试验研究

Fenton氧化法处理含乌洛托品废水

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  • 1. 上海市建设工程管理有限公司, 上海 200031;
    2. 同济大学环境科学与工程学院, 上海 200092
李菊(1966-),1988年毕业于上海城市建设学院,高级工程师.电话:021-65980400,E-mail:chq496@163.com.

网络出版日期: 2010-10-01

Research of the application of Fenton oxidation to the treatment of wastewater containing urotropine

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  • 1. Shanghai Construction Engineering Administration Co., Ltd., Shanghai 200031, China;
    2. School of Environment Science and Engineering, Tongji University, Shanghai 200092, China

Online published: 2010-10-01

摘要

通过实验优化了Fenton试剂法氧化处理含乌洛托品废水的反应条件。实验表明,当ρ(H2O2)=8.25g/L,n(H2O2)∶n(Fe)=20∶1,pH=3.0,在35℃下反应5h以后,CODCr可从1250mg/L降到>100mg/L。但当温度降低到15℃时,出水CODCr则很难降到>100mg/L。在同样的反应条件下,连续流完全混合反应器的出水CODCr明显高于间歇反应的出水。

本文引用格式

李菊, 陈和谦, 黄友谊, 吴志超 . Fenton氧化法处理含乌洛托品废水[J]. 工业水处理, 2004 , 24(6) : 39 -41 . DOI: 10.11894/1005-829x.2004.24(6).39

Abstract

The reaction condition has been optimized through experiments for the oxidation of wastewater containing urotropine by Fenton reagent. It is indicated that when ρ(H2O2) = 8.25 g/L, n(H2O2) ∶ n(Fe) = 20 ∶ 1, pH = 3.0, CODCr may be decreased from 1 250 mg/L to lower than 100 mg /L after 5 h reaction under 35 ℃. But it is difficult for CODCr to reach 100 mg /L when the temperature dropped to 15 ℃. It is also suggested that CODCr of the effluent from CSTR(continuous-flow stirred tank reactor) is significantly higher than that from SBR(sequnencing batch reactor) under the same condition.

参考文献

[l] 李广林. 乌洛托品及其生产方法[J]. 化肥工业, 1997, 24(4):51-53
[2] Neyens E, Bacyens J. A review of classic Fenton's peroxidation as an advanced oxidation technique[J]. Journal of Hazardous Materials, 2003, 98(2):33-50
[3] 韦朝海, 等. Fenton试剂催化氧化降解含硝基苯废水的特性[J]. 环境科学, 2001, 22(5): 60-64
[4] Sheng H Lin, Chi M Lin, Horng G Leu. Operation characteristics and kinetic studies of surfactant wastewater treatment by Fenton oxidation[J]. Water Research, 1999, 33(7):1735-1741
[5] Malik P K, SaHa S K. Oxidation of direct dyes with hydrogen peroxide using ferrous ion as catalyst[J]. Separation and Purification Technology, 2003, 31(3):241-250

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