碳源投加方式对SBR工艺脱氮速率的影响

张兰河, 丘晓春, 张宇, 庞香蕊, 刘鹤楠. 碳源投加方式对SBR工艺脱氮速率的影响[J]. 环境工程学报, 2015, 9(2): 731-736. doi: 10.12030/j.cjee.20150237
引用本文: 张兰河, 丘晓春, 张宇, 庞香蕊, 刘鹤楠. 碳源投加方式对SBR工艺脱氮速率的影响[J]. 环境工程学报, 2015, 9(2): 731-736. doi: 10.12030/j.cjee.20150237
Zhang Lanhe, Qiu Xiaochun, Zhang Yu, Pang Xiangrui, Liu Henan. Effect of different adding methods of carbon sources on denitrification rate[J]. Chinese Journal of Environmental Engineering, 2015, 9(2): 731-736. doi: 10.12030/j.cjee.20150237
Citation: Zhang Lanhe, Qiu Xiaochun, Zhang Yu, Pang Xiangrui, Liu Henan. Effect of different adding methods of carbon sources on denitrification rate[J]. Chinese Journal of Environmental Engineering, 2015, 9(2): 731-736. doi: 10.12030/j.cjee.20150237

碳源投加方式对SBR工艺脱氮速率的影响

  • 基金项目:

    吉林省科技发展计划项目(20130303080SF,20110405)

    吉林省省校合作技术开发项目(吉工信科技2011-507)

