试验研究

TiO2光催化超滤反应器降解酸性胡兰的试验研究

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  • 天津大学环境科学与工程学院, 天津 300072
金洛楠(1981- ),2003 级天津大学在读研究生。电话:022 -27407240,E-mail:xiaonan -002@163.com

收稿日期: 2005-03-25

  网络出版日期: 2010-10-01

Application of TiO2-photocatalys is -ultrafiltration reactor to the degradation of acid blue 7

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  • School of Environmental Science and Engineering, Tianjin University, Tianjin 300072, China

Received date: 2005-03-25

  Online published: 2010-10-01

摘要

设计研制了一种光催化超滤反应器,并选用一种纳米级颗粒状TiO2做光催化剂,对染料酸性胡兰(AcidBlue 7)氧化降解进行了研究。试验结果表明,光催化超滤反应器对染料废水有很好的降解效果,且粉末态催化剂能够实现良好分离。通过对影响反应系统的操作参数研究发现,当错流速度从0.45 m/s增加到1.06 m/s时,降解速率常数也从0.070 8 min-1提高到0.151 5 min-1;反应系统的最佳TiO2投加质量浓度为0.5 g/L;当染料质量浓度从5 mg/L增加到25 mg/L,相应的反应速率常数也从0.162 5 min-1降为0.053 0 min-1;反应系统中用纯氧曝气可以得到最佳的染料去除效果;当染料废水在pH为2时,其去除效果非常明显。

本文引用格式

金洛楠, 季民, 傅剑锋 . TiO2光催化超滤反应器降解酸性胡兰的试验研究[J]. 工业水处理, 2005 , 25(10) : 32 -35 . DOI: 10.11894/1005-829x.2005.25(10).32

Abstract

A set of photocatalytic-ultrafiltration separation reactor for the degradation of acid blue 7 by using nanoparticle TiO2 as photocatalyst has been designed. The experimental results showthat the well degradation effects of dye wastewaters are achieved by this reactor and TiO2 particle can be separated from water successfully. The results obtained from influencing parameters of photocatalytic membrane reactor′s kinetic studies indicates that the rate increases from 0.0708min-1 to 0.151 5 min-1 with increasing cross-flow velocity ranging from 0.45 m/s to 1.06 m/s. The optimum TiO2 dosage is 0.5 g/L. The increase in the initial dye concentration from 5 mg/L to 25 mg/L can decrease the degradation rate constant from 0.162 5 min-1 to 0.053 0 min-1. Being aerated with industrial grade oxygen in the experiment can get the best removal results. The pH values have substantial effect on the degradation of acid blue 7,particularly at pH 2.

参考文献

[1]Butler E C,Davis A P. Photocatalytic oxidation in aqueous titanium dioxide suspensions:the influence of dissolved transition metals[J].J. Photochem. Photobiol. A:Chem.,1993,70(3):273 - 283
[2]Goswami D Y. A Review of Engineering Developments of Aqueous Phase Solar Photocatalytic Detoxification and Disinfection Processes[J]. Journal of Solar EnergyEngineering,1997,119(3):101- 107
[3]Lepore G P,Persaud L,Langford C H. Supporting titanium dioxide photocatalysts on silica gel and hydrophobically modified silica gel[J]. J. Photochem. A:Chem.,1996,98(1 - 2):103 - 111
[4]loddo V,Marci G,Palmisano L,et al. Preparation and characterization of Al2O3 supported TiO2 catalysts employed for 4 - nitrophenol photodegradation in aqueous medium[J]. Mat. Chem. Phys., 1998,53(3):217 - 224
[5]Robert D,Gauthier A. Prospects for a Supported Photocatalyst in the Detoxification of Drinking Water[J]. Water Qual. Int.,1998,(11 -12):27 - 28 [6]Raffaele Molinari,et al. Studies on various reactor configurations for coupling photocatalysis and membrane processes in water purification[J]. Journal ofMembrane Science,2002,206(1 - 2):399 - 415
[7]Lee Soo-Ah,et al. Use of Ultrafiltration Membrane for the Separation of TiO2 Photocatalysts in Drinking Water Treatment[J]. Ind. Eng.Chem. Res.,2001,40(7):1 712 - 1 719
[8]Lee J C,KimMS,Kim C K,et al. Removal of paraquat in aqueous suspension of TiO2 in an immersed UV photoreactor [J]. Korean J.Chem. Eng.,2003,20(5):862 - 868
[9]San N,Hatipoglu A,Kocturk G,et al. Prediction of primary intermediates and the photodegradation kinetics of 3 - aminophenol in aqueous TiO2 suspensions[J]. J. Photochem. Photobiol. A:Chem.,2001,139(2 - 3):225 - 232
[10]Turchi C S, Ollis D F. Photocatalytic degradation of organic water contaminants:mechanisms involving hydroxyl radical attack [J]. J.Catal.,1990,122(1):178 - 192
[11]FoxMA,DulayMT. Heterogeneous photocatalysis[J]. Chem. Res.,1993,93(1):341 - 357
[12]Legrini O,Oliveros E,Braun AM. Photochemical process for water treatment [J]. Chem. Rev.,1993,93(2):671 - 698
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