匹配厌氧氨氧化—部分亚硝化启动调控策略研究

doi:10.11894/iwt.2019-1087

摘要/Abstract

摘要：

对部分亚硝化（PN）启动过程的基本认识和最新趋势进行总结，介绍了近年来关于PN启动调控的影响因素的研究结果，指出实际工程应用条件下的主要挑战和机遇，对PN研究进行展望并提供可用的优化策略，以期促进主流PN/AMX的工艺设计和操作。

Abstract:

The basic understanding and the latest trend of partial nitritation(PN) initiation process were summarized. The influencing factors and research results of PN initiation regulation in recent years were expounded. The main challenges and opportunities under practical engineering conditions were pointed out. PN research was prospected, and available optimization strategies were provided. It is hoped to facilitate the process design and operation of mainstream PN/AMX.

Key words: partial nitritation, Anaerobic ammonium oxidation, initial regulation, optimization

中图分类号:

TU992.3

达方华,徐乐中,王垚,王超超,陈茂林. 匹配厌氧氨氧化—部分亚硝化启动调控策略研究[J]. 工业水处理, 2020, 40(12): 19-24.

Fanghua Da,Lezhong Xu,Yao Wang,Chaochao Wang,Maolin Chen. Research progress on matching anaerobic ammonia oxidation-partial nitritation initiation regulation strategies[J]. Industrial Water Treatment, 2020, 40(12): 19-24.

https://www.iwt.cn/CN/Y2020/V40/I12/19

图/表 2

参考文献 44

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反应器	废水水源	温度/℃	启动方法	启动时间/d
SBR	人工配制低碳氮比（0.25~1.5）废水	27±1	结合微孔曝气和连续搅拌，通过逐步减小曝气量和HRT，完成AOB的富集和NOB抑制，实现部分亚硝化	16~50^〔6〕
CSTR	人工配水	20±3	采用控制DO（0.15~0.40 mg/L）、逐渐降低氨氮（245~60 mg/L）的方式启动亚硝化后，通过缩短HRT和调节DO实现部分亚硝化	44~70^〔7〕
MBR	高氨氮废水	25	在限氧条件下逐步提升进水NH₄⁺-N，将氨负荷率（ALR）作为主要控制参数，启动亚硝化后通过缩短HRT完成部分亚硝化	27^〔8〕
MBBR	低碳氮比生活污水	28	控制DO为0.8~1.0 mg/L促进AOB生长，消除NOB代谢，启动部分亚硝化	14^〔9〕
CRI	模拟生活污水	—	通过饥饿协同pH调控的方式启动部分亚硝化	15^〔10〕
IFAS	城市污水	25	通过间歇曝气、控制曝气强度和曝气时间协同控制进水氮负荷的方式启动部分亚硝化	43~80^〔11〕
气提式反应器	模拟含氨废水	30	采用高氨氮负荷（进水NH₄⁺-N为358.5~942.3 mg/L）和低HRT（0.86~2 h）方式启动半亚硝化	37^〔12〕

反应器	废水水源	温度/℃	启动方法	启动时间/d
SBR	人工配制低碳氮比（0.25~1.5）废水	27±1	结合微孔曝气和连续搅拌，通过逐步减小曝气量和HRT，完成AOB的富集和NOB抑制，实现部分亚硝化	16~50^〔6〕
CSTR	人工配水	20±3	采用控制DO（0.15~0.40 mg/L）、逐渐降低氨氮（245~60 mg/L）的方式启动亚硝化后，通过缩短HRT和调节DO实现部分亚硝化	44~70^〔7〕
MBR	高氨氮废水	25	在限氧条件下逐步提升进水NH₄⁺-N，将氨负荷率（ALR）作为主要控制参数，启动亚硝化后通过缩短HRT完成部分亚硝化	27^〔8〕
MBBR	低碳氮比生活污水	28	控制DO为0.8~1.0 mg/L促进AOB生长，消除NOB代谢，启动部分亚硝化	14^〔9〕
CRI	模拟生活污水	—	通过饥饿协同pH调控的方式启动部分亚硝化	15^〔10〕
IFAS	城市污水	25	通过间歇曝气、控制曝气强度和曝气时间协同控制进水氮负荷的方式启动部分亚硝化	43~80^〔11〕
气提式反应器	模拟含氨废水	30	采用高氨氮负荷（进水NH₄⁺-N为358.5~942.3 mg/L）和低HRT（0.86~2 h）方式启动半亚硝化	37^〔12〕

种泥类型	反应器	启动方法	启动时间/d
厌氧污泥（厌氧亚硝化污泥）	MBR	结合间歇曝气和缩短HRT的方式实现短程硝化	8^〔18〕
好氧颗粒污泥	GSBR	逐步提高进水NH₄⁺-N负荷启动亚硝化，调控曝气，用低DO和高NLR的协同调控完成部分亚硝化	60^〔19〕
好氧絮状污泥	CSTR	控制低DO（0.8~1.2 mg/L）和短HRT（3 h）启动亚硝化，调控FA（2~10 mg/L）驯化AOB实现部分亚硝化	15^〔20〕
厌氧亚硝化和反硝化混合污泥	MBR	结合间歇曝气和缩短HRT的方式实现短程硝化	30^〔18〕

种泥类型	反应器	启动方法	启动时间/d
厌氧污泥（厌氧亚硝化污泥）	MBR	结合间歇曝气和缩短HRT的方式实现短程硝化	8^〔18〕
好氧颗粒污泥	GSBR	逐步提高进水NH₄⁺-N负荷启动亚硝化，调控曝气，用低DO和高NLR的协同调控完成部分亚硝化	60^〔19〕
好氧絮状污泥	CSTR	控制低DO（0.8~1.2 mg/L）和短HRT（3 h）启动亚硝化，调控FA（2~10 mg/L）驯化AOB实现部分亚硝化	15^〔20〕
厌氧亚硝化和反硝化混合污泥	MBR	结合间歇曝气和缩短HRT的方式实现短程硝化	30^〔18〕

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