工业水处理 ›› 2007, Vol. 27 ›› Issue (3): 16-18. doi: 10.11894/1005-829x.2000.20(4).16

• 试验研究 • 上一篇    下一篇

厌氧复合床反应器处理高浓度硫酸盐有机废水

冯雷雨1,2, 孙力平2, 严媛媛2, 张艳3   

  1. 1. 同济大学污染控制与资源化研究国家重点实验室, 上海 200092;
    2. 天津城市建设学院环境与市政工程系, 天津 300384;
    3. 天津创业环保股份有限公司, 天津 300381
  • 收稿日期:2006-10-20 出版日期:2007-03-20 发布日期:2010-10-01
  • 作者简介:冯雷雨(1979- ), 同济大学在读博士生。E-mail: fengleiyu2001@yahoo.com.cn。

Combined anaerobic reactor for the treatment of organic was tewater containing highly concentrated sulfate

Feng Leiyu1,2, Sun Liping2, Yan Yuanyuan2, Zhang Yan3   

  1. 1. State Key Laboratory of Pollution Control and Resources Reuse, Tongji University, Shanghai 200092, China;
    2. Department of Municipal and Environmental Engineering, Tianjin Institute of Urban Construction, Tianjin 300384, China;
    3. Tianjin Capital Environmental Protection Co., Ltd., Tianjin 300381, China
  • Received:2006-10-20 Online:2007-03-20 Published:2010-10-01

摘要:

通过对硫酸盐还原菌与产甲烷菌的竞争机制、硫酸盐还原产物的影响以及反应器运行性能等方面的研究,认为厌氧复合床反应器处理高硫酸盐有机废水是可行的。当进水硫酸盐质量浓度为1000~1600mg/L时,即SO42-容积负荷为1~1.6kg/(m3·d)时,出水硫酸盐质量浓度为140mg/L左右,平均去除率为88.6%。

关键词: 厌氧复合床反应器, 高浓度硫酸盐有机废水, 硫酸盐还原菌, 产甲烷菌

Abstract:

After the study on the competition mechanismof sulfate reducing bacteri a(SRB) and methanogens(MPB), the impact of reducing product of sulfate and the operational performance of reactor,etc.,combined anaerobic reactor is considered feasible for treating organic wastewater containing highly concentrated sulfate.When the influent SO2-4 is 1 000-1 600 mg/L, i. e. volumetric loading rate is 1-1.6 kg/(m3·d),effluent SO4 2-maintains 140 mg/L,and the average removal rate is 88.6%.

Key words: combined anaerobic reactor, organic wastewater containing highly concentrated sulfate, sulfatereducing bacteria, methanogen

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