化工进展 ›› 2022, Vol. 41 ›› Issue (4): 2191-2201.DOI: 10.16085/j.issn.1000-6613.2021-0863

• 资源与环境化工 • 上一篇    下一篇

反硝化除磷+短程反硝化厌氧氨氧化工艺的深度脱氮除磷效能

汪宇光1(), 张星星1, 王超超1, 夏云康1, 王垚1, 周澄1, 吴翼伶1, 吴鹏1,2,3, 徐乐中1,2,3()   

  1. 1.苏州科技大学环境科学与工程学院,江苏 苏州 215009
    2.城市生活污水资源化利用技术国家地方联合工程 实验室,江苏 苏州 215009
    3.江苏高校水处理技术与材料协同创新中心,江苏 苏州 215009
  • 收稿日期:2021-04-22 修回日期:2021-05-22 出版日期:2022-04-23 发布日期:2022-04-25
  • 通讯作者: 徐乐中
  • 作者简介:汪宇光(1996—),男,硕士研究生,研究方向为污水处理与回用技术。E-mail:746962887@qq.com
  • 基金资助:
    国家自然科学基金(51578353)

Achieving advanced nitrogen and phosphorus removal based on denitrifying phosphorus removal and partial denitrification Anammox process

WANG Yuguang1(), ZHANG Xingxing1, WANG Chaochao1, XIA Yunkang1, WANG Yao1, ZHOU Cheng1, WU Yiling1, WU Peng1,2,3, XU Lezhong1,2,3()   

  1. 1.School of Environmental Science and Engineering, Suzhou University of Science and Technology, Suzhou 215009, Jiangsu, China
    2.National and Local Joint Engineering Laboratory of Resource Utilization Technology of Municipal Sewage, Suzhou 215009, Jiangsu, China
    3.Jiangsu High Education Collaborative Innovation Center of Water Treatment Technology and Material, Suzhou 215009, Jiangsu, China
  • Received:2021-04-22 Revised:2021-05-22 Online:2022-04-23 Published:2022-04-25
  • Contact: XU Lezhong

摘要:

为经济高效地去除城市生活污水和硝酸盐废水中的氮磷元素,本研究在厌氧折流板反应器(ABR)和连续搅拌反应器(CSTR)一体式反应器中分别建立了反硝化除磷(DPR)和短程反硝化厌氧氨氧化(PDA)工艺。结果表明,反应器运行185天,在缺氧/厌氧和外加COD/NO3--N比仅为0.7条件下,PO43--P和TN的去除率高达96.91%和97.75%,最终出水PO43--P和TN的浓度低至0.22mg/L和3.30mg/L,意味着该系统极佳的脱氮除磷效果不依赖氧气和有机碳源量。DPR对系统PO43--P和TN的去除均占主体部分(99.07%和60.23%),而PDA对总氮(TN)的去除占比呈现逐渐上升的趋势(4.53%→37.52%)。批次实验表明:①COD(300mg/L)显著抑制DPR菌活性,PO43--P主要是在缺氧状态下以NO3--N为电子受体,有机物为电子供体通过DPR途径去除;②高效短程反硝化过程(亚硝酸转化率92.25%)稳定为厌氧氨氧化供给电子受体(NO2--N),DPR系统剩余NH4+-N主要被NO2--N氧化去除,因此DPR+PDA系统实现了高效同步脱氮除磷效果。高通量测序表明,Accumulibacter(7.41%)是DPR系统功能性除磷菌,Thauera(7.24%)和Candidatus Brocadia(3.12%)为PDA系统关键脱氮菌。

关键词: 反硝化除磷, 厌氧氨氧化, 短程反硝化, 脱氮除磷, 微生物群落

Abstract:

In order to remove nitrogen and phosphorus from municipal wastewater and nitrate wastewater economically and efficiently, denitrifying phosphorus removal (DPR) and partial denitrification Anammox (PDA) processes were established in an Anaerobic Baffled Reactor (ABR) and Continuous Stirred Tank Reactor (CSTR) integrated reactor, respectively. Results showed that the removal efficiencies of PO43--P and TN were 96.91% and 97.75%, respectively, under the conditions of anoxic/anaerobic and external COD/NO3--N ratio of 0.7 after 185 days of operation. The final effluent PO43--P and TN concentrations were as low as 0.22mg/L and 3.30mg/L, respectively, which indicated that the excellent nitrogen and phosphorus removal efficiency of the system independent of oxygen and organic carbon sources. The removal of PO43--P and TN by DPR accounted for 99.07% and 60.23% of the total, respectively, while the proportion of TN removal by PDA increased gradually (4.53%→37.52%). Batch experiments showed that, ①high concentration of COD (300mg/L) significantly inhibited the activity of DPR bacteria, and PO43--P was mainly removed by DPR with NO3--N as electron acceptor and organic matter as electron donor under anoxic condition; ②the highly-efficient partial denitrification process (NTR 92.25%) supplied stable electron acceptor (NO2--N) for anammox, andthe residual NH4+-N of DPR system was mainly eliminated by NO2--N oxidation. Therefore, the DPR+PDA system had achieved the high-efficiency and synchronous nitrogen and phosphorus removal effect. High throughput sequencing showed that Accumulibacter (7.41%) was the functional phosphorus removal bacteria in DPR system, and Thauera (7.24%) and Candidatus Brocadia (3.12%) were the key nitrogen removal bacteria in PDA system.

Key words: denitrification and phosphorus removal(DPR), anaerobic ammonia oxidation(Anammox), partial denitrification(PD), nitrogen and phosphorus removal, microbial community

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