Removal of phenol from steel wastewater by combined electrocoagulation with photo-Fenton Mohammad Malakootian and Mohammad Reza Heidari ABSTRACT Phenol and its derivatives are available in various industries such as reneries, coking plants, steel mills, drugs, pesticides, paints, plastics, explosives and herbicides industries. This substance is carcinogenic and highly toxic to humans. The purpose of the study was to investigate the removal of phenol from wastewater of the steel industry using the electrocoagulationphoto-Fenton (EC-PF) process. Phenol and chemical oxygen demand (COD) removal efciency were investigated using the parameters pH, Fe 2þ /H 2 O 2 , reaction time and current density. The highest removal efciency rates of phenol and COD were 100 and 98%, respectively, for real wastewater under optimal conditions of pH ¼ 4, current density ¼ 1.5 mA/cm 2 , Fe 2þ /H 2 O 2 ¼ 1.5 and reaction time of 25 min. Combination of the two effective methods for the removal of phenol and COD, photocatalytic electrocoagulation photo-Fenton process is a suitable alternative for the removal of organic pollutants in industry wastewater because of the low consumption of chemicals, absence of sludge and other side products, and its high efciency. Mohammad Malakootian Environmental Health Engineering Research Center, Kerman University of Medical Sciences, Kerman, Iran and Department of Environmental Health, School of Public Health, Kerman University of Medical Sciences, Kerman, Iran Mohammad Reza Heidari (corresponding author) Environmental Health Engineering, Department of Environmental Health, School of Public Health, Bam University of Medical Sciences, Bam, Iran E-mail: moheidari86@gmail.com Key words | electrocoagulation, phenol, photo-Fenton, steel plant INTRODUCTION One widespread form of organic chemical pollutant is phenol and its compounds, which are found in industrial wastewater (Malakootian et al. ). These compounds are very dangerous because of their high toxicity and harm- ful impact on the environment. High concentrations of phenol and its compounds are commonly found in efuent from oil reneries and industries such as petrochemicals, ceramics, coke and steel, coal conversion processes, resin manufacturing, drugs, pesticides, plastics, explosives and herbicides industries (Alizadeh et al. ). The presence of phenol in drinking and irrigation water is a serious threat to the health of humans, animals, plants and microor- ganisms (Fajardo et al. ). Phenol is highly carcinogenic to humans and causes signicant health concerns even at low concentrations (Farhadi et al. ). Its toxic effects include permeating cell membranes and cytoplasmic coagulation. The standard amount of phenol in drinking water is 0.5 mg, while the limit for efuent from industrial waste output is 1 mg/L. There are many methods for phenol removal, which include adsorption (Liu et al. ), chemical oxidation (Hernández-Francisco et al. ), biological methods (Priyadharshini & Bakthavatsalam ), distillation, extraction, ion exchange, membrane pro- cess, reverse osmosis and electrochemical techniques (Víctor-Ortega et al. ). Physical methods for removal of phenol are expensive and inefcient. Presently, chemical methods are not used due to their disadvantages such as high maintenance costs, sludge issues and disposal problems. Electrooxidation methods are a good alternative for the treatment of organic pollutants (Farhadi et al. ). The conventional biological processes cannot be used for the complete treatment of industrial wastewater due to high toxicity and carcinogenicity, high chemical and physical resistance of the pollutants, and also, bacteria or fungi are sensitive to changes in the environmental parameters. Electrocoagulation (EC) has been used in the treatment of urban wastewater (Yavuz & Ögutveren ), efuents of oil (Gobbi et al. ), dyes (Khemila et al. ), antibiotics (Baran et al. ), sulfate (Mamelkina et al. ) and cad- mium (Malakootian et al. ). The EC process involves the formation of metallic hydroxides in the efuent by dis- solving the electrodes (anodes), usually formed by iron or aluminum. A coagulant with no impurities or extra metal 1260 © IWA Publishing 2018 Water Science & Technology | 78.6 | 2018 doi: 10.2166/wst.2018.376 Downloaded from http://iwaponline.com/wst/article-pdf/78/6/1260/504547/wst078061260.pdf by guest on 22 July 2022