处理造纸废水的EGSB反应器内颗粒污泥特性

李江, 何强, 孙兴福, 湖澄, TonnySchuit. 处理造纸废水的EGSB反应器内颗粒污泥特性[J]. 环境工程学报, 2013, 7(11): 4255-4258.
引用本文: 李江, 何强, 孙兴福, 湖澄, TonnySchuit. 处理造纸废水的EGSB反应器内颗粒污泥特性[J]. 环境工程学报, 2013, 7(11): 4255-4258.
Li Jiang, He Qiang, Sun Xingfu, Hu Cheng, Tonny Schuit. Granule sludge characteristics of full-scale EGSB reactor treating paper-mill effluents[J]. Chinese Journal of Environmental Engineering, 2013, 7(11): 4255-4258.
Citation: Li Jiang, He Qiang, Sun Xingfu, Hu Cheng, Tonny Schuit. Granule sludge characteristics of full-scale EGSB reactor treating paper-mill effluents[J]. Chinese Journal of Environmental Engineering, 2013, 7(11): 4255-4258.

处理造纸废水的EGSB反应器内颗粒污泥特性

  • 基金项目:
  • 中图分类号: TU992

Granule sludge characteristics of full-scale EGSB reactor treating paper-mill effluents

  • Fund Project:
  • 摘要: 为了解高效厌氧反应器的颗粒污泥特性,研究了生产性EGSB反应器处理造纸废水不同高度的颗粒污泥的固体浓度、外观形态和产甲烷活性。采用甲烷势自动测试系统测试产甲烷活性,测试时间3 d。结果表明,颗粒污泥的固体浓度以及溶解性COD随高度的增加逐渐降低,有机质含量沿整个反应器高度不变。反应器内固体浓度和有机质含量平均值为TS:(123±4) g/L,VS:(75±3) g/L,VS/TS:(61±3)%。溶解性COD浓度由723 mg/L降低到449 mg/L。反应器内的颗粒污泥产甲烷活性为(0.32±0.03) g COD/g VSSd (112 mL CH4/g VSSd)。反应器底部和顶部颗粒污泥的当量直径分别为169 μm和145 μm,颗粒污泥呈椭球状(圆度为2.6)。EGSB反应器内由于进水的上升流速较高,污泥颗粒处于膨胀状态,致使颗粒污泥特性沿反应器高度变化不大。
  • 加载中
  • [1] Perry L. M. Anaerobic waste treatment fundamentals. Public Works, 1964, 95 (9):107-112
    [2] Van Lier J. B., Tilche A., Ahring B.K., et al. New perspectives in anaerobic digestion. Water Science and Technology, 2001, 43(1): 1-18
    [3] 董春娟,王海会,陈素云, 等. EGSB 反应器处理焦化废水的启动试验研究.中国给水排水,2011,27(9):91-94 Dong C. J., Wang H. H., Chen S. Y., et al. Startup experimental research of EGSB reactor for treatment of coking wastewater. China Water & Wastewater, 2011, 27(9):91-94(in Chinese)
    [4] Lin J.G., Chang C.N., Chang S.C. Enhancement of anaerobic digestion of waste activated sludge by alkaline solubilization. Bioresource Technology, 1997,62 (3):85-90
    [5] Appels L., Baeyens J., Degreve J., et al. Principles and potential of the anaerobic digestion of waste-activated sludge. Progress in Energy and Combustion Science, 2008, 34(6): 755-781
    [6] Rajeshwari K.V., Balakrishnan M., Kansal A., et al. State-of-the-art of anaerobic digestion technology for industrial wastewater treatment. Renewable and Sustainable Energy Reviews, 2000, (4):135-156
    [7] 张振家,周伟丽,林荣忱. 膨胀颗粒污泥床处理玉米酒精糟液的生产性试验. 环境科学,2001,22(4):114-116 Zhang Z. J., Zhou W. L., Lin R. C. Full-scale experiment on corn-ethanol production wastewater treatment with the thermophilic EGSB reactor. Environmental Science, 2001, 22(4):114-116 (in Chinese)
    [8] Tchobanoglous G., Burton F.L., Stensel H.D. Wastewater Engineering Treatment and Reuse. New York: McGraw-Hill Science Engineering, 2003
    [9] Van Lier J. B. High-rate anaerobic wastewater treatment: Diversifying from end-of-the-pipe treatment to resource-oriented techniques. Water Science and Technology, 2008, 57(8):1137-1148
    [10] 刘永红,周孝德,谭华安, 等. 生产实践中厌氧颗粒污泥品质评价参数的研究及其实际应用. 环境工程学报, 2010, 4(8): 1729-1734 Liu Y. H., Zhou X. D., Tan H. N., et al. Study and application of assessment parameters for anaerobic granules in practice. Chinese Journal of Environmental Engineering, 2010, 4(8): 1729-1734(in Chinese)
    [11] Mahmoud N., Zeeman G., Gijzen H., et al. Anaerobic sewage treatment in a one-stage UASB reactor and a combined UASB-Digester system. Water Research, 2004, 38(9): 2348-2358
    [12] An Y.Y., Yang F.L., Bucciali B., et al. Municipal wastewater treatment using a UASB coupled with cross-flow membrane filtration. Journal of Environmental Engineering, 2009, 135(2):86-91
    [13] 周洪波, 陈坚, 任洪强, 等. UASB和EGSB反应器中厌氧颗粒污泥生物学特性的比较. 应用与环境生物学报, 2000,6(5):473-476 Zhou H. B., Chen J., Ren H. Q., et al. Comparative on the biological characteristics of anaerobic granular sludges from UASB and EGSB reactors. Chinese Journal of Applied and Environmental Biology, 2000, 6(5):473-476(in Chinese)
    [14] APHA. Standard Methods for the Examination of Water and Wastewater. Washington: American Public Health Association, 2005
    [15] Angelidaki I., Alves M., Bolzonella D., et al. Defining the biomethane potential (BMP) of solid organic wastes and energy crops: A proposed protocol for batch assays. Water Science and Technology, 2009, 59(5): 927-934
    [16] Uemura S., Harada H. Treatment of sewage by a UASB reactor under moderate to low temperature conditions. Bioresource Technology, 2000, 72(3):275-282
    [17] 王妍春,左剑恶,肖晶华. EGSB反应器内厌氧颗粒污泥性质的研究. 中国沼气,2002,20(4): 3-7 Wang Y. C., Zuo J. E., Xiao J. H. A study on characteristics of anaerobic granular sludge in an EGSB reactor. China Biogas, 2002, 20(4): 3-7(in Chinese)
  • 加载中
计量
  • 文章访问数:  1927
  • HTML全文浏览数:  1348
  • PDF下载数:  869
  • 施引文献:  0
出版历程
  • 收稿日期:  2012-09-02
  • 刊出日期:  2013-11-21
李江, 何强, 孙兴福, 湖澄, TonnySchuit. 处理造纸废水的EGSB反应器内颗粒污泥特性[J]. 环境工程学报, 2013, 7(11): 4255-4258.
引用本文: 李江, 何强, 孙兴福, 湖澄, TonnySchuit. 处理造纸废水的EGSB反应器内颗粒污泥特性[J]. 环境工程学报, 2013, 7(11): 4255-4258.
Li Jiang, He Qiang, Sun Xingfu, Hu Cheng, Tonny Schuit. Granule sludge characteristics of full-scale EGSB reactor treating paper-mill effluents[J]. Chinese Journal of Environmental Engineering, 2013, 7(11): 4255-4258.
Citation: Li Jiang, He Qiang, Sun Xingfu, Hu Cheng, Tonny Schuit. Granule sludge characteristics of full-scale EGSB reactor treating paper-mill effluents[J]. Chinese Journal of Environmental Engineering, 2013, 7(11): 4255-4258.

