Modified diatomites for Fenton-like oxidation of phenol

被引:33
|
作者
Inchaurrondo, N. [1 ]
Ramos, C. P. [2 ]
Zerjav, G. [3 ]
Font, J. [4 ]
Pintar, A. [3 ]
Haure, P. [1 ]
机构
[1] Univ Nacl Mar del Plata, INTEMA, CONICET, Dept Ingn Quim,Div Catalizadores & Superficies, RA-7600 Mar Del Plata, Argentina
[2] CNEA, CAC, GiyA, Dept Fis Mat Condensada, Ave Gral Paz 1499 San Martin, Buenos Aires, DF, Argentina
[3] Natl Inst Chem, Dept Environm Sci & Engn, Hajdrihova 19, SI-1001 Ljubljana, Slovenia
[4] Univ Rovira & Virgili, Dept Engn Quim, Escola Tecn Super Engn Quim, E-43007 Tarragona, Catalonia, Spain
关键词
Diatomites; Phenol; Natural catalyst; Fenton-like; HYDROGEN-PEROXIDE OXIDATION; PILLARED CLAYS; CATALYST; IRON; MOSSBAUER; FE; HYDROXYLATION; REMOVAL; ADSORPTION; MINERALS;
D O I
10.1016/j.micromeso.2016.10.026
中图分类号
O69 [应用化学];
学科分类号
081704 ;
摘要
Raw diatomites were modified by acid or base treatments; addition of Fe or Cu species through the incipient wet impregnation method (IWI) and calcination at 700 degrees C. Samples were characterized by X-ray powder diffraction (XRD), scanning electron microscopy (SEM-EDX), Mossbauer spectroscopy, point of zero charge (PZC), pyridine temperature programme desorption (TPD), thermogravimetric analysis (TGA) and BET surface area determination. According to characterization results, four samples were selected: simply calcined Diatom (D), iron added (Fe-D), acid treated Fe reimpregnated (H-Fe-D) and copper added (Cu/Fe-D). Materials were tested as catalysts for the peroxidation of phenol solutions (1000 mg/L) in a batch laboratory reactor, at different operating conditions in 5 h tests. D, Fe-D and H-Fe-D samples allowed complete phenol removal under all the operating range studied. At optimum conditions, TOC conversions of 50-55% were obtained. Metal ions added through the IWI procedure resulted more labile than metal present originally. The acidic treatment favored the initiation of the reaction showing a reduction of the induction period at almost neutral initial pH. The Fe-D catalyst exhibited poor performance, lower reactions rates and higher Fe leaching. Conversely, high TOC conversions (80%) were achieved with Cu/Fe-D, however, Cu leaching was excessive (12.7%). D and H-Fe-D samples were used in consecutive runs (up to 20 h) maintaining phenol conversion and TOC reduction. Overall, a good performance was obtained, even comparable to more sophisticated Fe catalysts. (C) 2016 Elsevier Inc. All rights reserved.
引用
收藏
页码:396 / 408
页数:13
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