1Laboratory of Catalysis and Synthesis in Organic Chemistry (LCSCO) Abou Bekr Belkaid University of Tlemcen, BP 119, 13000 Tlemcen, Algeria
2Laboratory of Materials Chemistry (LCM), University Oran1 “Ahmed Ben Bella”, BP 1524, El-Menaouer, 31000 Oran, Algeria
BibTex Citation Data :
@article{BCREC20545, author = {Farah Guitouni and Ilhem Rekkab-Hammoumraoui and Sanaa El Korso and Mohamed Sassi and Chewki Ziani-Cherif}, title = {Ceria-Promoted Titanium Dioxide (CeO2/TiO2) Nanocomposites for Efficient Phenol Removal under Advanced Oxidation Processes (AOPs)}, journal = {Bulletin of Chemical Reaction Engineering & Catalysis}, volume = {21}, number = {1}, year = {2026}, keywords = {Cerium doped titanium dioxide; Phenol; Advanced oxidation processes; Hydrogen peroxide; UV irradiation. }, abstract = { In this study, a series of x %CeO 2 /TiO 2 (x= 1, 2, 3, 5 and 10) catalysts were successfully synthesized with Ce(NO 3 ) 3 .6H 2 O as precursor via a simple wetness impregnation method. The resulting samples were characterized by XRD, FTIR, surface area and pore volume measurements, Raman spectroscopy, SEM, and UV-Vis -DRS. These catalysts were used for the degradation of the phenol through three types of advanced oxidation processes (AOPs), namely the heterogeneous Fenton process (photocatalyst/H 2 O 2 ), the photocatalysis process (photocatalyst/UV), and the photo-Fenton process (photocatalyst/UV/H 2 O 2 ). The 10 % CeO 2 /TiO 2 catalyst showed superior degradation efficiency of 99.05 %, when used in the heterogeneous photo-Fenton process. To determine the optimal conditions for phenol degradation, using the heterogeneous photo-Fenton process, the effects of parameters such as photocatalyst dosage, initial pH, phenol concentration, H 2 O 2 volume, and temperature were investigated. The optimal conditions were as follows: 0.1 g of catalyst, 0.6 mM of hydrogen peroxide, a reaction temperature of 25 °C, an initial pH of 8, an initial phenol concentration of 30 ppm, and a reaction time of 240 minutes. The impact of radical scavengers (such as p-benzonquinone, silver nitrate, EDTA-2Na and propan-2-ol) on degradation efficiency was also studied. For all three oxidation processes, phenol photodegradation could be described by the pseudo-first-order kinetics according to the Langmuir-Hinshelwood model. Furthermore, the catalysts could be easily recovered from the reaction solution by centrifugation and reused for five cycles without significant loss of activity. Copyright © 2026 by Authors, Published by BCREC Publishing Group. This is an open access article under the CC BY-SA License ( https://creativecommons.org/licenses/by-sa/4.0 ). }, issn = {1978-2993}, pages = {191--212} doi = {10.9767/bcrec.20545}, url = {https://journal.bcrec.id/index.php/bcrec/article/view/20545} }
Refworks Citation Data :
In this study, a series of x %CeO2/TiO2 (x= 1, 2, 3, 5 and 10) catalysts were successfully synthesized with Ce(NO3)3.6H2O as precursor via a simple wetness impregnation method. The resulting samples were characterized by XRD, FTIR, surface area and pore volume measurements, Raman spectroscopy, SEM, and UV-Vis -DRS. These catalysts were used for the degradation of the phenol through three types of advanced oxidation processes (AOPs), namely the heterogeneous Fenton process (photocatalyst/H2O2), the photocatalysis process (photocatalyst/UV), and the photo-Fenton process (photocatalyst/UV/H2O2). The 10 % CeO2/TiO2 catalyst showed superior degradation efficiency of 99.05 %, when used in the heterogeneous photo-Fenton process. To determine the optimal conditions for phenol degradation, using the heterogeneous photo-Fenton process, the effects of parameters such as photocatalyst dosage, initial pH, phenol concentration, H2O2 volume, and temperature were investigated. The optimal conditions were as follows: 0.1 g of catalyst, 0.6 mM of hydrogen peroxide, a reaction temperature of 25 °C, an initial pH of 8, an initial phenol concentration of 30 ppm, and a reaction time of 240 minutes. The impact of radical scavengers (such as p-benzonquinone, silver nitrate, EDTA-2Na and propan-2-ol) on degradation efficiency was also studied. For all three oxidation processes, phenol photodegradation could be described by the pseudo-first-order kinetics according to the Langmuir-Hinshelwood model. Furthermore, the catalysts could be easily recovered from the reaction solution by centrifugation and reused for five cycles without significant loss of activity. Copyright © 2026 by Authors, Published by BCREC Publishing Group. This is an open access article under the CC BY-SA License (https://creativecommons.org/licenses/by-sa/4.0).
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