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碳氮比对气水交替式膜生物反应器同步脱氮除碳的影响 被引量:2

Effect of 碳氮 ratio on simultaneous removal of carbon and nitrogen by a gas-water alternate membrane bioreactor
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摘要 为确定气水交替式膜生物反应器(AMBR)处理污水时的适宜碳氮比,实现较好的同步脱氮除碳效果,构建以2片亲水性聚丙烯中空纤维膜轮流作为曝气膜和出水膜的AMBR,在150 d连续运行的时间内,考察碳氮比对AMBR处理模拟生活污水同步脱氮除碳的影响.结果表明:将混合液中DO的质量浓度控制在0.5 mg/L左右,进水COD和NH4+-N质量浓度分别为100~350 mg/L和34 mg/L,碳氮比在3~10之间的条件下,碳氮比的增加不影响AMBR对COD和NH4+-N的去除,在150 d的运行时间内,出水COD和NH4+-N质量浓度始终分别保持在20 mg/L和2 mg/L左右;但碳氮比的增加有利于AMBR去除TN,当碳氮比大于5时,TN去除率超过66%,出水TN质量浓度低于15 mg/L,满足国家GB 18918—2002中一级A的要求. In order to investigate the optimal C/N ratio for simultaneous nitrogen and carbon removal by a gas-water alternate membrane bioreactor(AMBR)treating wastewater,an AMBR in which two hydrophilic polypropylene hollow-fiber membrane modules was used for aeration and filtration alternately was constructed,and the effect of C/N ratio on simultaneous removal of nitrogen and carbon by AMBR treating synthetic wastewater was studied during the 150 days' continuous operation.The results showed that under the condition that DO in the mixed liquor was 0.5 mg/L around,the influent COD and NH4+-N was(100-350)mg/L and 34 mg/L,and C/N ratio was in the range of 3-10,increase of C/N ratio had no influence on COD and NH4+-N removal.During the 150 days' operation,COD and NH4+-N in effluent maintained 20 mg/L and 2 mg/L around,respectively.However,increase of C/N ratio was beneficial to TN removal by AMBR.When C/N ratio was more than 5,TN removal efficiency was more than 66%,and the effluent TN was lower than 15 mg/L,which met the First A-level requirement of national GB 18918—2002.
出处 《哈尔滨工业大学学报》 EI CAS CSCD 北大核心 2011年第2期45-49,共5页 Journal of Harbin Institute of Technology
基金 "十一五"国家科技支撑计划项目(2006BAB17B06) 建设部研究开发项目(2008-k7-8) 深圳市科技计划项目(深科信2008-343号) 深圳市南山区科技计划项目(南科院2007009)
关键词 碳氮比 气水交替式膜生物反应器 同步脱氮除碳 C/N ratio gas-water alternate membrane bioreactor simultaneous nitrogen and carbon removal
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参考文献15

  • 1付婉霞,李海俊,张璐璐.膜生物反应器中膜污染控制方法的研究[J].环境工程,2004,22(6):15-16. 被引量:11
  • 2PANKHANIA M, STEPHENSON T. Hollow fibre bio reactor for wastewater treatment using bubbleless mem- brane aeration [J]. Water Research, 1994, 28(10): 2233 - 2236.
  • 3BRINDLE K, STEPHENSON T, SEMMENS M J. Pi lot plant treatment of a high strength brewery wastewater using a membrane aeration bioreactor [ J ]. Water Environment Research, 1999, 71(6) : 1197 - 1204.
  • 4BRINDLE K, STEPHENSON T, SEMMENSM J. Ni- trification and oxygen utilization in a membrane aera tion bioreactor [ J ]. Journal of Membrane Science, 1998, 144:197-209.
  • 5SEMMENSM J, DAHM K, SHANAHAN J, et al. COD and nitrogen removal by biofilms growing on gas permeable membranes [ J ]. Water Research, 2003, 37(18) : 4343 -4350.
  • 6HIBIYA K, TERADA A, TSUNEDA S, et al. Simul taneous nitrification and denitrification by controlling vertical and horizontal microenvironment in a mem brane aerated biofilm reactor [ J ]. Journal of Biotech- nology, 2003, 100( 1 ): 23-32.
  • 7HISASHI S, HIDEKI O, BIAN R, et al. Macroscale and microscale analyses of nitrification and denitrifica tion in biofilms attached on membrane aerated biofilm reactors [J]. Water Research, 2004, 38(6): 1633 1641.
  • 8HISASHI S, HIDEKI O, BIAN R, et al. Macroscal and microscale analyses of nitrification and denitrifica tion in biofilms attached on membrane aerated biofilr reactors [J]. Water Research, 2004, 38(6): 1633 - 1641.
  • 9汪舒怡,汪诚文,梁鹏,黄霞.膜曝气生物反应器的除碳脱氮特性研究[J].中国给水排水,2007,23(9):40-43. 被引量:8
  • 10MATSUMOTO S, TERADA A, TSUNEDA S. Modeling of membrane-aerated biofilm: effects of C/N ratio, bio film thickness and surface loading of oxygen on feasibili ty of simultaneous nitrification and denitrification [ J ]. Biochemical Engineering Journal, 2007, 37 ( 1 ) : 98 - 107.

