doi:10.13205/j.hjgc.201909013

Volume 37 Issue 9

Sep. 2019

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doi: 10.13205/j.hjgc.201909013

Received Date: 2018-11-21
Available Online: 2023-11-24
Publish Date: 2019-09-30

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References

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[3]	Stinson B,Peric M,Neupane D,et al. Design and operating considerations for a post denitrification MBBR to achieve limit of technology effluent NO_x<1 mg/L and effluent TP <0. 18 mg/L[J].Proceedings of the Water Environment Federation,2009(30):1225-1254.
[4]	周永刚.反硝化生物滤池在污水厂升级改造中的应用[J].中国给水排水,2014,30(24):49-52.
[5]	曹相生,钱栋,孟雪征.乙酸钠为碳源时的污水反硝化规律研究[J].中国给水排水,2011,27(21):76-79.
[6]	Taljemark K,Aspegren H,Gruvberger C,et al. 10 years of experiences of an MBBR process for post-denitrification[J].Proceedings of the Water Environment Federation,2004(16):355-366.
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[8]	付昆明,曹相生,孟雪征,等.污水反硝化过程中亚硝酸盐氮的积累规律[J].环境科学,2011,32(6):1660-1664.
[9]	谢丽,蔡碧婧,杨殿海,等.亚硝酸积累条件下反硝化脱氮过程动力学模型[J].同济大学学报,2009,37(2):224-228.
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