厌氧折流板反应器处理邻苯二甲酸二丁酯废水

刘霖, 王平, 王小伟. 厌氧折流板反应器处理邻苯二甲酸二丁酯废水[J]. 环境工程学报, 2013, 7(9): 3375-3379.
引用本文: 刘霖, 王平, 王小伟. 厌氧折流板反应器处理邻苯二甲酸二丁酯废水[J]. 环境工程学报, 2013, 7(9): 3375-3379.
Liu Lin, Wang Ping, Wang Xiaowei. Treatment of di-n-butyl phthalate wastewater by an anaerobic baffled reactor[J]. Chinese Journal of Environmental Engineering, 2013, 7(9): 3375-3379.
Citation: Liu Lin, Wang Ping, Wang Xiaowei. Treatment of di-n-butyl phthalate wastewater by an anaerobic baffled reactor[J]. Chinese Journal of Environmental Engineering, 2013, 7(9): 3375-3379.

厌氧折流板反应器处理邻苯二甲酸二丁酯废水

  • 基金项目:

    国家自然科学基金面上项目(31270680)

    江苏省"六大人才高峰"第八批高层次人才项目(2011-XCL-018)

    江苏高校优势学科(环境科学与工程)建设工程资助项目

  • 中图分类号: X703

Treatment of di-n-butyl phthalate wastewater by an anaerobic baffled reactor

  • Fund Project:
  • 摘要: 采用南京江心洲污水处理厂的厌氧消化污泥作为厌氧折流板反应器(ABR)的接种污泥,研究室温(25±5)℃条件下ABR对邻苯二甲酸二丁酯(DBP)降解的运行特性。结果表明,ABR在室温、容积负荷为0.9~1.8 kg/(m3·d)条件下启动运行30 d可以达到运行稳定,其COD去除率在90%左右。在负荷提高阶段,当水力停留时间(HRT)为12 h,容积负荷为2.0~6.8 kg/(m3·d)时,反应器对COD平均去除率大于85%;当HRT为12 h,容积负荷6.8 kg/(m3·d)时,COD去除率达90.7%,DBP降解率达87.3%。
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  • [1] Bajt O., Mailhot G., Bolte M. Degradation of dibutyl phthalate by homogeneous photocatalysis with Fe(Ⅲ) in aqueous solution. Applied Catalysis B:Environmental, 2001, 33(3): 239-248
    [2] Xu B., Gao N. Y., Cheng H., et al. Oxidative degradation of dimethyl phthalate(DMP) by UV/H2O2 process. Journal of Hazardous Materials, 2009, 162(3): 954-959
    [3] Li L., Ye W., Zhang Q., et al. Catalytic ozonation of dimethyl phthalate over cerium supported on activated carbon. Journal of Hazardous Materials, 2009, 170(1): 411-416
    [4] 赵文华, 赵冬梅, 徐春涛. 环境中PAEs的分析方法研究. 江西化工, 2009, 26(4): 30-34 Zhao Wenhua, Zhao Dongmei, Xu Chuntao. Analytical methods of phthalate esters in environment. Jiangxi Chemical Industry, 2009, 26(4): 30-34(in Chinese)
    [5] William P., David S. The use of the anaerobic baffled reactor ABR for waste water treatment: A rview. Water Research, 1999, 33(7): 1559-1578
    [6] Wang Y. Y., Fan Y. Z., Gu J. D. Dimethyl phthalate ester degradation by two planktonic and immobilized bacterial consortia. International Biodeterioration & Biodegradation, 2004, 53(2): 93-103
    [7] 郑晓英, 周玉文, 王俊安. 城市污水处理厂中领苯二甲酸酯的研究. 给水排水, 2006, 32(3): 19-22 Zheng Xiaoying, Zhou Yuwen, Wang Junan. Study on the behavior of phthalate acid esters at municipal sewage treatment plant. Water & Wastewater Engineering, 2006, 32(3): 19-22(in Chinese)
    [8] Venkata M. S., Shailaja S., Rama K. M., et al. Adsorptive removal of phthalate ester(di-ethyl phthalate) from aqueous phase by activated carbon: A Kinetic study. Journal of Hazardous Materials, 2007, 146(1-2): 278-282
    [9] Li L., Zhu W., Chen L., et al. Photocatalytic ozonation of dibutyl phthalate over TiO2 film. Journal of Photochemistry and Photobiology A:Chemistry, 2005, 175(2-3): 172-177
    [10] 费学宁, 姜远光, 吕岩, 等. 环境激素邻苯二甲酸酯的光催化降解机理探讨. 应用化学, 2006, 23(1): 59-62 Fei Xuening, Jiang Yuanguang, Lo Yan, et al. Photocatalytic degradation of dibutyl phthalate in aqueous TiO2 suspension. Chinese Journal of Applied Chemistry, 2006, 23(1): 59-62(in Chinese)
    [11] 徐金兰, 王志盈, 李贺. 厌氧折流板反应器(ABR)的工艺特征与处理性能. 西安建筑科技大学学报, 2002, 34(4): 362-365 Xu Jinlan,Wang Zhiying,Li He. Characteristics of the an aerobic baffled reactor(ABR)and applicability of the organic wastewater treatment. Journal of Xi'an University of Architecture & Technology, 2002, 34(4): 362-365(in Chinese)
    [12] 李清雪, 贺晶晶, 赵海萍. 厌氧折流板反应器处理高含量有机废水的启动试验研究. 河北师范大学学报, 2009, 33(2): 224-226 Li Qingxue, He Jingjing, Zhao Haiping. Start-up research on treating high-strength organic wastewater by anaerobic baffled reactor. Journal of Hebei Normal University, 2009, 33(2): 224-226(in Chinese)
    [13] 王建龙, 钱易. 邻苯二甲酸酯的生物降解研究. 环境科学, 1995, 16(6): 26-28 Wang Jianlong, Qian Ti. Microbial degradation of phthalic acid esters. Environmental Science, 1995, 16(6): 26-28(in Chinese)
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出版历程
  • 收稿日期:  2012-06-06
  • 刊出日期:  2013-09-15

厌氧折流板反应器处理邻苯二甲酸二丁酯废水

  • 1. 南京林业大学化学工程学院, 南京 210037
基金项目:

国家自然科学基金面上项目(31270680)

江苏省"六大人才高峰"第八批高层次人才项目(2011-XCL-018)

江苏高校优势学科(环境科学与工程)建设工程资助项目

摘要: 采用南京江心洲污水处理厂的厌氧消化污泥作为厌氧折流板反应器(ABR)的接种污泥,研究室温(25±5)℃条件下ABR对邻苯二甲酸二丁酯(DBP)降解的运行特性。结果表明,ABR在室温、容积负荷为0.9~1.8 kg/(m3·d)条件下启动运行30 d可以达到运行稳定,其COD去除率在90%左右。在负荷提高阶段,当水力停留时间(HRT)为12 h,容积负荷为2.0~6.8 kg/(m3·d)时,反应器对COD平均去除率大于85%;当HRT为12 h,容积负荷6.8 kg/(m3·d)时,COD去除率达90.7%,DBP降解率达87.3%。

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