4.7 Article

Decolorization of CI Reactive Red 2 by catalytic ozonation processes

Journal

JOURNAL OF HAZARDOUS MATERIALS
Volume 153, Issue 3, Pages 1052-1058

Publisher

ELSEVIER
DOI: 10.1016/j.jhazmat.2007.09.058

Keywords

O-3; UV/TiO2; Mn(II); MnO2; CI Reactive Red 2; catalytic ozonation

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Ths study adopted O-3, UV/TiO2/O-3, O-3/Mn(H) and 03/MnO2 systems to assess the decolorization efficiency of C.I. Reactive Red 2 (RR2). The decolorization rate increased with concentrations of Mn(II) and MnO2 in the ranges 0.054.1 and 0.05-0.8 g/l, respectively. However, when 0.5-3 g/l TiO2 was added, the effect of TiO2 dosage for RR2 decolorization was insignificant in the LTV/TiO2/O-3 system. At pH 2, the decolorization rate constants of O-3, O-3/Mn(II) (0.05 g/l), O-3/Mn(II) (0.1 g/l), O-3/Mn(II) (0.15 g/l), O-3/MnO2 (0.05 g/l) and O-3/MnO2 (0.8 g/l) were 0.816, 2.001, 3.173, 3.087, 1.040 and 1.648 min(-1), respectively. After 5 min of reaction, the decolorization rates followed the order O-3/Mn(II) > O-3/MnO2 > O-3 > UV/TiO2/O-3; however, the TOC removal did not vary among these systems. Adding ethanol reduced the decolorization rate of the UV/TiO2/O-3 and O-3/MnO2 Systems and did not affect the decolorization rate of O-3/Mn(II). Decolorization in UV/TiO2/O-3, O-3/Mn(III) and O-3/MnO2 systems is suggested to proceed by mainly radical-, surface- and radical-type mechanisms, respectively. Additionally, direct ozonation cannot be ignored in O-3/Mn(II) and O-3/MnO2 Systems. (C) 2007 Elsevier B.V. All rights reserved.

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