温度为31~35 ℃,
    HRT为24 h
    88.2 84.2 Brocadia 文献[54]
    垃圾渗
    滤液
    高C/N,
    生化性差
    短程硝化
    污泥
    一体式
    PD/A
    SBR反应器,
    温度为(30±1)℃,
    C/N为3.0
    80 90 75.6 84.8 Thauera
    Brocadia
    文献[55]
    污水处理厂剩余污泥 PVA/SA凝胶一体式PD/A
    SBR反应器,
    乙酸钠为碳源,
    温度为13 ℃,
    C/N为3.0±0.1
    90 95 86.8 90 Thauera
    Kuenenia
    文献[56]
    下载: 导出CSV
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出版历程
  • 收稿日期:  2023-08-26
  • 录用日期:  2023-12-29
  • 修回日期:  2023-12-18

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