Abstract：Based on the traditional SBR, a new pilot SBR system was established for the treatment of a high-strength ammonia nitrogen wastewater in order to research the effective treatment process. The effects of the nitrogen removal were emphatically studied. The results show that the optimum operating parameters gained is as follow: the inflow time is 1.5 h, the aeration time is 9 h, the aeration rate is 80 m3/h, the anaerobic stir time is 3 h, sedimentation time is 50 min, and the effluent time is 1.5 h. The SBR effluent meets the demands of the first class standard for synthetic ammonia industry wastewater of GB 13458—2001 "Integrated Wastewater Discharge Standard" when the removal rates of COD, NH+4-N and TN were equal to 91%, 87% and 83%, respectively.
黄天寅, 刘峰, 王传琦, 周彪, 吴玮. SBR工艺处理合成氨废水的中试研究[J]. 排灌机械工程学报, 2014, 32(6): 517-522.
Huang Tianyin, Liu Feng, Wang Chuanqi, Zhou Biao, Wu Wei. Pilot scale SBR process for removal of synthetic ammonium wastewater. Journal of Drainage and Irrigation Machinery Engin, 2014, 32(6): 517-522.
[1]国家统计局, 环境保护部. 2012中国环境统计年鉴[M]. 北京: 中国统计出版社, 2013.[2]曾庆玲, 李咏梅, 顾国维, 等. 合成氨废水资源化处理技术研究进展[J]. 环境科学与技术, 2010, 33(2): 95-98. Zeng Qingling, Li Yongmei, Gu Guowei, et al. Resources reuse approaches to synthetic ammonia waste-water treatment [J]. Environmental Science & Techno-logy, 2010, 33(2): 95-98.(in Chinese)[3]李桂荣, 潘文琛, 宋同鹤, 等. 硝化反硝化/生物接触氧化工艺处理合成氨废水[J]. 中国给水排水, 2010, 26(24): 77-80. Li Guirong, Pan Wenchen, Song Tonghe, et al. Combined process of nitrification, denitrification and biological contact oxidation for treatment of synthetic ammonia wastewater [J]. China Water & Wastewater, 2010, 26(24): 77-80.(in Chinese)[4]Obaja D, Macé S, Mata-Alvarez J, et al. Nitrification, denitrification and biological phosphorus removal in pi-ggery wastewater using a sequencing batch reactor [J]. Bioresource Technology, 2003, 87(1): 103-111.[5]Ra C S, Lo K V, Shin J S, et al. Biological nutrient removal with an internal organic carbon source in piggery wastewater treatment [J]. Water Research, 2000, 34(3):965-973.[6]Tilche A, Bortone G, Malaspina F, et al. Biological nutrient removal in a full-scale SBR treating piggery wastewater: Results and modeling [J]. Water Science and Technology, 2001, 43(3):363-371.[7]王凯军, 宋英豪. SBR工艺的发展类型及其应用特性[J]. 中国给水排水, 2010, 18(7): 23-26. Wang Kaijun, Song Yinghao. Development types and application characteristics of SBR process [J]. China Water & Wastewater, 2010, 18(7): 23-26.(in Chinese)[8]彭永臻. SBR法的五大优点[J]. 中国给水排水, 1993, 9(2): 29-31. Peng Yongzhen. Five advantages of SBR [J]. China Water & Wastewater, 1993, 9(2): 29-31.(in Chinese)[9]Jaume P, Joan G, Humbert S. Microfauna community as an indicator of effluent quality and operational para-meters in an activated sludge system for treating piggery wastewater [J].Water Air Soil Pollution, 2009, 203: 207-216.[10]国家环境保护总局.