Removal of Reactive Black 5 azo dye from aqueous solutions by catalytic oxidation using CuO/Al2O3 and NiO/Al2O3

被引:100
作者
Bradu, Corina [1 ]
Frunza, Ligia [2 ]
Mihalche, Nicoleta [1 ]
Avramescu, Sorin-Marius [1 ]
Neata, Marian [1 ]
Udrea, Ion [1 ]
机构
[1] Univ Bucharest, Dept Organ Chem, Bucharest 030018, Romania
[2] Natl Inst Mat Phys, Magurele 077125, Romania
关键词
Azo dye removal; Catalytic oxidation; Advanced oxidation processes; Reactive Black 5; WET PEROXIDE OXIDATION; HYDROGEN-PEROXIDE; WASTE-WATER; COLOR REMOVAL; OXALIC-ACID; DEGRADATION; OZONATION; KINETICS; DECOLORIZATION; DECOMPOSITION;
D O I
10.1016/j.apcatb.2010.03.019
中图分类号
O64 [物理化学(理论化学)、化学物理学];
学科分类号
070304 ; 081704 ;
摘要
CuO/Al2O3 and NiO/Al2O3 catalysts prepared by incipient wetness impregnation were used for the oxidation of Reactive Black 5 (RB5) in aqueous solution. Removal of the dye was assessed by High Performance Liquid Chromatography (HPLC) and Total Organic Carbon (TOC) measurements and the generation of the hydroxyl radicals in the process was evaluated by chemiluminescence measurements. To put in evidence the interaction RB5 - catalyst and the surface species formed onto catalysts during the oxidation, Diffuse Reflectance Infrared Fourier Transform (DRIFT) analysis was performed. A different behavior of the two catalytic systems was revealed by the comparative analysis of the data obtained from the adsorption and oxidation tests. Only CuO/Al2O3 was effective in the RB5 degradation, NiO/Al2O3 acted as a simple adsorbent. In the presence of CuO/Al2O3, at H2O2 concentration of 40 mM the azo dye was totally eliminated from both solution and catalyst surface after 4 h, with a mineralization degree higher than 90%. However, a strong inhibition of the catalytic oxidation of RB5 was observed in the presence of phosphate ions. In the conditions of hydrogen peroxide excess, the rate equation in the case of copper catalyst was simply expressed by a pseudo-first order equation and the model was found to fit well the data. The amount of copper leached from catalyst during the oxidation process was only 1.0-1.6% per cycle leading to the conclusion that the decrease of the dye mineralization with the number of cycles has to be explained mostly by the surface covering with the reaction products, at least to a certain extent. (C) 2010 Elsevier B.V. All rights reserved.
引用
收藏
页码:548 / 556
页数:9
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