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厌氧复合床反应器处理高浓度硫酸盐有机废水 被引量:4

Combined anaerobic reactor for the treatment of organic wastewater containing highly concentrated sulfate
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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%。 After the study on the competition mechanism of 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 SO4^2- is 1 000- 1 600 mg/L, i. e. volumetric loading rate is 1 - 1.6 kg/(m^3-d) ,effluent SO4^2- maintains 140 mg/L, and the average removal rate is 88.6%.
出处 《工业水处理》 CAS CSCD 北大核心 2007年第3期16-18,共3页 Industrial Water Treatment
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 combined anaerobic reactor organic wastewater containing highly concentrated sulfate sulfate reducing bacteria methanogen
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参考文献3

  • 1冀滨弘,章非娟,史平.硫酸盐有机废水厌氧处理工艺的试验研究[J].给水排水,2003,29(8):46-50. 被引量:6
  • 2Pomeroy R,Bowlus F D.Process report on sulphide control research[J].Sew Works,1946,18:597-640.
  • 3Harada H,Vemura S,Moraonoi K.Interaction between sulfate-reducing bacteria and methane-producing bacteria in UASB reactors feed with low strength wastes containing different levels of sulfate[J].Water Res.,1994,28(2):355 -376.

二级参考文献4

  • 1Isa Z, et al. Sulphate reduction relative to methane production in High-rate Anaerobic Digestion. Technical Aspects, (Appl) Environ Microbiol, 1986, 51( 3 ) : 572 -- 579.
  • 2Isa Z, et al. Sulphate reduction relative to methane production in High-rate Anaerobic Digestion. Microbiological Aspects, (Appl) Environ Microbiol, 1986, 51(3) :580--587.
  • 3Pomeroy R, F D Bowlus. Process report on sulphide control reseach.Sew Works, 1946,18:597--640.
  • 4Harada H, Vemura S, Moraonoi K. Interaction between sulfate-reducing bacteria and mathane-produeing bacteria in UASB reactors feed with low strength wastes containing different levels of sulfate.Water Res, 1994, 28 (2) :355--376.

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