处理造纸废水的EGSB反应器内颗粒污泥特性

  • 1. 重庆大学三峡库区生态环境教育部重点实验室, 重庆 400045
  • 2. 代尔夫特理工大学卫生工程系, 代尔夫特, 荷兰
基金项目:

摘要: 为了解高效厌氧反应器的颗粒污泥特性,研究了生产性EGSB反应器处理造纸废水不同高度的颗粒污泥的固体浓度、外观形态和产甲烷活性。采用甲烷势自动测试系统测试产甲烷活性,测试时间3 d。结果表明,颗粒污泥的固体浓度以及溶解性COD随高度的增加逐渐降低,有机质含量沿整个反应器高度不变。反应器内固体浓度和有机质含量平均值为TS:(123±4) g/L,VS:(75±3) g/L,VS/TS:(61±3)%。溶解性COD浓度由723 mg/L降低到449 mg/L。反应器内的颗粒污泥产甲烷活性为(0.32±0.03) g COD/g VSSd (112 mL CH4/g VSSd)。反应器底部和顶部颗粒污泥的当量直径分别为169 μm和145 μm,颗粒污泥呈椭球状(圆度为2.6)。EGSB反应器内由于进水的上升流速较高,污泥颗粒处于膨胀状态,致使颗粒污泥特性沿反应器高度变化不大。

English Abstract

参考文献 (17)

返回顶部

目录

/

返回文章
返回