WANG Zhao-zhao,ZHANG Huan,YAN Li-na,et al.Recovery and Operational Characteristics of Anammox Process after High Salinity Shock[J].China Water & Wastewater,2021,37(3):16-23.
高盐度冲击后厌氧氨氧化工艺恢复及运行特性
- Title:
- Recovery and Operational Characteristics of Anammox Process after High Salinity Shock
- 摘要:
- 通过逐步增加UASB反应器进水氮负荷[1.06~1.42 kg/(m3·d)]方式,考察了厌氧氨氧化(Anammox)工艺受到高盐度冲击后的恢复及运行特性。结果表明,经过156 d的运行,NH4+-N、NO2--N、TN去除率及总氮去除负荷(NRR)分别达到97.57%、96.40%、83.90%和1.19 kg/(m3·d),这主要归功于Anammox污泥的活性得到了有效恢复[TN的比降解速率由0.131 mg/(mgVSS·d)提高到0.302 mg/(mgVSS·d)];随着工艺运行效能的恢复,颗粒污泥的颜色由深褐色变为红褐色,平均粒径也随之增大,粒径>1.5 mm的占比最高,达到了68.25%;此外,胞外聚合物(EPS)含量由96.66 mg/g增大至147.98 mg/g,并且PN/PS值由4.86增大至13.34,厌氧氨氧化工艺可恢复到高效运行状态。
- Abstract:
- The recovery and operational characteristics of Anammox process after high salinity shock were investigated by stepwise increasing influent nitrogen loading rate (NLR) from 1.06 kg/(m3·d) to 1.42 kg/(m3·d) in an upflow anaerobic sludge blanket (UASB). After operating for 156 days, the removal efficiencies of? NH4+-N、NO2--N and TN reached 97.57%, 96.40% and 83.90%,and the total nitrogen removal loading (NRR) reached 1.19 kg/(m3·d), which was attributed to the effective recovery of Anammox sludge activity [specific degradation rate of TN increased from 0.131 mg/(mgVSS·d) to 0.302 mg/(mgVSS·d)]. With the recovery of the process performance, the color of the granular sludge turned from deep brown to red brown, and the average particle size increased,among which granules with particle size larger than 1.5 mm accounted for the maximum proportion of 68.25%. Moreover, EPS content increased from 96.66 mg/g to 147.98 mg/g, and PN/PS ratio increased from 4.86 to 13.34, which further proved that the Anammox process recovered to an efficient operational state.
相似文献/References:
[1]郭莉芳,朱宇峰,滕良方,等.MBBR用于南方某污水厂强化脱氮效果分析[J].中国给水排水,2020,36(7):101.
[2]田敏,崔涛,吕恺,等.西安市第四污水处理厂A2/O工艺的脱氮性能评价[J].中国给水排水,2020,36(13):1.
TIAN Min,CUI Tao,LU Kai,et al. Denitrification Performance Evaluation of A2/O Process in Xi’an Fourth Wastewater Treatment Plant [J].China Water & Wastewater,2020,36(3):1.
[3]吴彦成,顾鑫,朱继涛,等.铁氨氧化污水生物脱氮技术的研究进展[J].中国给水排水,2020,36(18):38.
WU Yan-cheng,GU Xin,ZHU Ji-tao,et al.Research Advances of Biological Nitrogen Removal from Wastewater via Fe(Ⅲ) Reduction Coupled to Anaerobic Ammonium Oxidation (Feammox) Process[J].China Water & Wastewater,2020,36(3):38.
[4]黄子洪,向婷,方华,等.分步进水SBR工艺生物脱氮运行条件优化及数学模拟[J].中国给水排水,2020,36(23):89.
HUANG Zi-hong,XIANG Ting,FANG Hua,et al.Operational Condition Optimization and Mathematical Simulation of Biological Denitrification in Step-feed SBR Process[J].China Water & Wastewater,2020,36(3):89.
[5]冯红利,赵梦月,丁舒喆.城市污水厂A2/O工艺生物脱氮过程优化控制[J].中国给水排水,2021,37(6):102.
FENG Hong-li,ZHAO Meng-yue,DING Shu-zhe.Optimal Control of Biological Nitrogen Removal in A2/O Process of WWTP[J].China Water & Wastewater,2021,37(3):102.
[6]付昆明,傅思博,仇付国.不同生物脱氮路径下氧气、碳源等需求理论分析[J].中国给水排水,2021,37(10):8.
FU Kun-ming,FU Si-bo,QIU Fu-guo.Theoretical Analysis of Oxygen and Carbon Source Demand under Different Biological Nitrogen Removal Pathways[J].China Water & Wastewater,2021,37(3):8.
[7]王拓,严冰.多级A/O工艺协同精确控制系统用于低C/N进水污水厂[J].中国给水排水,2021,37(12):65.
WANG Tuo,YAN Bing.Application of Multi-stage A/O Process Collaborative Precise Control System in Wastewater Treatment Plant with Low C/N Influent[J].China Water & Wastewater,2021,37(3):65.
[8]周小琳,樊星,毕学军,等.两段式A/O-MBBR工艺生物脱氮中试与系统优化[J].中国给水排水,2021,37(19):72.
ZHOU Xiao-lin,FAN Xing,BI Xue-jun,et al.Pilot-scale Test and System Optimization of Two-stage A/O-MBBR Process for Biological Nitrogen Removal[J].China Water & Wastewater,2021,37(3):72.
[9]贺阳,袁玉亮,王进峰,等.超高浓度总氮废水生物脱氮工艺运行实例[J].中国给水排水,2021,37(20):116.
HE Yang,YUAN Yu-liang,WANG Jin-feng,et al.An Operation Case of Biological Denitrification Process for Ultra-high Total Nitrogen Wastewater[J].China Water & Wastewater,2021,37(3):116.
[10]刘臣,樊雪红,徐耀鹏.基于日本下水道事业团的多级AO工艺计算与探讨[J].中国给水排水,2022,38(2):49.
LIU Chen,FAN Xue?hong,XU Yao?peng.Calculation and Discussion of Multi?stage AO Process Based on Japanese Sewage Works Agency[J].China Water & Wastewater,2022,38(3):49.