期刊文献+

利用水厂生产废水促进UASB工艺处理低温城市污水启动

Reuse of Waterworks Wastewater to Enhance the Start-up of UASB Process for Low Temperature Municipal Wastewater Treatment
在线阅读 下载PDF
导出
摘要 为缩短UASB工艺处理低温城市污水的启动周期,开展在原水中添加水厂生产废水强化UASB系统污泥颗粒化可行性研究,并以常规启动方式做为比较,对启动过程中系统运行特性和形成的颗粒污泥特性进行探讨。试验结果表明,在水温为15℃,初始有机负荷为0.25kgCOD/(m3.d)的条件下,采用逐步提高负荷的传统启动方式和添加生产废水的强化启动方式都能实现UASB工艺的低温启动,相应的启动周期分别为120d和95d左右。在整个启动过程中,添加生产废水启动方式对有机负荷提高适应性较强,达到4kgCOD/(m3.d)时较常规方式缩短30d,而且具有较高的COD去除效率和微生物增长速率(分别为0.029g VSS/d和0.043g VSS/d)。与常规启动方式相比,强化启动方式颗粒粒径较大,在第95d内可形成2mm粒径颗粒污泥。采用添加生产废水的启动方式能够缩短UASB工艺的启动周期并强化污泥颗粒化,提高低温城市污水的处理效率和运行稳定性。 To shorten the start-up period of UASB process for the low temperature municipal wastewater treatment,two lab-scale UASB reactors were employed to study the feasibility of enhanced start-up with addition of waterworks wastewater to raw water.Also the operation and biomass characteristics were investigated with comparison of conventional start-up mode.The results show that,under the water temperature of 15℃ and the initial organic loading rate(OLR) of 0.25 kgCOD/(m3·d),the UASB system can get stable condition with both the OLR escalating and enhanced mode,and the start-up period is approximate 120 days and 95 days respectively.Throughout the experiment the enhanced start-up processes preferable adaptability,which shorten 30days to achieve the OLR of 4 kgCOD/(m3·d),and higher COD removal as well as biomass growth rate(0.029 g VSS/d versus 0.043 g VSS/d) correspondingly.Compared to conventional mode,the mean diameter of granular sludge is larger and 2 mm granular sludge can be formed within 95 days by enhanced mode.The experimental results demonstrate that adding waterworks wastewater can shorten the start-up time and enhance granulation,which in turn leads to improvement in organics removal efficiency and stability of the UASB system for low temperature municipal wastewater treatment.
出处 《土木建筑与环境工程》 CSCD 北大核心 2011年第6期135-139,共5页 Journal of Civil,Architectural & Environment Engineering
关键词 UASB 启动 颗粒污泥 低温 生产废水 UASB start-up granulation low temperature waterworks wastewater
  • 相关文献

参考文献11

  • 1ALVAREZ J A, ARMSTRONG E, GOMEZ M. Anaerobic treatment of low-strength municipal wastewater by a two-stage pilot plant under psychrophilic conditions [J]. Bioresouree Technology, 2008, 99(15): 7051-7062.
  • 2NACHEVA P M, CHAVEZ G M, CHACON J M. Treatment of cane sugar mill wastewater in an upflow anaerobic sludge bed reactor[J]. Water Sci Technol, 2009, 60(5): 1347-1352.
  • 3CAO Y S, ANG C M. Coupled UASB-activated sludge process for COD and nitrogen removals in municipal sewage treatment in warm climate [J]. Water Sci Technol, 2009, 60(11): 2829-2839.
  • 4DIAMANTIS V I, VERSTRAETE W, AIVASIDIS A. Upflow anaerobic clarification tank (UACT) to upgrade existing anaerobic effluents[J]. Water Sci Technol, 2009, 59(12) : 2411-2419.
  • 5WEILI ZHOU, TSUYOSHI IMAI, MASAO UKITA, et al. Effect of loading rate on the granulation process and granular activity in a bench scale UASB reactor[J]. Bioresource Technology, 2007, 98(7) : 1386-1392.
  • 6GHANGREKAR M M, ASOLEKAR S R, JOSHI S G. Characteristics of sludge developed under different loading conditions during UASB reactor start-up and granulation[J]. Water Res, 2005, 39(6): 1123-1133.
  • 7WenNi,HongweiDuan,XiaolingAi,JianpingLi.Promoting sludge granulation by putting xonotlite into the UASB reactors during starting-up stage[J].Journal of University of Science and Technology Beijing,2003,10(4):7-11. 被引量:4
  • 8王磊,佘宗莲,郭晶,孙淑慧.常温下向ABR反应器中加入惰性载体促进颗粒污泥形成[J].环境工程学报,2008,2(7):955-958. 被引量:8
  • 9SAITO T, BRDJANOVIC D, VAN LOOSDRECHT M C M. Effect of nitrite on phosphate uptake by phosphate accumulating organisms [ J ]. Water Research, 2004, 38: 3760-3768.
  • 10国家环保局.水和水质监测分析方法[M].4版.北京:中国环境科学出版社,2002.

二级参考文献17

  • 1王林山,吴允,张勇,王升荣.UASB反应器中加入惰性载体促进颗粒污泥生成[J].环境导报,1996(3):12-14. 被引量:18
  • 2[1]Barber W.P.,Stuckey D.C.The use of the anaerobic baffled reactor (ABR) for wastewater treatment:A review.Water Res.,1999,33(7):1559~1578
  • 3[2]Nachaiyasit S.,Stuckey D.C.The effect of shock loads on the performance of an anaerobic baffled reactor (ABR).1.Step changes in feed concentration at constant retention time.Water Research,1997,31(11):2737~2746
  • 4[4]Sallis P.J.,Uyanik S.Granule development in a split-feed anaerobic baffled reactor.Bioresource Technology,2003,89:255~265
  • 5[6]Wirtz R.A.,Dague R.R.Enhancement of granulation and start-up in the anaerobic sequencing batch reactor.Water Environ.Res.,1996,68(5):883~892
  • 6[7]Uyanik S.,Sallis P.J.,Anderson G.K.The effect of polymer addition on granulation in an anaerobic baffled reactor(ABR) Part I:Process performance.War.Res.,2002,36:933~943
  • 7[8]Yu H.Q.,Tay J.H.,Fang H.H.P.Effect of added powdered and granular activated carbons on start-up performance of UASB reactors.Environ.Technol.,1999,20:1095~1101
  • 8[9]国家环保总局.水和废水监测分析方法(第3版).北京:中国环境科学出版社,1998.354~356
  • 9Pereira M A, Roest K, Stams A J M, et al. Molecular monitoring of microbial diver in expanded granular sludge bed (EGSB) reactors treating oleic acid[J]. FEMS Microsity Biology Ecology,2002,41 (10) :95 - 103.
  • 10Rebac S, Gerbens S, Lens P, et al. Kinetics of fatty acid degradation by psychrophilically grown anaerobic granular sludge [J]. Biosour Technol, 1999,69 (6) :241 - 248.

共引文献31

相关作者

内容加载中请稍等...

相关机构

内容加载中请稍等...

相关主题

内容加载中请稍等...

浏览历史

内容加载中请稍等...
;
使用帮助 返回顶部