二级参考文献29

  • 1国家环保局.水和废水监测分析方法(第3版)[M].北京:中国环境科学出版社,1989.246-251.
  • 2美国公共卫生协会AHPA 自来水厂协会AWWA 水污染控制联合会WPCF 宋仁元译.水和废水标准检验法(第15版)[M].北京:中国建筑工业出版社,1982..
  • 3付婉霞 李蕾.活性炭投加浓度对膜通量影响的试验研究[J].环境工程,2003,:51-53.
  • 4Gorgun E,Artan E,Orhon D,et al.Evaluation of nitrogen removal by step feeding in large treatment plants[J].Wat.Sci.Tech,1996,34(1-2):253-260.
  • 5Fillos John,Vasil Diyamandoglu,Luis A,et al.Full-scale evaluation of biological nitrogen removal in the step-feed activated sludge process[J].Water Environ.Res,1996,68(2):132-142.
  • 6Larrea L,Larrea A,Ayesa E,et al.Development and verification of design and operation criteria for the step feed process with nitrogen removal[J].Wat.Sci.Tech,2001,43(1):261-268.
  • 7Lesouef A,Payraudeau F,Rogalla M,et al.Optimizing nitrogen removal reactor configurations by on-site calibration of the IWAPRC activated sludge model[J].Wat.Sci.Tech,1992,25(1):115-123.
  • 8Kayser R,Stobbe G,Werner M.Operational results of the Wolfsburg wastewater treatment plant[J].Wat.Sci.Tech,1992,25(4-5):203-209.
  • 9Shigeo F.Theoretical analysis on nitrogen removal of the step-feed anoxic-oxic activated sludge process and its application for the optimal operation[J].Wat.Sci.Tech,1996,34(1-2):459-466.
  • 10Dold P L,Ekama G A,Marais Gv R.Evaluation of the general activated sludge model[J].Wat.Sci.Tech,1986,18(6):63-69.

共引文献44

同被引文献22

  • 1李发站,吕锡武,窦月芹.生物法脱氮新技术及研究进展[J].安全与环境工程,2005,12(2):53-56. 被引量:3
  • 2汪舒怡,汪诚文,梁鹏,黄霞.膜曝气生物反应器的除碳脱氮特性研究[J].中国给水排水,2007,23(9):40-43. 被引量:8
  • 3国家环境保护总局.GBl8918-2002城镇污水处理厂污染物排放标准[S].北京:中国标准出版社,2002.
  • 4PANKHANIA M, STEPHENSON T. Hollow fibre bio- reactor for wastewater treatment using bubbleless mem- brane aeration [ J]. Water Research, 1994, 28 (10) : 2233 - 2236.
  • 5COTE P L, BERSILLON J L, HUYARD A. Bubble - free aeration using membranes: process analysis [ J ]. Journal Water PoUution Control Federation, 1988, 60 (11) : 1986 -1992.
  • 6BRINDLE K, STEPHENSON T, SEMMENS M J. Pi- lot plant treatment of a high strength brewery wastewater using a membrane aeration bioreactor [ J ]. Water Environment Research, 1999, 71 (6) : 1197 - 1204.
  • 7BRINDLE K, STEPHENSON T, SEMMENSM J. Ni- trification and oxygen utilization in a membrane aera- tion bioreactor [ J ]. Journal of Membrane Science, 1998, 144:197-209.
  • 8SEMMENSM J, DAHM K, SHANAHAN J, et al. COD and nitrogen removal by biofilms growing on gas permeable membranes [ J ]. Water Research, 2003, 37(18): 4343 -4350.
  • 9HIBIYA K, TERADA A, TSUNEDA S, et al. Simul- taneous nitrification and denitrification by controlling vertical and horizontal microenvironment in a mem- brane aerated biofilm reactor [ J ]. Journal of Biotech- nology, 2003, 100(1): 23-32.
  • 10HISASHI S, I-IIDEKI O, BIAN R, et al. Macroscale and microscale analyses of nitrification and denitrifica-tion in biofilms attached on membrane aerated biofilm reactors [J]. Water Research, 2004, 38(6): 1633 - 1641.

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