  • 中图分类号: X703.1

Effect of different adding methods of carbon sources on denitrification rate

  • Fund Project:
  • 摘要: 为了提高生物反应器的脱氮效率,研究采用SBR处理模拟生活污水,利用醋酸钠作为碳源,考察碳源投加方式对脱氮速率的影响。结果表明,当温度为10~15℃,进水COD为330~550 mg/L时,采用不同的碳源投加方式,COD去除率均高于95%。进水一次投加2.4 g碳源,COD平均反应速率为5.3 mg/(g·h),平均反硝化速率为0.28 mg/(g·h)。进水、反应器运行3 h时分别投加1.2 g碳源,COD平均反应速率为6.89 mg/(g·h),平均反硝化速率为0.37 mg/(g·h)。进水、反应6 h时分别投加1.2 g碳源,COD平均反应速率为6.50 mg/(g·h),平均反硝化速率为0.52 mg/(g·h)。进水投加1.2 g碳源、反应器运行3 h和6 h时分别投加0.6 g醋酸钠碳源,COD平均反应速率为6.2 mg/(g·h),平均反硝化速率为0.39 mg/(g·h)。分次投加碳源能够提高COD反应速率和TN去除率,同时保持较高的硝化反硝化速率。
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  • [1] Bernat K., Wojnowska-Baryła I., Dobrzyńska A. Denitrification with endogenous carbon source at low C/N and its effect on P(3HB) accumulation. Bioresource Technology, 2008, 99(7): 2410-2418
    [2] 贾艳萍, 贾心倩, 刘印, 等. 同步硝化反硝化脱氮机理及影响因素研究. 东北电力大学学报, 2013, 33(4): 19-23 Jia Yanping, Jia Xinqian, Liu Yin, et al. The study on nitrogen removal mechanism and affecting factors of simultaneous nitrification and denitrification. Journal of Northeast Dianli University, 2013, 33(4): 19-23 (in Chinese)
    [3] Kulkarni P. M. Effect of shock and mixed loading on the performance of SND based sequencing batch reactors (SBR) degrading nitrophenols. Water Research, 2012, 46(7): 2405-2414
    [4] 陈柏成, 马卓汝, 唐美珍. 外加碳源对SBR法处理生活污水的影响研究. 绿色科技, 2012, 9(2): 166-171 Chen Baicheng, Ma Zhuoru, Tang Meizhen. Effects of external carbon source on processing of beer wastewater according to SBR law. Journal of Green Science and Technology, 2012, 9(2): 166-171 (in Chinese)
    [5] Lan C. J., Kumar M., Wang C. C., et al. Development of simultaneous partial nitrification, anammox and denitrification (SNAD) process in a sequential batch reactor. Bioresource Technology, 2011, 102(9): 5514- 5519
    [6] Torà J. A., Baeza J. A., Carrera J., et al. Denitritation of a high-strength nitrite wastewater in a sequencing batch reactor using different organic carbon sources. Chemical Engineering Journal, 2011, 172(2-3): 994-998
    [7] 张万友, 张兰河, 杨涛, 等. 不同有机碳源对SBR工艺同步硝化反硝化影响. 化工进展, 2010, 29(12): 2395-2399 Zhang Wanyou, Zhang Lanhe, Yang Tao, et al. Effects of organic carbon on simultaneous nitrification and denitrification in sequencing batch reactor. Chemical Industry and Engineering Progress, 2010, 29(12): 2395-2399 (in Chinese)
    [8] 胡宇华, 丁富新, 范轶, 等. 有机碳源对同时硝化/反硝化(SND)过程的影响. 环境工程, 2001, 19(4): 17-20 Hu Yuhua, Ding Fuxin, Fan Yi, et al. Efects of organic carbon resource on process of simultaneous nitrification and denitrification (SND). Environmental Engineering, 2001, 19(4): 17-20 (in Chinese)
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    [10] 高景峰, 彭永臻, 王淑莹. SBR法反硝化过程模糊控制器的设计和碳源投加方式的选择. 环境科学学报, 2003, 23(6): 733-737 Gao Jingfeng, Peng Yongzhen, Wang Shuying. The construction of fuzzy controller of denitrification in SBR process and the choice of carbon addition method. Acta Scientiae Circumstantiae, 2003, 23(6): 733-737 (in Chinese)
    [11] 操家顺, 侯梁浩, 方芳, 等. 温度及外加碳源对生物脱氮除磷过程的影响. 环境工程学报, 2013, 7(6): 2013-2018 Cao Jiashun, Hou Lianghao, Fang Fang, et al. Effect of temperature and external carbon source on simultaneous nitrogen and phosphorus removal. Chinese Journal of Environmental Engineering, 2013, 7(6): 2013-2018 (in Chinese)
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出版历程
  • 收稿日期:  2014-06-27
  • 刊出日期:  2015-02-07
张兰河, 丘晓春, 张宇, 庞香蕊, 刘鹤楠. 碳源投加方式对SBR工艺脱氮速率的影响[J]. 环境工程学报, 2015, 9(2): 731-736. doi: 10.12030/j.cjee.20150237
引用本文: 张兰河, 丘晓春, 张宇, 庞香蕊, 刘鹤楠. 碳源投加方式对SBR工艺脱氮速率的影响[J]. 环境工程学报, 2015, 9(2): 731-736. doi: 10.12030/j.cjee.20150237
Zhang Lanhe, Qiu Xiaochun, Zhang Yu, Pang Xiangrui, Liu Henan. Effect of different adding methods of carbon sources on denitrification rate[J]. Chinese Journal of Environmental Engineering, 2015, 9(2): 731-736. doi: 10.12030/j.cjee.20150237
Citation: Zhang Lanhe, Qiu Xiaochun, Zhang Yu, Pang Xiangrui, Liu Henan. Effect of different adding methods of carbon sources on denitrification rate[J]. Chinese Journal of Environmental Engineering, 2015, 9(2): 731-736. doi: 10.12030/j.cjee.20150237

碳源投加方式对SBR工艺脱氮速率的影响

  • 1. 东北电力大学化学工程学院, 吉林 132012
  • 2. 辽宁大学环境学院, 沈阳 110036
基金项目:

吉林省科技发展计划项目(20130303080SF,20110405)

吉林省省校合作技术开发项目(吉工信科技2011-507)

摘要: 为了提高生物反应器的脱氮效率,研究采用SBR处理模拟生活污水,利用醋酸钠作为碳源,考察碳源投加方式对脱氮速率的影响。结果表明,当温度为10~15℃,进水COD为330~550 mg/L时,采用不同的碳源投加方式,COD去除率均高于95%。进水一次投加2.4 g碳源,COD平均反应速率为5.3 mg/(g·h),平均反硝化速率为0.28 mg/(g·h)。进水、反应器运行3 h时分别投加1.2 g碳源,COD平均反应速率为6.89 mg/(g·h),平均反硝化速率为0.37 mg/(g·h)。进水、反应6 h时分别投加1.2 g碳源,COD平均反应速率为6.50 mg/(g·h),平均反硝化速率为0.52 mg/(g·h)。进水投加1.2 g碳源、反应器运行3 h和6 h时分别投加0.6 g醋酸钠碳源,COD平均反应速率为6.2 mg/(g·h),平均反硝化速率为0.39 mg/(g·h)。分次投加碳源能够提高COD反应速率和TN去除率,同时保持较高的硝化反硝化速率。

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