期刊文献+

芬顿-臭氧组合处理柠檬酸镍废水的实验研究 被引量:2

Combined Fenton-Ozone Treatment Technology for Ni(Ⅱ)-citrate Wastewater
下载PDF
导出
摘要 以初始镍质量浓度为50 mg/L的柠檬酸镍废水为研究对象,第一段采用芬顿法进行破络,第二段采用“O_(3)/Fe^(2+)”臭氧组合工艺进一步处理。探讨了芬顿段H_(2)O_(2)投加量和臭氧组合工艺中pH、臭氧投加量、Fe^(2+)投加量、干扰离子对于镍离子去除效果的影响。实验结果表明,芬顿段最佳条件:H_(2)O_(2)投加量为0.15 mL/L,初始pH为5.0,Fe^(2+)投加量为111.11 mg/L,反应时间为12 min;臭氧组合工艺段最佳条件:维持O_(3)质量浓度为30 mg/L,反应时间为18 min,在两段工艺的最佳条件下,柠檬酸镍废水中约99.8%的柠檬酸镍得以去除,出水镍浓度达到国家排放标准。 Ni(Ⅱ)-citrate wastewater with an initial nickel concentration of 50 mg/L was studied,and the first stage was treated with Fenton method for complex breaking,and the second stage was further treated with“O_(3)/Fe^(2+)”ozone combination process.The effects of H_(2)O_(2)dosage in Fenton section and pH,ozone dosage,Fe^(2+)dosage and interfering ions on the removal of nickel ions in the combined ozone process were investigated.The experimental results showed that the optimum conditions in the Fenton section were 0.15 mL/L H_(2)O_(2)dosage,5.0 initial pH,111.11 mg/L Fe^(2+)dosage and 12 min reaction time;the optimum conditions in the ozone combination process section were 30 mg/L O_(3)concentration and 18 min reaction time,and under the optimum conditions of the two processes,about 99.8%of nickel citrate in the nickel citrate wastewater was removed.Under the optimal conditions of the two processes,99.8%of nickel citrate was removed and the effluent nickel concentration reached the national emission standard.
作者 刘静静 徐小凤 卓琼芳 孟翠琳 谢水波 LIU Jingjing;XU Xiaofeng;ZHUO Qiongfang;MENG Cuilin;XIE Shuibo(School of Civil Engineering,University of South China,Hengyang,Hunan 421001,China;School of Environment and Civil Engineering,Dongguan University of Technology,Dongguan,Guangdong 523808,China)
出处 《南华大学学报(自然科学版)》 2022年第4期35-40,56,共7页 Journal of University of South China:Science and Technology
基金 东莞理工学院博士启动项目(2062016141)
关键词 芬顿-臭氧组合工艺 柠檬酸镍 破络 Fenton-ozone combined process Ni(Ⅱ)-citrate decomplexation
  • 相关文献

参考文献9

二级参考文献40

  • 1王树涛,张立珠,马军,刘惠玲.臭氧预氧化对城市污水二级出水可生化性的影响[J].环境科学与技术,2010,33(6):181-184. 被引量:25
  • 2国家环保局编.水与废水监测分析方法(第三版)[M].北京:中国环境科学出版社,1989..
  • 3Enric Brillas,Juan Casado.Aniline degradation by electro-Fenton andperoxi-coagulation process using a flow reactor for wastewater treatment[ J ].Chemosphere,2002,47:241-248.
  • 4Gallard H,De Laat J.Kinetic modelling of Fe (Ⅲ)/H2O2 oxidation reaction in dilute aqueous solution using atrazine as a modle organic compound[ J ].Wat Res,2000,34(12):3107-3116.
  • 5De Laat J,Gallard H.Catalytic decomposition of hydrogen peroxide by Fe (Ⅲ) in homogeneous aqueous solution:mechanism and kinetic modeling[ J].Environ Sci Technol,1999,33:2726-2732.
  • 6Neyens E, Baeyens J. A review of classic Fenton' s peroxidation as an advanced oxidationtechnique [ J 7. Journal of Hazardous ma- terials, 2003, 98 ( 1 ) : 33-50.
  • 7Barbusi6skiK, Filipek K. Use of Fenton' s reagent for removal of pesticides from industrial wastewater[ J]. Polish Journal of Envi- ronmental Studies, 2001, 10(4) : 207-212.
  • 8汪林,杜茂安,李欣.芬顿氧化法深度处理亚麻生产废水[J].工业用水与废水,2008,39(1):52-54. 被引量:26
  • 9任学昌,史载锋,孔令仁,展宗城.TiO2薄膜光催化体系中羟基自由基的水杨酸分子探针法测定[J].环境科学学报,2008,28(4):705-709. 被引量:18
  • 10陈卫国,朱锡海.电催化产生H_2O_2和·OH机理及在有机物降解中的应用[J].水处理技术,1997,23(6):354-357. 被引量:54

共引文献130

同被引文献23

引证文献2

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