The main goal of this study is to investigate the effectiveness of modified Electro-Fenton process (EF-Fere) involving ferrous ions regeneration coupled with direct oxidation method on COD reduction of paint manufacturing wastewater. The present Electro-Fenton cell consisted of stainless steel porous cathode and lead anode covered by PbO2 film. The performance was measured through studying the effect of different parameters on the percentage of COD removal such as: ferric ions concentration, initial concentration of wastewater, current density and irradiation of UV light. The parameters showed high COD removal efficiency 99% for highly contaminated wastewater of 13000 mg/l COD in acidic medium pH=2 at continuous H2O2 feeding dosage of 1.4 ml/min and current density = 19 mA/cm2 in presence of UV light.
Published in | American Journal of Chemical Engineering (Volume 4, Issue 1) |
DOI | 10.11648/j.ajche.20160401.11 |
Page(s) | 1-8 |
Creative Commons |
This is an Open Access article, distributed under the terms of the Creative Commons Attribution 4.0 International License (http://creativecommons.org/licenses/by/4.0/), which permits unrestricted use, distribution and reproduction in any medium or format, provided the original work is properly cited. |
Copyright |
Copyright © The Author(s), 2016. Published by Science Publishing Group |
Paint Manufacturing Wastewater, Fe2+ Generation, EF-Fere, COD Removal, Direct Oxidation, UV/EF-Fere
[1] | Dey, Hashim M, Hassan S (2004) Micro filtration of water-based paint effluents, Adv. in Environ. Res. 8, p. 455-466. |
[2] | Huang Y, Chang P, Chen C (2008) Comparative study of oxidation of dye-Reactive Black B by different advanced oxidation processes. Jr. of Haz. Mat. 154, p. 655–662. |
[3] | Torrades F, García-Hortal J, Domènech X (2002) Removal of organic contaminants in paper pulp treatment effluents under Fenton and photo-Fenton conditions. Applied Catalysis B: Environmental 36 (1), p. 63–74. |
[4] | Xia M, Long M, Yang Y, Chen C, Cai W, Zhou B (2011) a highly active bimetallic oxides catalyst supported on Al-containing MCM-41 for Fenton oxidation of phenol solution, Appl. Catal. B: Environ. 110, p. 118-125. |
[5] | Bremmer D, Burgess A, Houllemare D, Namkung K (2006) Appl. Catal. B: Environ. 63, pp. 15. |
[6] | Zhang A, Wang N, Zhou J (2012) Heterogeneous Fenton-like catalytic removal of p-nitrophenol in water using acid-activated fly ash, J. Hazard. Mater. 201, p. 68. |
[7] | Luis A, Miguel A, Antonio G (2011) Chem. Eng. J. 178, P. 146. |
[8] | Ayodele O, Lim J, Hameed B (2012) Pillared montmorillonite supported ferric oxalate as heterogeneous photo-Fenton catalyst for degradation of amoxicillin, Appl. Catal. A-Gen. 413, P. 301. |
[9] | Youssef S, Ines W, Ridha A, Kinetic degradation of the pollutant guaiacol by dark Fenton and solar photo Fenton processes (2001), Environ. Sci. pollut. Res. 18, p. 1497. |
[10] | Lypczynska-Kochany E (1993) Hydrogen peroxide mediated photodegradation of phenol as studied by a flash photolysis/HPLC technique, Environ. Pollut. 80, P. 147–152. |
[11] | Maciel R, Sant-Anna G, Dezotti M (2004) Phenol removal from high salinity effluents using Fenton's reagent and photo-Fenton reactions, Chemosphere, 57, P. 711. |
[12] | Wang W, Kalck P, Faria J (2005) visible light photo degradation of phenol on MWCNT TiO2 composite catalysts prepared by a modified sol-gel method Mol. Catal. A Chem., 235, P. 194. |
[13] | Herrmann J (1999) Fundamentals and applications to the removal various types of aqueous pollutants, Catal. Today, 53, p. 115. |
[14] | Boye B, Dieng M, Brillas E (2002) Degradation of herbicide 4-chlorophenoxyacetic acid by advanced electrochemical oxidation methods, Environ. Sci. Technol., 36, p. 3030. |
[15] | Brillas E, Calpe J, Casado J (2000) Mineralization of 2, 4-D by advanced electrochemical oxidation, Water Res., 34, p. 2253. |
[16] | Qiang Z, Chang J, Huang C (2002) Electrochemical generation of hydrogen peroxide from dissolved oxygen in acidic solution, Water Res., 36, P. 85. |
[17] | Gozmen B, Oturan M, Oturan N (2003), Environ. Sci. Technol., 37, P. 3716. |
[18] | Fernandes A, Morao A, Magrinho M, Lopes A, Goncalves I (2004) Electrochemical degradation of C. I. Acid orange 7, Dyes Pigments., 61, p. 287–296. |
