Title of article
Landfill leachate treatment by solar-driven AOPs
Author/Authors
Elisangela M.R. Rocha a، نويسنده , , V?´tor J.P. Vilar b، نويسنده , , ?، نويسنده , , Ame´lia Fonseca c، نويسنده , , Isabel Saraiva c، نويسنده , , Rui A.R. Boaventura، نويسنده ,
Issue Information
ماهنامه با شماره پیاپی سال 2011
Pages
11
From page
46
To page
56
Abstract
Sanitary landfill leachate resulting from the rainwater percolation through the landfill layers and waste material decomposition is a
complex mixture of high-strength organic and inorganic compounds which constitutes serious environmental problems. In this study,
different heterogeneous (TiO2/UV, TiO2/H2O2/UV) and homogenous (H2O2/UV, Fe2+/H2O2/UV) photocatalytic processes were investigated
as an alternative for the treatment of a mature landfill leachate. The addition of H2O2 to TiO2/UV system increased the reduction
of the aromatic compounds from 15% to 61%, although mineralization was almost the same. The DOC and aromatic content abatement
is similar for the H2O2/UV and TiO2/H2O2/UV processes, although the H2O2 consumption is three times higher in the H2O2/UV system.
The low efficiency of TiO2/H2O2/UV system is presumably due to the alkaline leachate solution, for which the H2O2 becomes highly
unstable and self-decomposition of H2O2 occurs. The efficiency of the TiO2/H2O2/UV system increased 10 times after a preliminary
pH correction to 4. The photo-Fenton process is much more efficient than heterogeneous (TiO2, TiO2/H2O2/UV) or homogeneous
(H2O2/UV) photocatalysis, showing an initial reaction rate more than 20 times higher, and leading to almost complete mineralization
of the wastewater. However, when compared with TiO2/H2O2/UV with acidification, the photo-Fenton reaction is only two times faster.
The optimal initial iron dose for the photo-Fenton treatment of the leachate is 60 mg Fe2+ L 1, which is in agreement with path length
of 5 cm in the photoreactor. The kinetic behaviour of the process (60 mg Fe2+ L 1) comprises a slow initial reaction, followed by a firstorder
kinetics (k = 0.020 L kJ 1
UV, r0 = 12.5 mg kJ 1
UV), with H2O2 consumption rate of kH2O2 = 3.0 mmol H2O2 kJ 1
UV, and finally, the third
reaction period, characterized by a lower DOC degradation and H2O2 consumption until the end of the experiment, presumably due to
the formation of low-molecular-weight carboxylic groups. A total of 306 mM of H2O2 was consumed for achieving 86% mineralization
(DOCfinal = 134 mg L 1) and 94% aromatic content reduction after 110 kJUV L 1, using an initial iron concentration of 60 mg Fe2+ L 1.
2010 Elsevier Ltd. All rights reserved
Keywords
UV/H2O2 , Fe2+/H2O2/UV , TiO2/H2O2/UV , Sanitary landfill leachate , Pilot Plant with CPCs , Solar-driven AOPs
Journal title
Solar Energy
Serial Year
2011
Journal title
Solar Energy
Record number
940476
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