期刊文献+

长江下游某工业园区含低浓度有机氮综合工业废水处理实践

Practice of Low Concentration Organic Nitrogen Industrial Wastewater Treatment of an Industrial Park in Lower Reaches of the Yangtze River
下载PDF
导出
摘要 对进水含有低浓度有机氮的工业园区综合废水进行处理,在充分调查企业出水水质及现状污水处理厂运行情况的基础上,采用改良型AO+芬顿氧化+加载澄清+活性炭吸附主体工艺,并对AO工艺进行了针对性的优化,出水满足“准Ⅳ类”水标准要求(TN质量浓度≤12 mg/L)。项目设计规模为2.0×104 m^(3)/d,工程总投资为15819.18万元,直接运行成本为3.863元/m^(3)。在江苏省《城镇污水处理厂污染物排放限值》(DB 32/4440—2022)颁布实施后,出水也满足新标准的要求,主体工艺具有较强的适应性、稳定性及前瞻性。 On the basis of full investigation of wastewater treatment plant(WWTP)operation and water quality of effluent from enterprises,the combined process of modified AO-Fenton oxidation-high efficient clarifier-activated carbon adsorption is used for treatment of industrial park wastewater which contained low concentration of organic nitrogen and refractory organic pollutants.The AO process is optimized,and the effluent meets the requirements of Quasi-Ⅳclass of surface water standards(TN≤12 mg/L).The capacity of this plant is 2×104 m^(3)/d.The total investment of the project is 158.19 million yuan and direct operation cost is 3.863 yuan/m^(3).The effluent also meets the requirements of the Discharge Standard of Pollutants for Municipal Wastewater Treatment Plant(DB 32/4440—2022)of Jiangsu Province.It shows that the main process not only has strong adaptability and stability,but also has certain prospective.
作者 陈秋萍 张万里 程明涛 CHEN Qiuping;ZHANG Wanli;CHENG Mingtao(Huaxin Design Group Co.,Ltd.,Wuxi 214072,China)
出处 《净水技术》 CAS 2024年第3期134-142,共9页 Water Purification Technology
关键词 有机氮 改良 AO 芬顿氧化 活性炭吸附 工业园区污水处理厂 organic nitrogen modified AO Fenton oxidation activated carbon adsorption WWTP in industrial park
  • 相关文献

参考文献6

二级参考文献63

  • 1胡湖生,杨明德,叶血清,党杰,杨立春.萃取-吸附法处理二甲基甲酰胺(DMF)废水的实验研究[J].环境科学研究,2004,17(4):40-43. 被引量:46
  • 2张亚利.二甲基乙酰胺的合成进展及应用[J].河北化工,2006,29(1):41-42. 被引量:18
  • 3杨明德,吴玉龙,党杰,等.一种废水中二甲基甲酰胺的回收方法.中国:200510086784.5,2006.
  • 4李益雄.DMF废水的液液相平衡研究及回收工艺模拟.福州:福州大学,2009.
  • 5Heertjes P. M. , Holve W. A. , Talsma H. Mass transfer between isobutanol and water in a spray column. Chemical Engineering Science, 1954,3 ( 3 ) : 122-142.
  • 6Handlos A. E. , Baron T. Mass and heat transfer from drops in liquid-liquid extraction. American Institute of Chemical Engineers, 1957, 3( 1 ) : 127-136.
  • 7Mohanty S. Modeling of liquid-liquid extraction column: a review. Reviews in Chemical Engineering, 2000, 16(3) : 199-248.
  • 8Hufnagl H. , Mclntyre M. , Blass E. Dynamic behaviour and simulation of a liquid-liquid extraction column. Chemical Engineering & Technology, 1991, 14( 5 ) : 301- 306.
  • 9Steiner L. Drop population balance tool or flop. Chemie Ingenieur Technik, 1996, 68 ( 1 ) : 141-146.
  • 10Goodson M., Kraft M. Simulation of coalescence and breakage:An assessment of two stochastic methods suit- able for simulating liquid-liquid extraction. Chemical Engineering Science, 2004, 59(18) : 3865-3881.

共引文献97

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