[19] | Clesceri L, Greenberg A, Andrew D (1998) Standard methods for the examination of water and wastewater. 20, p. 312. |
[20] | Li J, Xuhui M (2012) Degradation of Phenol-containing Wastewater Using an Improved Electro-Fenton Process, Int. J. Electrochem. Sci. 7, P. 4078 – 4088. |
[21] | Naimi I, Bellakhal N (2012) Removal of 17β-Estradiol by Electro-Fenton Process, Materials Sciences and Applications, 3, P. 880-886. |
[22] | Vasilica A, Igor C, Doina L, Constantin L, Ioannis P (2015) enhancing the fenton process by UV light applied in textile wastewater treatment., Environmental Engineering and Management Journal. 14, P. 595-600. |
APA Style
Ahmed Mostafa Sadek, Riham Ali Hazzaa, Mohamed Hussien Abd-El-Magied. (2016). Study on the Treatment of Effluents from Paint Industry by Modified Electro-Fenton Process. American Journal of Chemical Engineering, 4(1), 1-8. https://doi.org/10.11648/j.ajche.20160401.11
ACS Style
Ahmed Mostafa Sadek; Riham Ali Hazzaa; Mohamed Hussien Abd-El-Magied. Study on the Treatment of Effluents from Paint Industry by Modified Electro-Fenton Process. Am. J. Chem. Eng. 2016, 4(1), 1-8. doi: 10.11648/j.ajche.20160401.11
AMA Style
Ahmed Mostafa Sadek, Riham Ali Hazzaa, Mohamed Hussien Abd-El-Magied. Study on the Treatment of Effluents from Paint Industry by Modified Electro-Fenton Process. Am J Chem Eng. 2016;4(1):1-8. doi: 10.11648/j.ajche.20160401.11
@article{10.11648/j.ajche.20160401.11, author = {Ahmed Mostafa Sadek and Riham Ali Hazzaa and Mohamed Hussien Abd-El-Magied}, title = {Study on the Treatment of Effluents from Paint Industry by Modified Electro-Fenton Process}, journal = {American Journal of Chemical Engineering}, volume = {4}, number = {1}, pages = {1-8}, doi = {10.11648/j.ajche.20160401.11}, url = {https://doi.org/10.11648/j.ajche.20160401.11}, eprint = {https://article.sciencepublishinggroup.com/pdf/10.11648.j.ajche.20160401.11}, abstract = {The main goal of this study is to investigate the effectiveness of modified Electro-Fenton process (EF-Fere) involving ferrous ions regeneration coupled with direct oxidation method on COD reduction of paint manufacturing wastewater. The present Electro-Fenton cell consisted of stainless steel porous cathode and lead anode covered by PbO2 film. The performance was measured through studying the effect of different parameters on the percentage of COD removal such as: ferric ions concentration, initial concentration of wastewater, current density and irradiation of UV light. The parameters showed high COD removal efficiency 99% for highly contaminated wastewater of 13000 mg/l COD in acidic medium pH=2 at continuous H2O2 feeding dosage of 1.4 ml/min and current density = 19 mA/cm2 in presence of UV light.}, year = {2016} }
TY - JOUR T1 - Study on the Treatment of Effluents from Paint Industry by Modified Electro-Fenton Process AU - Ahmed Mostafa Sadek AU - Riham Ali Hazzaa AU - Mohamed Hussien Abd-El-Magied Y1 - 2016/01/25 PY - 2016 N1 - https://doi.org/10.11648/j.ajche.20160401.11 DO - 10.11648/j.ajche.20160401.11 T2 - American Journal of Chemical Engineering JF - American Journal of Chemical Engineering JO - American Journal of Chemical Engineering SP - 1 EP - 8 PB - Science Publishing Group SN - 2330-8613 UR - https://doi.org/10.11648/j.ajche.20160401.11 AB - The main goal of this study is to investigate the effectiveness of modified Electro-Fenton process (EF-Fere) involving ferrous ions regeneration coupled with direct oxidation method on COD reduction of paint manufacturing wastewater. The present Electro-Fenton cell consisted of stainless steel porous cathode and lead anode covered by PbO2 film. The performance was measured through studying the effect of different parameters on the percentage of COD removal such as: ferric ions concentration, initial concentration of wastewater, current density and irradiation of UV light. The parameters showed high COD removal efficiency 99% for highly contaminated wastewater of 13000 mg/l COD in acidic medium pH=2 at continuous H2O2 feeding dosage of 1.4 ml/min and current density = 19 mA/cm2 in presence of UV light. VL - 4 IS - 1 ER -