矿化污泥生物反应器处理生活垃圾填埋场老龄渗滤液

史昕龙, 刘勇弟, 魏云梅. 矿化污泥生物反应器处理生活垃圾填埋场老龄渗滤液[J]. 环境工程学报, 2013, 7(6): 2371-2377.
引用本文: 史昕龙, 刘勇弟, 魏云梅. 矿化污泥生物反应器处理生活垃圾填埋场老龄渗滤液[J]. 环境工程学报, 2013, 7(6): 2371-2377.
Shi Xinlong, Liu Yongdi, Wei Yunmei. Aged landfill leachate treatment by aged sludge-based bioreactor[J]. Chinese Journal of Environmental Engineering, 2013, 7(6): 2371-2377.
Citation: Shi Xinlong, Liu Yongdi, Wei Yunmei. Aged landfill leachate treatment by aged sludge-based bioreactor[J]. Chinese Journal of Environmental Engineering, 2013, 7(6): 2371-2377.

矿化污泥生物反应器处理生活垃圾填埋场老龄渗滤液

  • 基金项目:

    上海市科委2010年度科技创新行动计划社会发展领域重大科技项目(10DZ1200104,10DZ1200005)

  • 中图分类号: X705

Aged landfill leachate treatment by aged sludge-based bioreactor

  • Fund Project:
  • 摘要: 经长时间稳定化形成的矿化污泥中,含有种类丰富和数量繁多的降解性微生物,具有处理渗滤液的潜力。建立3个矿化污泥生物反应器, 即C1(粉煤灰0%),C2(粉煤灰9.1%),C3(粉煤灰16.7%),以处理垃圾填埋场老龄渗滤液。在单级矿化污泥反应器中,当进水COD和 NH3-N分别约为1350和900 mg/L时,水力负荷为17.7~70.8 L/(m3·d),COD去除率可超过65%,氨氮的去除率可超过94%。粉煤灰的加入一定程度上降低了COD去除率,但有助于氨氮的去除。在二级矿化污泥生物反应器中(即C3~C1串联),水力负荷为35.4 L/(m3·d)的工况下,当COD、TOC、IC和NH3-N分别为1 500~2 500,500~900,1 200~1 600和1 200~1 450 mg/L时,出水可达到COD3-N<5 mg/L。但是,矿化污泥生物反应器对渗滤液总氮的去除率较低,仅为20%左右。
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    [5] 简放陵, 刘洁萍, 叶新方, 等. 垃圾渗滤液物化处理研究. 环境工程学报, 2007,1(3):116-118 Jian F. L., Liu J. P., Yue X. F., et al. Research on physical and chemical treatment of municipal solid waste landfill leachate. China Journal of Environmental Engineering, 2007,1(3):116-118(in Chinese)
    [6] Kheradmand S., Karimi-Jashni A., Sartaj M. Treatment of municipal landfill leachate using a combined anaerobic digester and activated sludge system. Waste Management, 2010,30(6):1025-1031
    [7] De Morais J. L., Zamora P. P. Use of advanced oxidation processes to improve the biodegradability of mature landfill leachates. Journal of Hazardous Materials, 2005,123(1-3),181-186
    [8] Foo K. Y., Hameed B. H. An overview of landfill leachate treatment via activated carbon adsorption process. Journal of Hazardous Materials, 2009,171(1-3):54-60
    [9] 楼紫阳, 赵由才, 张全. 渗滤液处理处置技术及工程实例. 北京:化学工业出版社, 2006
    [10] Renou S., Givaudan J. G., Poulain S., et al. Landfill leachate treatment: Review and opportunity. Journal of Hazardous Materials, 2008,150(3),468-93
    [11] 位菁, 张彩香, 马腾. 混凝去除垃圾渗滤液中DOM的实验研究. 环境科学与技术, 2007,30(8):1-2 Wei J., Zhang C. X., Ma T. Removal of DOM in leachate by coagulation. Environmental Science and Technology, 2007,30(8):1-2(in Chinese)
    [12] 王宝贞, 王承武, 杨铨大, 等. A(缺氧活性污泥)/B(A/O淹没式生物膜)复合系统处理垃圾填埋场渗沥液.给水排水,1996,22(5):15-18 Wang B. Z., Wang C.W., Yang S. D., et al. Composite system of anoxic activated sludge submerged A/O biofilm to treat urban domestic refuse infiltration liquid. Water & Wastewater Engineering, 1996,22(5):15-18(in Chinese)
    [13] 郭广寨,苏良湖,孙旭, 等.不同粒径零价铁(ZVI)对污水污泥H2S和CH4释放速率的影响. 环境工程学报,2012,6(5):1693-1698 Guo G. Z., Su L. H., Sun X., et al. Effect of different particle sizes of zero-valent iron (ZVI) on H2S and CH4 emission in sewage sludge. China Journal of Environmental Engineering, 2012,6(5):1693-1698(in Chinese)
    [14] Zhen G. Y., Yan X. F., Zhou H. Y., et al. Effects of calcined aluminum salts on the advanced dewatering and solidification/stabilization of sewage sludge. Journal of Environmental Sciences, 2011,23(7):1225-1232
    [15] 张云霞, 王瑞, 王立彤, 等. 填埋方式对污泥填埋稳定性的影响. 中国给水排水, 2011,27(11):75-77 Zhang Y. X., Wang R., Wang L. T., et al. Influence of landfill modes on stabilization of sludge landfill. China Water & Wastewater, 2011,27(11):75-77(in Chinese)
    [16] 朱英. 卫生填埋场中污泥降解与稳定化过程研究. 上海:同济大学博士学位论文, 2008 Zhu Y. Sludge biodegradation and stabilization process in the sanitary landfill. Shanghai: Doctoral Dissertation of Tongji University, 2008(in Chinese)
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    [18] 马建立, 魏云梅, 赵由才. 矿化污泥基质分析及作为生物填料可行性研究. 新农村建设与环境保护:华北五省市区环境科学学会第十六届学术年会, 秦皇岛,2009.495-500 Ma J.L., Wei Y.M., Zhao Y.C. Characterization of aged sludge and its feasibility as bio-filler. Sixteenth Annual Conference of the Society of Environmental Science of the Five Provinces and Municipalities in North China:New Rural Construction and Environmental Protection, Qinhuangdao,2009.495-500(in Chinese)
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出版历程
  • 收稿日期:  2013-03-27
  • 刊出日期:  2013-06-11
史昕龙, 刘勇弟, 魏云梅. 矿化污泥生物反应器处理生活垃圾填埋场老龄渗滤液[J]. 环境工程学报, 2013, 7(6): 2371-2377.
引用本文: 史昕龙, 刘勇弟, 魏云梅. 矿化污泥生物反应器处理生活垃圾填埋场老龄渗滤液[J]. 环境工程学报, 2013, 7(6): 2371-2377.
Shi Xinlong, Liu Yongdi, Wei Yunmei. Aged landfill leachate treatment by aged sludge-based bioreactor[J]. Chinese Journal of Environmental Engineering, 2013, 7(6): 2371-2377.
Citation: Shi Xinlong, Liu Yongdi, Wei Yunmei. Aged landfill leachate treatment by aged sludge-based bioreactor[J]. Chinese Journal of Environmental Engineering, 2013, 7(6): 2371-2377.

