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厌氧生物法处理高浓度酸性硫酸盐废水研究 被引量:6

Research on treatment of high concentration sulfate acidic wastewater by an anaerobic bioreactor
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摘要 以厌氧移动床生物膜反应器处理高浓度酸性硫酸盐废水,考察了生长因子B对体系pH缓冲能力和SO42-去除率影响。实验证明,加入生长因子后,可使进水pH值从6.80降到3.08,出水pH稳定在6.78±0.5,此pH下SO42-去除率比单一葡萄糖为碳源提高5.72倍。在半连续试验确定的体系最佳运行参数下连续运行试验,SO42-、CODCr去除率分别从85.17%、74.05%增至95.66%和88.56%,148 d负荷试验后,进水SO42-浓度从500 mg/L增加至2 876 mg/L时,出水SO42-浓度均在238.42 mg/L以下,SO42-的去除率稳定在90%以上,处理SO42-浓度最高可达3 580 mg/L。该体系在加入生长因后,可处理高浓度的酸性硫酸盐废水。 Anaerobic moving bed biofilm reactor was used to deal with the high concentration sulfate acidic wastewater.The effect of growth factor-B on pH buffering capacity of the system and SO4^2- removal rate was researched.The results show that the influent pH decreased from 6.80 to 3.08 while the growth factor-B was added,the effluent pH was stabilized on 6.78±0.5 and SO4^2- removal rate was 5.72 times higher than single glucose as the carbon source without growth factor-B.Based on continuous operation test under the best operating parameters in the semi-continuous operation test,the results show that the removal rates of SO4^2- and CODCr increased from 85.17% to 95.66% and 74.05% to 88.56%,respectively.Operating the load test for 148 days,the results show that the influent SO4^2-concentration increased from 500 mg/L to 2 876 mg/L,the effluent was below 238.42mg/L,the SO4^2- removal rate was above 90%,the highest concentration of SO4^2- can be treated up to 3 580 mg/L.So the systems can treat high concentration sulfate acidic wastewater when growth factor B was added to it.
出处 《世界地质》 CAS CSCD 2008年第3期310-313,344,共5页 World Geology
基金 吉林省科学技术厅资助项目(20000124) 校企合作资助项目:集安市利源黄金有限责任公司资助项目
关键词 厌氧移动床生物膜反应器 高浓度酸性硫酸盐废水 生长因子B anaerobic moving bed biofilm reactor high concentration sulfate acidic wastewater growth factor-B
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参考文献7

  • 1Burckhard S R, Schwab A P, Banks M K. The effects of organic acids on the leaching of heavy metals from Mine Tailings [J]. Journal of Hazardous Materials, 1995, 41 : 135-145.
  • 2Kaksonen A H, Riekkola-Vanhanen M L, Puhakka J A. Optimization of metal sulphide precipitation in fluidizedbed treatment of acidic wastewater [ J]. Wat Res, 2003, 37 : 255-266.
  • 3赵宇华,叶央芳,刘学东.硫酸盐还原菌及其影响因子[J].环境污染与防治,1997,19(5):41-43. 被引量:104
  • 4王爱杰,任南琪,杜大仲,徐潇文,吴丽红.硫酸盐还原过程中乙酸型代谢方式的形成及其稳定性[J].环境科学,2004,25(2):73-76. 被引量:17
  • 5Van Houten R T, Hulshoff Pol L W, Lettinga G. Biological sulphate reduction using gaslift reactor fed with hydrogen and carbon dioxide as energy and carbon source [ J ]. Biotech Bioeng, 1994, 44 (5): 586-594.
  • 6Maree J P, Strydom W F. Biological sulfate removal from industrial effluent in an up flow packed bed reactor [ J ]. Wat Res, 1987, 21 (2) : 141-146.
  • 7Maree J P, Hulse G. Pilot plant studies from industrial effluent [J]. Wat Sci Tech, 1991, 23: 1293-1300.

二级参考文献10

  • 1任南琪.一体化有机废水处理产酸发酵设备[P].中国专利:982408013.1998-09-21.
  • 2Czako L. Biological Sulfate Removal in the Acidic Phase of Anaerobic Digestion[A]. Fifth International symposium on Anaerobic Digestion (Poster Papers), Bologna, Italy: 1988, 833-837.
  • 3Reis M A M. Sulfate Reduction in Acidogenic Phase Anaerobic Digestion[A]. Proc. Int. Conf. on Water and Wastewater, Microbial, Cam, USA, 1988, 58: 1-7.
  • 4Sarner E. The ANTRIC Filter-A Novel Process for Sulphur Removal and Recovery[A]. Fifth International Symposium on Anaerobic Digestion (Poster Papers), Bologna, Italy: 1988, 889-892.
  • 5Gao Yan. Anaerobic Digestion of High Strength Wastewaters containing High Levels of sulfate[D]. England:Univ. of Newcastle upon Tyne, 1989.
  • 6SY/T0532-93.中国石油天然气行业标准:油田注入水细菌分析方法-绝迹稀释法(S).[S].,..
  • 7Postgate J R. The sulfate reducing Bacteria[M]. UK:Cambridge University Press, 1984.
  • 8Cohen A. Anaerobic digestion of glucose with separated acid production and methane formation[J]. Wat. Res., 1979, 13: 571-580.
  • 9俞汉青,陈国中.含硫酸盐工业有机废水的处理方法[J].工业水处理,1991,11(5):12-14. 被引量:7
  • 10左剑恶,胡纪萃.含硫酸盐有机废水的厌氧生物处理[J].环境科学,1991,12(3):67-71. 被引量:38

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