Séminaire
Pollutant degradation processes triggered by magnetic materials
Date
le 25-10-2017 à 14:00Lieu Salle de Conférences, ISM, 3ème étage Est, Bât. A12, Université de Bordeaux
Intervenant(s) Davide VIONE, enseignant-chercheur, Université de Turin (UNITO) |
Résumé
The Fenton reaction is a promising technique for the abatement of pollutants in water and wastewater and it is currently finding applications in the fields of environmental remediation and industrial wastewater treatment. It has been developed into several variants, including the thermal (dark) process and the photo-Fenton one, which makes preferably use of solar radiation. The (photo-)Fenton process is based on Fe(II) and H
2O
2 to produce oxidizing species (most notably, but not exclusively, the hydroxyl radical) [1]. The two reactants can be provided as such or generated photochemically, electrochemically or sonochemically from several precursors, giving rise to the different variants of the Fenton reaction. Moreover, the use of other metals or peroxides in the same process has given rise to the vast Fenton-like family of reactions [2].
A major drawback of the classical Fenton process is that Fe(II) + H
2O
2 yields Fe(III), insoluble at the ~neutral pH at which treated water is used or discharged, giving a slurry as process waste. The use of ligands to keep Fe(III) dissolved is an option [3], but residual dissolved Fe could easily exceed the water quality requirements and, in this case, a precipitation step would still be needed. An alternative is the use of solid and Fenton-active Fe-containing materials, which provide a low amount of dissolved Fe(II) for Fenton operation and can be recycled for further reaction cycles. Solid recovery is easier with magnetic materials such as magnetite (Fe
3O
4) and Fe° (ZVI: zero-valent iron). On such bases, this talk describes the use of magnetite and ZVI in (photo-)Fenton and (photo-)Fenton-like processes.
Nanometric magnetite undergoes easy surface oxidation to Fe(III) and it is often inactive in the dark Fenton process, but it can be activated by UV irradiation. In this case, one can produce °OH radicals with Fe
3O
4 + H
2O
2 + UV [4], and SO
42-° radicals with Fe
3O
4 + S
2O
82- + UV [5]. The latter process yields SO
42-° that is a more selective oxidant than °OH and can often achieve decontamination with limited interference from dissolved organic matter [2]. Non-stoichiometric magnetite, with a Fe(II) excess in the inner lattice is to be preferred over stoichiometric Fe
3O
4 because of its much higher activity. ZVI + H
2O
2 triggers a dark Fenton reaction and it enables the use of passivated ZVI, which is a spent residual (waste) of ZVI-based reductive decontamination treatments (e.g., of chlorinated hydrocarbons). One can achieve further oxidative degradation of already dechlorinated compounds by just adding H
2O
2 to the residues of the dechlorination step.
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[2] S. Gligorovski, R. Strekovski, S. Barbati and D. Vione, Chem. Rev., 2015, 115, 13051.
[3] W. Y. Huang, M. Brigante, F. Wu, C. Mousty, K. Hanna and G. Mailhot, Environ. Sci. Technol., 2013, 47, 1952.
[4] M. Minella, G. Marchetti, E. De Laurentiis, M. Malandrino, V. Maurino, C. Minero, D. Vione and K. Hanna, Appl. Catal., B, 2014, 154, 102.
[5] P. Avetta, A. Pensato, M. Minella, M. Malandrino, V. Maurino, C. Minero, K. Hanna and D. Vione, Environ. Sci. Technol., 2015, 49, 1043.