SBR工艺用于焦化纳滤浓盐水生物脱氮

李恩超, 王治立, 金学文, 吕树光, 侯红娟, 尹婷婷. SBR工艺用于焦化纳滤浓盐水生物脱氮[J]. 环境工程学报, 2015, 9(8): 3854-3858. doi: 10.12030/j.cjee.20150843
引用本文: 李恩超, 王治立, 金学文, 吕树光, 侯红娟, 尹婷婷. SBR工艺用于焦化纳滤浓盐水生物脱氮[J]. 环境工程学报, 2015, 9(8): 3854-3858. doi: 10.12030/j.cjee.20150843
Li Enchao, Wang Zhili, Jin Xuewen, Lü Shuguang, Hou Hongjuan, Yin Tingting. Biological denitrification for nanofiltration concentrate from coking wastewater by SBR process[J]. Chinese Journal of Environmental Engineering, 2015, 9(8): 3854-3858. doi: 10.12030/j.cjee.20150843
Citation: Li Enchao, Wang Zhili, Jin Xuewen, Lü Shuguang, Hou Hongjuan, Yin Tingting. Biological denitrification for nanofiltration concentrate from coking wastewater by SBR process[J]. Chinese Journal of Environmental Engineering, 2015, 9(8): 3854-3858. doi: 10.12030/j.cjee.20150843

SBR工艺用于焦化纳滤浓盐水生物脱氮

  • 基金项目:
  • 中图分类号: X703

Biological denitrification for nanofiltration concentrate from coking wastewater by SBR process

