期刊文献+

某污水处理厂低负荷运行问题的分析与调控措施 被引量:8

Analysis and Controlling Measures of Low-Load Operation Problem for a Wastewater Treatment Plant
下载PDF
导出
摘要 浙江省湖州市某污水处理厂采用传统AAO工艺,建设规模为0.5×10~4 m^3/d,实际处理水量为0.33×10~4 m^3/d。实际运行过程中,进水COD_(Cr)浓度为设计值的19.3%,TN为设计值的48.22%,污水厂长期处于低负荷运行状态,给污水厂稳定达标运行造成较大困扰。通过采用间歇曝气的方式运行,同时将污泥浓度由原设计值3 g/L降低至1.5 g/L;关闭内回流,增加200%外回流;精确投加碳源等工艺参数进行了相应的优化,调整后出水水质稳定达到一级A排放标准。调整后吨水电耗节约0.096元/m^3,直接运行成本预计节约17.5万元/年。 AAO process is adopted in a wastewater treatment plant(WWTP)in Huzhou City of Zhejiang Province. The design scale is0. 5×10~4 m^3/d, and the actual handing capacity is 0. 33×10~4 m^3/d. In actual operation, the influent COD_(Cr)concentration is 19. 3% of the design value, and TN is 48. 22% of the design value. The wastewater treatment plant is in a low loading operation for a long time.The sludge concentration is reduced from the original design value 3 g/L to 1. 5 g/L by means of intermittent aeration. Then sludge inward reflux is stoped and external reflux concentration is increased by 200%. Then BOD concentration is added precisely. By optimizing these process parameters, effluent water quality reaches to level A emission standard. The water cost of per ton is saved0. 096 yuan, and the direct operation cost would be saved 175 000 yuan per year.
出处 《净水技术》 CAS 2018年第1期77-81,共5页 Water Purification Technology
关键词 污水厂 低负荷运行 AAO工艺 间歇曝气 分析与调控 wastewater treatment plant(WWTP) low-loading operation AAO process intermittent aeration analysis and controlling
  • 相关文献

参考文献4

二级参考文献49

  • 1宋文清,杨海真.活性污泥数学模型中异养菌产率系数的测定[J].环境污染与防治,2004,26(4):253-255. 被引量:12
  • 2王少坡,彭永臻,王淑莹,张艳萍.温度和污泥浓度对短程内源反硝化脱氮的影响[J].环境科学与技术,2005,28(4):85-86. 被引量:19
  • 3黄勇,杨铨大,王宝贞,聂梅生.生物处理动力学参数测定研究[J].中国环境科学,1996,16(2):123-127. 被引量:20
  • 4[1]Arun V, Minp T and Matsuo T. Biological mechanisms of acetate uptake mediated by carbohydrate consumption in excess phosphorus removal systems.Wat Res, 1988, 22:565~570.
  • 5[2]Smolders GJF, van Loosdrecht MCM and Heijnen JJ. Stoichiometric model of the aerobic metabolism of the biological phosphorus removal process.Biotechnol Bioengng, 1994, 44:837~848.
  • 6[3]Smolders GJF, van der Meij J, van Loosdrecht MCM, et al. Model of the aerobic metabolism of the biological phosphorus removal process, stoichiometric and pH influence. Biotechnol Bioengng,1994, 43:461~470.
  • 7[4]Henze M, Gujer W, Mino T, et al. IAWQ task group on mathematical modeling for design and operation of biological wastewater treatment processes, Activated sludge model No 2, Scientific and Technical Reports No 3 IAWQ, 1995, London.
  • 8[5]Murnleitner E, Kuba T, van Loosdrecht MCM, et al. An integrated metabolic model for the aerobic and denitrifying biological phosphorus removal. J Environ Engng (ASCE), 1997, 56: 876~883.
  • 9[6]Ternmink H, Petersen B, Isaacs S, et al. Recovery of biological phosphorus removal after periods of low organic loading. Wat Sci Technol, 1996, 34(1/2): 1 ~ 8.
  • 10[7]Brdjanovic D, Slamet A, van Loosdrecht MCM, et al. Impact of excessive aeration on biological phosphorus removal from wastewater. Wat Res, 1998,32: 200~ 208.

共引文献68

同被引文献32

引证文献8

二级引证文献3

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