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UASB启动及不同浓度垃圾渗滤液的处理效果 被引量:8

UASB start-up and treatment effect of landfill leachate with different concentrations
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摘要 在UASB反应器中接种好氧污泥培养厌氧颗粒污泥进行启动,研究不同浓度老龄(13年)垃圾渗滤液对处理效果的影响情况。通过保持进水COD浓度不变、逐步缩短HRT从而提高容积负荷到20 g COD/(L.d)的方法,可以培育出直径为1~3 mm颗粒污泥,最终产气量稳定在60~70 L/d,甲烷含量在50%~70%之间,COD去除率保持在90%左右,污泥层最底部MLSS为50 g/L。逐步提高进水中渗滤液的含量考察其对处理效果的影响,当进水为100%渗滤液时日产气量为500 mL/d、COD去除率仅为10%,表明渗滤液中多为难降解性有机物质。 Treatment of 13 years old of municipal landfill leachate was investigated using UASB reactor which was inoculated with activited sludge as the seed material, 1 - 3 mm anaerobic granular sludge were ob-tained at volumetric loading rate of 20 g COD/( L · d) by keeping the influent COD concentration unchanged and a gradual reduction of the HRT. The final biogas production are 60 - 70 L/d with methane content of 50% 70% , COD removal rate remains about 90% , the MLSS of bottom of the sludge layer is 50 g/L. Comparing treatment efficiency with different concentrations of leachate, COD removal rate is only 10% , biogas production is only 500 mL/d when the influent is completely landfill leachate, indicating that most organic matters in the leachate are recalcitrant.
出处 《环境工程学报》 CAS CSCD 北大核心 2013年第5期1621-1626,共6页 Chinese Journal of Environmental Engineering
基金 国家"水体污染控制与治理"科技重大专项(2012ZX07308-002) 国家自然科学基金资助项目(50808128)
关键词 UASB 老龄垃圾渗滤液 浓度 UASB old landfill leachate concentration
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  • 1刘国涛,彭绪亚,袁荣焕,罗伟,周晓臣.UASB反应器处理城镇有机垃圾浸出液的研究[J].中国给水排水,2006,22(11):40-44. 被引量:9
  • 2Agdag O N, Sponza D T, 2005. Aanaerobic/aerobic treatment of municipal landfill leachate in sequential two-stage upflow sludge blanket reactor(UASB)/completely stirred tank reactor (CSTR) system. Process Biochemistry, 40(2): 895- 902.
  • 3Ahn D H, Yun-Chul C, Won-Seok, 2002a. Use of coagulant and zeolite to enhance biological treatment efficiency of high ammonia leachate. Journal of Environmental Science and Health, 37(2): 163-173.
  • 4Ahn W Y, Kang, M S, Yim S K, Choi K H, 2002b. Advanced landfill leachate treatment using an integrated MBR process. Desalination, 149(2): 109-114.
  • 5APHA, 1995. Standard Methods for the Examination of Water and Wastewater (19th ed.). Washington DC, USA.
  • 6Bdaszczyk M, Mycielski R, Deptuch H J, Brzostek K, 1980. Effect of various sources of organic carbon and high nitrite and nitrateconcentrations on the selection of denitrifying bacteria. Ⅰ. Stationary cultures. Acta Microbiologica polonica, 29(4): 397-406.
  • 7Betlach M R, Tiedje J M, 1981. Kinetic explanation for accumulation of nitrite, nitric oxide and nitrous oxide during bacterial denitrification. Applied and Environmental Microbiology, 42(6): 1074-1084.
  • 8Chen S, Sun D Z, Chung J S, 2007. Simultaneous removal of COD and ammonium from landfill leachate using anaerobic-aerobic moving-bed biofilm reactor system. Waste Management, 28(2): 339-346.
  • 9Chiang L C, Chang J E, Chung C T, 2001. Electrochemical oxidation combined with physical-chemical pretreatment processes for the treatment of refractory landfill leachate. Environmental Engineering Science, 18(6): 363-379.
  • 10Dawson R N, Murphy K L, 1972. The temperature dependency of biological denitirification. Water Research, 6(1 ): 71-83.

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