  • Fund Project:
  • 摘要: 以焦化废水超滤/纳滤/反渗透的"三膜法"深度处理工艺产生的高电导率纳滤(NF)浓盐水为研究对象,采用SBR脱氮工艺对NF浓盐水中有机污染物和总氮(TN)的去除性能进行了研究。实验结果表明,SBR脱氮工况为进水5 min,缺氧搅拌8 h,好氧曝气12 h,静置2 h,出水5 min,闲置1 h 50 min,污泥浓度(MLSS)为3 000 mg/L左右时,TN平均去除率为45.45%,COD平均去除率为45.36%。通过烧杯实验研究了不同C/N比对反硝化脱氮效率的影响及其中氮形态的变化,在C/N为4:1时,出水TN可降低至14.8 mg/L,其中NO3--N为5.0 mg/L。研究结果证明,SBR可将电导率为12 000~16 000 μS/cm的焦化纳滤浓盐水TN降低至15 mg/L以下。
  • 加载中
  • [1] Qian Yi, Wen Yibo, Zhang Huiming. Efficacy of pre-treatment methods in the activated sludge removal of refractory compounds in coke-plant wastewater. Water Research, 1994, 28(3): 701-707
    [2] 李登勇, 潘霞霞, 吴超飞, 等. 氧化/吸附/混凝协同工艺处理焦化废水生物处理出水的过程及效果分析. 环境工程学报, 2010, 4(8): 1719-1725 Li Dengyong, Pan Xiaxia, Wu Chaofei, et al. Process and effectiveness analysis of treatment of biologically treated coking wastewater by oxidation/adsorption/coagulation. Chinese Journal of Environmental Engineering, 2010, 4(8): 1719-1725 (in Chinese)
    [3] Zhang Min, Tay J. H., Qian Yi, et al. Coke plant wastewater treatment by fixed biofilm system for COD and NH3-N removal. Water Research, 1998, 32(2): 519-527
    [4] Ghose M. K. Complete physico-chemical treatment for coke plant effluents. Water Research, 2002, 36(5): 1127-1134
    [5] Minhalma M., de Pinho M. N. Development of nanofiltration/steam stripping sequence for coke plant wastewater treatment. Desalination, 2002, 149(1-3): 95-100
    [6] 金学文, 李恩超, 江一君, 等. 反渗透膜工艺用于焦化废水深度处理的实验研究. 水处理技术, 2014, 40(4): 59-62 Jing Xuewen, Li Enchao, Jiang Yijun, et al. Advanced treatment of coking wastewater by reverse osmosis process. Technology of Water Treatment, 2014, 40(4): 59-62 (in Chinese)
    [7] 阮燕霞, 魏宏斌, 任国栋, 等. 双膜法深度处理焦化废水的中试研究. 中国给水排水, 2014, 30(17): 82-84 Ruan Yanxia, Wei Hongbin, Ren Guodong, et al. Advanced treatment of coking wastewater by double membrane method. China Water & Wastewater, 2014, 30(17): 82-84 (in Chinese)
    [8] 闻晓今, 周正, 魏钢, 等. 超滤-纳滤对焦化废水深度处理的试验研究. 水处理技术, 2010, 36(3): 93-95 Wen Xiaojin, Zhou Zheng, Wei Gang, et al. Experimental study on advanced treating process of coking wastewater by UF and RO. Technology of Water Treatment, 2010, 36(3): 93-95 (in Chinese)
    [9] Minhalma M., de Pinho M. N. Integration of nanofiltration/steam stripping for the treatment of coke plant ammoniacal wastewaters. Journal of Membrane Science, 2004, 242(1-2): 87-95
    [10] Jin Xuewen, Li Enchao, Lu Shuguang, et al. Coking wastewater treatment for industrial reuse purpose: Combining biological processes with ultrafiltration, nanofiltration and reverse osmosis. Journal of Environmental Sciences, 2013, 25(8): 1565-1574
    [11] 金学文, 李恩超, 吕树光, 等. 膜工艺深度处理焦化废水的可行性实践研究. 环境污染与防治, 2013, 35(11): 77-81 Jing Xuewen, Li Enchao, Lü Shuguang, et al. Practical research on advanced treatment of coking wastewater by membrane process. Environmental Pollution and Control, 2013, 35(11): 77-81 (in Chinese)
    [12] 穆明明, 左青. 全膜法在焦化废水回用的应用. 工业水处理, 2015, 35(1): 97-100 Mu Mingming, Zuo Qing. Application of membrane process to coking wastewater reuse. Industrial Water Treatment, 2015, 35(1): 97-100 (in Chinese)
    [13] Marañón E., Vázquez I., Rodríguez J., et al. Treatment of coke wastewater in a sequential batch reactor (SBR) at pilot plant scale. Bioresource Technology, 2008, 99(10): 4192-4198
    [14] Glass C., Silverstein J. Denitrification of high-nitrate, high-salinity wastewater. Water Research, 1999, 33(1): 223-229
    [15] Uygur A., Kargı F. Salt inhibition on biological nutrient removal from saline wastewater in a sequencing batch reactor. Enzyme and Microbial Technology, 2004, 34(3-4): 313-318
    [16] 崔有为, 王淑莹, 孔祥智, 等. 活性污泥处理系统抗盐度冲击的能力. 中国给水排水, 2003, 19(11): 12-15 Cui Youwei, Wang Shuying, Kong Xiangzhi, et al. Resistance to salinity shock in activated sludge treatment system. China Water & Wastewater, 2003, 19(11): 12-15 (in Chinese)
    [17] 魏复盛. 水和废水监测分析方法(第4版). 北京: 中国环境科学出版社, 2002
  • 加载中
计量
  • 文章访问数:  2329
  • HTML全文浏览数:  1763
  • PDF下载数:  681
  • 施引文献:  0
出版历程
  • 收稿日期:  2015-05-22
  • 刊出日期:  2015-08-13
李恩超, 王治立, 金学文, 吕树光, 侯红娟, 尹婷婷. SBR工艺用于焦化纳滤浓盐水生物脱氮[J]. 环境工程学报, 2015, 9(8): 3854-3858. doi: 10.12030/j.cjee.20150843
引用本文: 李恩超, 王治立, 金学文, 吕树光, 侯红娟, 尹婷婷. SBR工艺用于焦化纳滤浓盐水生物脱氮[J]. 环境工程学报, 2015, 9(8): 3854-3858. doi: 10.12030/j.cjee.20150843
Li Enchao, Wang Zhili, Jin Xuewen, Lü Shuguang, Hou Hongjuan, Yin Tingting. Biological denitrification for nanofiltration concentrate from coking wastewater by SBR process[J]. Chinese Journal of Environmental Engineering, 2015, 9(8): 3854-3858. doi: 10.12030/j.cjee.20150843
Citation: Li Enchao, Wang Zhili, Jin Xuewen, Lü Shuguang, Hou Hongjuan, Yin Tingting. Biological denitrification for nanofiltration concentrate from coking wastewater by SBR process[J]. Chinese Journal of Environmental Engineering, 2015, 9(8): 3854-3858. doi: 10.12030/j.cjee.20150843

SBR工艺用于焦化纳滤浓盐水生物脱氮

  • 1.  华东理工大学, 国家环境保护化工过程环境风险评价与控制重点实验室, 上海 200237
  • 2.  宝山钢铁股份有限公司, 上海 201900
基金项目:

摘要: 以焦化废水超滤/纳滤/反渗透的"三膜法"深度处理工艺产生的高电导率纳滤(NF)浓盐水为研究对象,采用SBR脱氮工艺对NF浓盐水中有机污染物和总氮(TN)的去除性能进行了研究。实验结果表明,SBR脱氮工况为进水5 min,缺氧搅拌8 h,好氧曝气12 h,静置2 h,出水5 min,闲置1 h 50 min,污泥浓度(MLSS)为3 000 mg/L左右时,TN平均去除率为45.45%,COD平均去除率为45.36%。通过烧杯实验研究了不同C/N比对反硝化脱氮效率的影响及其中氮形态的变化,在C/N为4:1时,出水TN可降低至14.8 mg/L,其中NO3--N为5.0 mg/L。研究结果证明,SBR可将电导率为12 000~16 000 μS/cm的焦化纳滤浓盐水TN降低至15 mg/L以下。

English Abstract

参考文献 (17)

返回顶部

目录

/

返回文章
返回