Oxidation of nitrobenzene by ozone in the presence of faujasite zeolite in a continuous flow gas–liquid–solid reactor

Author:

Reungoat J.12,Pic J. S.1,Manéro M. H.3,Debellefontaine H.1

Affiliation:

1. Université de Toulouse, LISBP, UMR INSA/CNRS 5504 & UMR INSA/INRA 792, 135 Avenue de Rangueil, 31077 Toulouse Cedex 4, France E-mail: Jean-Stephane.Pic@insa-toulouse.fr; debelle@insa-toulouse.fr

2. Present address: The University of Queensland, Advanced Water Management Centre (AWMC), Brisbane Qld 4072, Australia E-mail: j.reungoat@awmc.uq.edu.au

3. Université de Toulouse, LGC, UMR CNRS 5503, IUT GCGP, 137 Avenue de Rangueil, 31077 Toulouse Cedex 4, France E-mail: marie-helene.manero@iut-tlse3.fr

Abstract

This work investigates the oxidation of nitrobenzene (NB) by ozone in the presence of faujasite zeolite. Experiments were carried out in a gas–liquid–solid reactor were ozone transfer and NB oxidation took place at the same time. Three configurations of the reactor were compared: empty, filled with inert glass beads and filled with faujasite pellets. First, ozone transfer coefficient (kLa) and decomposition rate constant (kC) were determined for each configuration. In presence of solid, kLa was 2.0 to 2.6 times higher and kC was 5.0 to 6.4 times higher compared to the empty reactor. Then, the various configurations were evaluated in terms of NB removal and chemical oxygen demand (COD) decrease. The faujasite reactor showed higher removal of NB and decrease of COD compared to other configurations under the same conditions suggesting that the faujasite increases the oxidation rate of NB. Oxidation of NB in presence of faujasite also proved to be limited by the transfer of ozone from the gas to the liquid phase.

Publisher

IWA Publishing

Subject

Water Science and Technology,Environmental Engineering

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