A mechanistic kinetic model for phenol degradation by the Fenton process

2010 ◽  
Vol 176 (1-3) ◽  
pp. 402-413 ◽  
Author(s):  
Ricardo F.F. Pontes ◽  
José E.F. Moraes ◽  
Amilcar Machulek Jr. ◽  
José M. Pinto
2008 ◽  
Vol 7 (1) ◽  
pp. 9-12 ◽  
Author(s):  
Ilie Siminiceanu ◽  
Carmen-Ionela Alexandru ◽  
Eric Brillas

2007 ◽  
Vol 6 (6) ◽  
pp. 479-482
Author(s):  
Ilie Siminiceanu ◽  
Beatrice Iurascu ◽  
Miguel Vincente

Catalysts ◽  
2021 ◽  
Vol 11 (8) ◽  
pp. 943
Author(s):  
Kaouther Kerboua ◽  
Oualid Hamdaoui ◽  
Naoufel Haddour ◽  
Abdulaziz Alghyamah

The present paper investigates the potential of the Galvano-Fenton process as an advanced technique in terms of the simultaneous oxidation of a model pollutant, phenol, and the energy release and saving as compared to conventional electrochemical techniques, namely, Fenton, Fenton-like, and Electro-Fenton. A numerical model describing the electrochemical, electrolytic, and phenol’s mineralization reactions is presented. Simulations are conducted to predict the kinetics of ferrous and ferric ions, radicals’ formation, and phenol degradation along with released power. Parametric analysis and comparisons are also performed between the basic configuration of the Galvano-Fenton process and its upgraded version integrating a pre-immersion stage of the electrodes in the electrolyte equivalent to 25% of the total experiment’s duration. The ratio of the initial concentration of H2O2 to the concentration of the released/added Fe2+ catalyst is varied from 10 to 30. The effect of phenol concentration is inspected over the range of 0.188 to 10 mg/L as well. Compared to conventional Fenton-based techniques, the Galvano-Fenton process demonstrated a higher performance by reaching 1.34% of degradation efficiency per released J. This is associated with the generation of hydroxyl radicals of 0.047 nM/released J with initial concentrations of hydrogen peroxide and phenol of 0.187 mM and 2 µM, respectively. Moreover, the integration of the pre-immersion stage allowed the overcoming the barrier of the null degradation rate at the initial instant.


2008 ◽  
Vol 59 (10) ◽  
Author(s):  
Beatrice Iurascu ◽  
Ilie Siminiceanu ◽  
Miguel Vicente

A new photo- Fenton catalyst has been manufactured from synthetic layered clay laponite (Laponite RD) by the pillaring technique. Eight different catalyst samples were prepared: four without thermal aging (WTA) calcined at 523 K, 623 K, 723 K and 823 K, and other four with thermal aging (TA) calcined at the same temperatures. The samples have been characterized by XRD and SEM/ EDS techniques, and through the bulk chemical analysis. The results of this characterization have been previously reported [8]. This paper presents the results regarding the activity of the catalyst samples, determined for the phenol degradation in water by the photo- Fenton process, using an aqueous solution of 0.1 mM concentration in the presence of 5mM H2O2, 1g/L catalyst, pH3, and 303 K. The activity of each catalyst sample was evaluated through the apparent first order rate constant derived from the experimental kinetic curves, representing the phenol conversion (XPh) versus reaction time.The best results were obtained with the TA- 623 catalyst.


2014 ◽  
Vol 70 (5) ◽  
pp. 780-786 ◽  
Author(s):  
Layla F. A. Freire ◽  
Fabiana Valéria da Fonseca ◽  
Lidia Yokoyama ◽  
Luiz Alberto Cesar Teixeira

This study evaluated the use of a Fenton's reaction in a falling film solar reactor (FFR), as a possible advanced oxidation process for the mineralization of the organic compound phenol in water. Preliminary tests were carried out to evaluate phenol degradation by photolysis and to select the optimal residence time in which to carry out the process using a solar photo-Fenton system. The variables studied were the initial phenol concentration (100 to 300 mg L−1), the [Phenol]:[H2O2] mass ratio (1.0 to 2.0) and the [H2O2]/[Fe2+] molar ratio (5 to 10). Phenol degradation of 99% and chemical oxygen demand (COD) reduction of 97% were obtained under the following reaction conditions: phenol concentration = 200 mg L−1, mass ratio [Phenol]:[H2O2] = 1.5 and molar ratio [H2O2]/[Fe2+] = 7.5. Overall mineralization was achieved using the solar photo-Fenton process to destroy phenol and COD. The solar photo-Fenton process using a FFR appears to be a viable method for removing phenols in wastewaters on an industrial scale.


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