试验研究

湿式催化氧化法处理含酚清洗废水的研究

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  • 1. 天津科技大学环境科学与工程学院, 天津市海洋资源与化学重点实验室, 天津 300457;
    2. 天津科技大学机械工程学院, 天津 300457
李桂菊(1969- ),2006 年毕业于天津科技大学,博士,副教授,研究方向:废水治理及固体废物资源化。电话:022-60601461,E-mail:lgj69@163.com。

修回日期: 2009-11-20

  网络出版日期: 2010-10-01

基金资助

天津市塘沽区科技发展资金项目(2008CG10-04)

Study on the application of wet catalytic oxidation process to the treatment of phenol-containing cleaning wastewater

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  • 1. Tianjin Key Laboratory of Marine Resources & Chemistry, College of Environmental Science and Engineering, Tianjin University of Science and Technology, Tianjin 300457, China;
    2. College of Mechanical Engineering, Tianjin University of Science and Technology, Tianjin 300457, China

Revised date: 2009-11-20

  Online published: 2010-10-01

摘要

针对化工集装罐清洗废水中含酚废水浓度大的特点,采用湿式催化氧化法进行了较深入的研究。对硝酸铜-AC制备CuO/AC催化剂过程中的浸渍液浓度、焙烧温度、焙烧时间等影响因素进行探讨;用该催化剂催化氧化降解模拟苯酚废水,对反应温度、氧化剂投加量、催化剂投加量、反应时间等工艺参数进行优化,确定最佳反应条件并进行了应用研究。研究结果表明,硝酸铜-AC制备CuO/AC催化剂的最佳条件为:硝酸铜质量分数为3%,浸渍温度为30℃,浸渍时间为6 h,焙烧温度为300℃,焙烧时间为3 h。湿式催化氧化法处理苯酚废水的最佳工艺条件为:反应温度为170℃,反应时间为1 h,催化剂投加质量浓度为2 g/L,氧化剂H2O2按m(H2O2)∶m(COD)=3投加,含酚清洗废水的COD去除率达到95%以上,处理效果显著。

本文引用格式

李桂菊, 朱丽香, 何迎春 . 湿式催化氧化法处理含酚清洗废水的研究[J]. 工业水处理, 2010 , 30(5) : 38 -41 . DOI: 10.11894/1005-829x.2010.30.(05).38

Abstract

Aiming at the characteristic that the concentration of phenol-containing wastewater in tank containers is rather high,advanced study has conducted by wet catalytic oxidation process. The preparation conditions of catalyst CuO/AC,such as its concentration of the soakage solution calcination temperature,calcination time,etc. are explored. Simulated phenol-containing wastewater is catalyzed,oxidized and degraded with this catalyst. Its technical parameters,including reaction temperature,dosages of oxidant and catalyst,reaction time,etc. are optimized. The best reaction conditions are confirmed and its application research is carried through. The results show that the optimum preparation conditions of CuO/AC catalyst are as follows:the concentration of Cu(NO32 is 3%,soakage temperature 30 ℃,soaking time 6 h,calcinating temperature 300 ℃,and calcinating time 3 h.The optimized reaction conditions of CWO for treating phenol wastewater are as follows: reaction temperature is 170 ℃,reaction time 1 h,dosage of catalyst 2 g/L,and dosage of oxidant m(H2O2)∶m(COD)=3. Thus,the COD removal rate of the phenol-containing cleaning wastewater is above 95%,revealing a significant treatment effect.

参考文献

[1] 杨云龙,白晓平.焦化废水的处理技术与进展[J].工业用水与废水,2001(3):8-10.
[2] 罗平,范益群.非均相湿式催化氧化中H2O2的分解[J].南京工业大学学报,2007,29(4):65-67.
[3] 韩利华,李国江,芮玉兰,等.高浓度焦化废水湿式氧化铜系催化剂的研制[J].环境污染治理技术与设备,2003,4(3):19-22.
[4] 张思华,王亚明,缪应菊,等.非贵金属铜系催化剂上氧化CO 的研究进展[J].工业催化,2008,16:46-50.
[5] 罗平,徐南平.铜系催化剂的研制及其在H2O2催化氧化中的应用研究[J].水处理技术,2006,32(12):44-46.
[6] 潘履让.固体催化剂的设计与制备[M]. 天津:南开大学出版社,1991:24-34.
[7] 左宁.铜锌铈体系催化剂催化氧化CO 的研究[D]. 哈尔滨:哈尔滨工程大学材料科学与化学工程学院,2007.

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