矿化污泥生物反应器处理生活垃圾填埋场老龄渗滤液

  • 1.  华东理工大学资源与环境工程学院, 上海 200237
  • 2.  上海环境实业有限公司, 上海 200060
  • 3.  同济大学污染控制与资源化研究国家重点实验室, 上海 200092
基金项目:

上海市科委2010年度科技创新行动计划社会发展领域重大科技项目(10DZ1200104,10DZ1200005)

摘要: 经长时间稳定化形成的矿化污泥中,含有种类丰富和数量繁多的降解性微生物,具有处理渗滤液的潜力。建立3个矿化污泥生物反应器, 即C1(粉煤灰0%),C2(粉煤灰9.1%),C3(粉煤灰16.7%),以处理垃圾填埋场老龄渗滤液。在单级矿化污泥反应器中,当进水COD和 NH3-N分别约为1350和900 mg/L时,水力负荷为17.7~70.8 L/(m3·d),COD去除率可超过65%,氨氮的去除率可超过94%。粉煤灰的加入一定程度上降低了COD去除率,但有助于氨氮的去除。在二级矿化污泥生物反应器中(即C3~C1串联),水力负荷为35.4 L/(m3·d)的工况下,当COD、TOC、IC和NH3-N分别为1 500~2 500,500~900,1 200~1 600和1 200~1 450 mg/L时,出水可达到COD3-N<5 mg/L。但是,矿化污泥生物反应器对渗滤液总氮的去除率较低,仅为20%左右。

English Abstract

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