[1]王娜,秦凯凯,姚雪薇,等.两段式MBBR亚硝化-厌氧氨氧化处理污泥消化液[J].中国给水排水,2024,40(13):61-67.
　WANGNa,QINKai-kai,YAOXue-wei,et al.Two-stage MBBR of Partial Nitritation-ANAMMOX for Treatment of Thermal-hydrolysis Anaerobic Digester Effluent[J].China Water & Wastewater,2024,40(13):61-67.
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两段式MBBR亚硝化-厌氧氨氧化处理污泥消化液

中国给水排水[ISSN:1000-4062/CN:12-1073/TU] 卷: 第40卷 期数: 2024年第13期 页码: 61-67 栏目: 出版日期: 2024-07-01
Title:
Two-stage MBBR of Partial Nitritation-ANAMMOX for Treatment of Thermal-hydrolysis Anaerobic Digester Effluent
作者:
王娜1,2， 秦凯凯3， 姚雪薇3， 吕恺1,2， 彭党聪3， 韩芸2
（1.宁夏大学 生态环境学院，宁夏 银川 750021；2.西北退化生态系统恢复与重建教育部重点实验室，宁夏 银川 750021；3.西安建筑科技大学 环境与市政工程学院，陕西 西安 710055）
Author(s):
WANG　Na1，2， QIN　Kai-kai3， YAO　Xue-wei3， Lü　Kai1，2， PENG　Dang-cong3， HAN　Yun2
（1. School of Ecology and Environment， Ningxia University， Yinchuan 750021， China； 2. Key Lab. of Restoration and Reconstruction of Degraded Ecosystems in Northwest ern China， Ningxia University， Yinchuan 750021， China； 3. School of Municipal and Environmental Engineering， Xi’an University of Architecture and Technology， Xi’an 710055， China）
关键词:
污泥热水解厌氧消化液;  亚硝化;  厌氧氨氧化;  移动床生物膜反应器
Keywords:
thermal-hydrolysis anaerobic digester effluent;  partial nitritation;  ANAMMOX;  moving-bed biofilm reactor (MBBR)
摘要:
采用两段式MBBR亚硝化-厌氧氨氧化工艺处理含有高浓度氨氮的污泥热水解厌氧消化液。结果表明，当进水NH4+-N浓度为（750.32±32.21） mg/L时，亚硝化反应器的氮负荷可达到1.25 kg/（m3·d），平均出水NO2--N/NH4+-N值为1.18±0.18，满足厌氧氨氧化进水水质要求。厌氧氨氧化反应器的氮负荷可达到0.84 kg/（m3·d），TN平均去除率为76.05%。在进水COD为（932±39） mg/L的条件下，亚硝化和厌氧氨氧化反应器出水COD浓度分别为（623±43）、（590±45） mg/L，COD的降解主要在亚硝化段完成，其对COD的去除贡献可达87.16%。在处理污泥热水解厌氧消化液后，氨氧化菌（AOB）和厌氧氨氧化菌活性分别损失了21.17%和39.82%，表明污泥热水解厌氧消化液中的复杂有机物对脱氮微生物有抑制作用，尤其是对厌氧氨氧化菌。
Abstract:
A two-stage MBBR of partial nitritation-ANAMMOX process was employed for the treatment of thermal-hydrolysis anaerobic digester effluent with high ammonia nitrogen. When the influent NH4+-N was (750.32±32.21) mg/L, the partial nitritation reactor reached a nitrogen load of 1.25 kg/(m3·d), with an average effluent NO2--N/NH4+-N ratio of 1.18±0.18, meeting the influent quality requirement for ANAMMOX. The ANAMMOX reactor was capable of reaching a nitrogen load of 0.84 kg/(m3·d), with an average TN removal rate of 76.05%. Under the condition of influent COD at (932±39) mg/L, the effluent COD from the partial nitritation and ANAMMOX reactors were (623±43) mg/L and (590±45) mg/L, respectively. The degradation of COD was primarily achieved in the partial nitritation reactor, with its contribution to COD removal reaching 87.16%. After treating thermal-hydrolysis anaerobic digester effluent, the activities of ammonia oxidizing bacteria (AOB) and ANAMMOX bacteria decreased by 21.17% and 39.82%, respectively, indicating that the complex organic matter had an inhibitory effect on nitrogen removal microorganisms, particularly on ANAMMOX bacteria.
更新日期/Last Update: 2024-07-01