Distribution of Fe(II) Concentration during Degradation of Rhodamine B by Fenton Reagent

Article Preview

Abstract:

The effects of reaction conditions including Fe2+, H2O2, oxalic acid, and humic acid dosages were discussed on the Fenton degradation of rhodamine B (RB). The optimal reaction conditions of Fenton reaction were 0.15 mM Fe2+, 5 mM H2O2, and pH 3.0, and the decolorization rate RB (10 mg/L) reached 97.8% after 30min catalytic degradation. The changes of Fe2+ concentrations in Fenton system has been focused on in this work. A relatively low concentration of Fe2+ was maintained during reaction process when Fe2+ and H2O2 were added with high concentration, and thus RB was degraded quickly. The results implicated that Fe2+ dosage played a very important role in the degradation of RB, and H2O2 dosage didn’t have an apparent influence on the degradation of RB in general. The Fenton degradation of RB could be inhibited in the presence of oxalic acid and humic acid, especially at a high concentration of oxalic acid and humic acid.

You might also be interested in these eBooks

Info:

Periodical:

Advanced Materials Research (Volumes 261-263)

Pages:

744-748

Citation:

Online since:

May 2011

Export:

Price:

Permissions CCC:

Permissions PLS:

Сopyright:

© 2011 Trans Tech Publications Ltd. All Rights Reserved

Share:

Citation:

[1] G.K. Zhang, Y.Y. Gao, Y.Z. Zhang et al.: Environmental Science and Technology Vol.44 (2010), p.6384

Google Scholar

[2] P. Janoš: Environmental Science and Technology Vol.37 (2003), p.5792

Google Scholar

[3] L.J. Kong and A.T. Lemley: Journal of Agricultural and Food Chemistry Vol.54 (2006), p.3941

Google Scholar

[4] S. Chiron, A. Fernandez-Alba, A. Rodriguez et al.: Water Research Vol.34 (2000), p.366

Google Scholar

[5] R.J. Watts, A.L. Teel: Journal of Environmental Engineering-asce. Vol.131 (2005), p.612

Google Scholar

[6] N. Masomboon, C. Ratanatamkkul and M.C. Lu: Environmental Science and Technology Vol.43 (2009), p.8629

Google Scholar

[7] C. Walling: Accounts of Chemical Research Vol.8 (1975), p.125

Google Scholar

[8] J.A. Zazo, J.A. Casas, A.F. Mohedano et al.: Environmental Science and Technology Vol.39 (2005), p.9295

Google Scholar

[9] M.D. Paciolla, G. Davies and S.A. Jansen: Environmental Science and Technology Vol.33 (1999), p.1814

Google Scholar

[10] M. Fukushima, K. Tatsumi and K. Morimoto: Environmental Science and Technology Vol.34 (2000), p.(2006)

Google Scholar

[11] J.H. Ma, W.H. Ma, W.J. Song et al.: Environmental Science and Technology Vol.40 (2006), p.618

Google Scholar

[12] J. Sarma, A. Sarma and K.G. Bhattacharyya: Industrial and Engineering Chemistry Research Vol.47 (2008), p.5433

Google Scholar

[13] T. Zhang, K.B. Li, J.T. Chen et al.: Journal of Northwest A and F University (Nat. Sci. Ed.) Vol.38 (2010), p.197, in Chinese.

Google Scholar

[14] Q. Wang, Y.P. Huang, M. Tang et al.: Acta Energiae Solaris Sinica. Vol.30 (2009), p.36, in Chinese.

Google Scholar

[15] Y.Y. Wu, F.H. Qin, Y.L. Lai, et al.: Research of Environmental Sciences Vol.23 (2010), p.94, in Chinese.

Google Scholar