Premium
Improved Fe 2 O 3 /Al 2 O 3 as heterogeneous Fenton catalysts for the oxidation of phenol solutions in a continuous reactor
Author(s) -
di Luca Carla,
Massa Paola,
Fenoglio Rosa,
Cabello Francisco Medina
Publication year - 2014
Publication title -
journal of chemical technology and biotechnology
Language(s) - English
Resource type - Journals
SCImago Journal Rank - 0.64
H-Index - 117
eISSN - 1097-4660
pISSN - 0268-2575
DOI - 10.1002/jctb.4412
Subject(s) - catalysis , oxalic acid , phenol , calcination , chemistry , hydrogen peroxide , leaching (pedology) , mineralization (soil science) , acetic acid , inorganic chemistry , nuclear chemistry , organic chemistry , nitrogen , environmental science , soil science , soil water
BACKGROUND Improved Fe 2 O 3 /Al 2 O 3 catalysts were studied for the catalytic oxidation of concentrated phenol solutions (5 g L −1 ) with H 2 O 2 . To enhance catalyst stability, two strategies were investigated: the use of a high calcination temperature and a step of immersion into an organic acid solution. The reaction runs were performed in a continuous reactor at 70°C and atmospheric pressure. RESULTS For all the catalysts, almost complete phenol degradation was achieved. The mineralization levels were incomplete, reaching 60 and 50% for the catalysts treated with acetic and oxalic acid, respectively. The leaching levels were reduced from 25% (for the untreated catalyst) to 11% after the immersion in oxalic acid. In all cases, the formation of reversible carbonaceous deposits was observed during reaction and a progressive decay in phenol, TOC and H 2 O 2 conversions was registered. CONCLUSION Catalyst resistance to leaching was significantly enhanced by combining both thermal and acidic treatments. These procedures did not affect the catalytic wet hydrogen peroxide oxidation ( CWHPO ) performance in terms of mineralization levels. The lixiviation levels were acceptable, taking into account the strong acidic reaction medium. Deactivation processes might be primarily associated with the formation of reversible carbonaceous deposits due to intermediates accumulation onto the catalyst surface. © 2014 Society of Chemical Industry