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曝气生物流化床处理高浓度含酚废水

宋玉栋 杨 健 杨婧晖 董 婧 周岳溪

宋玉栋, 杨 健, 杨婧晖, 董 婧, 周岳溪. 曝气生物流化床处理高浓度含酚废水[J]. 环境科学研究, 2010, 23(7): 930-935.
引用本文: 宋玉栋, 杨 健, 杨婧晖, 董 婧, 周岳溪. 曝气生物流化床处理高浓度含酚废水[J]. 环境科学研究, 2010, 23(7): 930-935.
SONG Yu-dong, YANG Jian, YANG Jing-hui, DONG Jing, ZHOU Yue-xi. Treatment of High-Concentration Phenolic Wastewater by Aerated Biological Fluidized Tank[J]. Research of Environmental Sciences, 2010, 23(7): 930-935.
Citation: SONG Yu-dong, YANG Jian, YANG Jing-hui, DONG Jing, ZHOU Yue-xi. Treatment of High-Concentration Phenolic Wastewater by Aerated Biological Fluidized Tank[J]. Research of Environmental Sciences, 2010, 23(7): 930-935.

曝气生物流化床处理高浓度含酚废水

基金项目: 国家水体污染控制与治理科技重大专项(2008ZX07207-004)

Treatment of High-Concentration Phenolic Wastewater by Aerated Biological Fluidized Tank

  • 摘要: 采用曝气生物流化床(ABFT)工艺处理自配及实际高浓度炼油含酚废水,在进水ρ(总酚)为200~4 900 mg/L时,总酚去除率可达99%以上;苯酚的去除主要发生在曝气生物流化床的第1池,其他反应池可进一步保证出水水质的稳定性,从而使该工艺具有很强的耐冲击负荷能力;曝气生物流化床第1池在苯酚负荷为4.80~7.84 kg/(m3·d)的条件下,苯酚去除率可达70%以上;曝气生物流化床内生物量以附着生长生物膜为主,丝状菌在生物膜中占有重要地位.对自配和实际废水,ABFT均在高苯酚负荷下实现了污染物的稳定去除.

     

  • [1] 周文敏,傅德黔,孙宗光.水中优先控制污染物黑名单[J].中国环境监测,1990,6(4):1-3.
    [2] BUSCA G,BERARDI NELLI S,RESINI C,et al.Technologies for the removal of phenol from fluid streams: a short review of recent developments[J].J Hazard Materi,2008,160:265-288.
    [3] SHETTY K V,RAMANJANEYULU R,SRINIKETHAN G.Biological phenol removal using immobilized cells in a pulsed plate bioreactor: effect of dilution rate and influent phenol concentration[J].J Hazard Materi,2007,149:452-459.
    [4] PEYTON B M,WILSONA T,YONGE D R.Kinetics of phenol biodegradation in high salt solutions[J].Water Res,2002,36: 4811-4820.
    [5] YU H Q,GU G W.Treatment of phenolic wastewater by sequencing batch reactors with aerated and unaerated fills[J].Waste Manage,1996,16(7):561-566.
    [6] 叶正芳,李彦锋,李贤真,等.曝气生物流化床(ABFB)处理煤气化废水的研究[J].中国环境科学,2002,22(1):32-35.
    [7] 陈怡.高氨氮污水和高浓度有机废水综合治理技术[J].油气田环境保护,2005,15(2):29-31.
    [8] JOU C G,HUANG G C.A pilot study for oil refinery wastewater treatment using a fixed film bioreactor[J].Advances in Environmental Research,2003,7:463-469.
    [9] 中国工程建设标准化协会.CECS209—2006 曝气生物流化池设计规程[S].北京:中国计划出版社,2006.
    [10] 赵婧,蒋进元,丁林,等.核黄素对偶氮染料生物降解的影响[J].环境科学研究,2009,22(10):1193-1197.
    [11] 国家环境保护总局.水与废水监测分析方法[M].4版.北京:中国环境科学出版社,2002:408-410.
    [12] TROOP W M.Alternative methods of phenol wastewater control[J].J Hazard Materi,1975,77(1):319-329.
    [13] YOONG E T,LANT P A,GREENFIELD P F.In situ respirometry in an SBR treating wastewater with high phenol concentration[J].Water Res,2000,34(1):239-245.
    [14] BANERJEE G.Treatment of phenolic wastewater in RBC reactor[J].Water Res,1997,31(4):705-714.
    [15] 张金利,李韦华,袁兵,等.生物流化床法处理高浓度含酚废水的研究[J].化学反应工程与工艺,2001,17(2):149-153.
    [16] 周如金,程丽华,李德豪,等.HCR工艺处理炼油含酚废水的特性研究[J].石油化工高等学校学报,2008,21(1):8-11.
    [17] 沈齐英,刘录,沈秋英,等.微生物降解炼油厂含酚废水的试验研究[J].四川环境,2003,22(4):23-34.
    [18] GONZALEZ G,HERRERA M G,GARCIA M T,et al.Biodegradation of phenol in a continuous process: comparative study of stirred tank and fluidized-bed bioreactors[J].Bioresource Technology,2001,76:245-251.
    [19] AHN S,CONGEEVARAM S,CHOUNG Y K,et al.Enhanced phenol removal by floating fungal populations in a high concentration phenol-fed membrane bioreactor[J].Desalination,2008,221:494-501.
    [20] PERRON N,WELANDER U.Degradation of phenol and cresols at low temperatures using a suspended-carrier biofilm process[J].Chemosphere,2004,55:45-50.
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出版历程
  • 收稿日期:  2010-01-25
  • 修回日期:  2010-04-10
  • 刊出日期:  2010-07-25

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