水和废水监测分析方法[M]. 北京:中国环境科学出版社, 2002.[11]刘艳, 张立卿, 邢嘉珅, 等. SBR工艺污泥沉降性能的影响因素研究[J]. 中国给水排水, 2008, 24(7): 104-108. Liu Yan, Zhang Liqing, Xing Jiashen, et al. Study on influencing factors of sludge settle ability in SBR [J]. China Water & Wastewater, 2008, 24(7): 104-108.(in Chinese)[12]Palm J C, Jenkins D, Parker D S. Relationship between organic loading, dissolved oxygen concentration and sludge process [J]. Journal of the Water Pollution Control Federation, 1980, 52(10): 2484-2506.[13]彭赵旭, 彭永臻, 吴昌永, 等. 曝气量对SBR工艺同步脱氮除磷的影响研究[J]. 中国给水排水, 2008, 24(3): 13-16. Peng Zhaoxu, Peng Yongzhen, Wu Changyong, et al. Effect of aeration rate on simultaneous nitrogen and phosphorus removal in SBR [J]. China Water & Wastewater, 2008, 24(3): 13-16.(in Chinese)[14]张晓丹, 宋乾武, 代晋国, 等. 温度及碳源对NPR工艺脱氮除磷效果的影响[J]. 环境科学研究, 2007, 20(4): 125-129. Zhang Xiaodan, Song Qianwu, Dai Jinguo, et al. Effect of sewage temperature and carbon source for nitrogen and phosphorus removal rate of NPR process [J]. Research of Environmental Sciences, 2007, 20(4): 125-129.(in Chinese)[15]Ginige M P, Bowyer J C, Foley L, et al. A comparative study of methanol as a supplementary carbon source for enhancing denitrification in primary and secondary ano-xic zones [J]. Biodegradation, 2009, 20(2): 221-234.[16]陈雪松, 陈水荣. 改善焦化废水生物脱氮效率的研究[J]. 中国给水排水, 2007, 21(2): 21-24. Chen Xuesong, Chen Shuirong. Study on improving the biodenitrification efficiency of coking wastewater [J]. China Water & Wastewater, 2007, 21(2): 21-24.(in Chinese)[17]周丹丹, 马放, 董双石, 等. 溶解氧和有机碳源对同步硝化反硝化的影响[J]. 环境工程学报, 2007, 1(4): 25-28. Zhou Dandan,Ma Fang,Dong Shuangshi, et al. Influen-ces of DO and organic carbon on simultaneous nitrification and denitrification [J]. Chinese Journal of Environmental Engineering, 2007, 1(4): 25-28.(in Chinese)[18]修海峰, 朱仲元, 丁爱中, 等. 潜流人工湿地生境因素分布及其除氮效应[J]. 人民黄河, 2011, 33(4): 60-65. Xiu Haifeng, Zhu Zhongyuan, Ding Aizhong, et al. Distribution of habitat factors of undercurrent constructed wetland and effect of nitrogen removal [J]. Yellow Ri-ver, 2011, 33(4): 60-62,65.(in Chinese)[19]吴昌永, 陈志强, 彭永臻, 等. 实时控制下短程生物脱氮的实现及其稳定性研究[J]. 中国给水排水, 2006, 19(11): 39-43. Wu Changyong, Chen Zhiqiang, Peng Yongzhen, et al. Achievement and stability of shortcut biological nitrogen removal under real-time control [J]. China Water & Wastewater, 2006, 19(11): 39-43.(in Chinese)[20]孙剑辉, 魏瑞霞. 缺氧/好氧SBR工艺去除亚铵法造纸废水中的氮[J]. 环境科学, 2001, 22(4): 117-119. Sun Jianhui, Wei Ruixia. Removing the nitrogen from the ammonium sulfite method paper mill wastewater by anoxic/aerobic SBR [J]. Environmental Science, 2001, 22(4): 117-119.(in Chinese)[21]冯素敏, 邵立荣, 杨景亮, 等. CASS工艺在合成氨废水处理工程中的应用[J]. 水处理技术, 2008, 34(5): 76-80. Feng Sumin, Shao Lirong, Yang Jingliang, et al. The application of CASS process in synthetic ammonia wastewater treatment engineering [J]. Technology of Water Treatment, 2008, 34(5): 76-80.(in Chinese)
