Copper removal from industrial wastewaters by means of electrostatic shielding

Electrostatic shielding zones made of electrode graphite powder were used as a new type of ionic and electronic currentsinks. Because of the local elimination of the applied electric field, voltage and current within the zones, ions are led insidethem and accumulate there. We implemented the current sinks in electrodialysis of a simulated copper plating rinse watercontaining 100 mg L-1 Cu2+ ions and electrodeionization of a 0.001 M CuSO4 solution with simultaneous electrochemicalregeneration of the used ion exchange resin beds and obtained pure water with a Cu2+ ion concentration of less than 0.12 mgL-1 at a flow rate of 1.29x10-4 L s-1 diluate stream and a current density of 2 mA cm-2

Removal of Sulfide and COD from a Crude Oil Wastewater Model by Aluminum and Iron Electrocoagulation

The treatment of petroleum wastewater was studied using the electrocoagulation process with aluminum and iron electrodes aiming to simultaneous removal of sulfide and COD. All affecting parameters, such as solution pH, applied current density, time of electroprocessing, electrode material and addition of surfactant, were investigated. Sulfide was rapidly and effectively removed using iron electrodes. The removal of COD was effectively effectively enhanced by performing the electrocoagulation process after addition of the surfactant polyethylene glycol oleate

Design and Application of Electrochemical Processes for Decolorization Treatment of Nylanthrene Red dye Bearing Wastewaters

The purpose of this paper is the investigation of the capability of electrochemical methods, such as electrocoagulation, electrooxidation and electro-Fenton for decolorization and degradation of synthetic aqueous solutions and actual dye house effluents containing nylanthrene red reactive dye. All electrochemical experiments with the synthetic dye solutions were conducted in electrochemical cell of volume 500 ml containing 200 mL of dye solution at concentration 50 mg/L and interelectrode distance of 1 cm. The three different electrochemical processes were analyzed, and their removal efficiencies were measured and evaluated. In addition, a flow diagram is designed for a continuously operated electrochemical process for remediation of synthetic and actual dye house effluents laden with nylanthrene dye. In the electrocoagulation process with aluminum electrodes, the colored aqueous dye solution was treated at the applied current densities of 5, 10 and 15 mA/cm2 and was quantitatively decolorized in 11, 9 and less than 6 minutes of electroprocessing time respectively. The electrooxidation process conducted with Ti/Pt and boron doped diamond (BDD) electrodes, at the applied current density of 10 mA/cm2 led to the quantitative decolorization and destruction of the dye in 25 and 15 min respectively. In the electro-Fenton process with iron electrodes, supply of added hydrogen peroxide and applied current density of 10 mA/cm2, complete decolorization and degradation of the nylanthrene red dye occurred in 6 min. The actual polyamide textile dyeing effluent of same volume 200 mL with initial turbidity of 114 NTU and COD of 1755 mg/L was treated by electrocoagulation at the same applied current density of 10 mA/cm2. The turbidity was quantitatively eliminated in only 10 min, while COD was reduced by 74.5 % in 40 minutes of electrolysis time

Decolorization Treatment of Copper Phthalocyanine Textile Dye Wastewater by Electrochemical Methods

Electrochemical decolorization and degradation treatment of aqueous copper phthalocyanine reactive dye solutions was comparatively studied by electrocoagulation, electrooxidation and electro-Fenton processes. In the electrocoagulation process with aluminum electrodes the colored aqueous solutions of initial pH 6.4 containing 50 mg L-1 copper phthalocyanine and 6 g L-1 NaCl were treated at applied current densities of 2.5 and 5 mA cm-2. Fast and 100% decolorization was achieved in 4 and 2 minutes of electroprocessing respectively. The indirect electrooxidation process was conducted in acidic electrolyte solutions containing 50 mg L-1 copper phthalocyanine and 6 g L-1 NaCl with Ti/Pt and graphite plate electrodes at the applied current density of 10 mA cm-2. Even after 90 minutes of electrolysis time the dye remained by 23 and 18.8 % respectively undegradable. By the direct and indirect electrooxidation with the same amount of Na2SO4 electrolyte and added H2O2 respectively and using the same electrodes, the copper phthalocyanine dye was not or was only barely degraded respectively. In the electro-Fenton process with Fe electrodes and added amounts of H2O2 at pH 3 and an applied current density of 5 mA/cm2 complete degradation of copper phthalocyanine occurred in 15 minutes

Evaluation of Potable Groundwater Quality Using Environmetrics. The case of Nestos and Strymon River Regions, Northern Greece

In the present study potable water samples were regularly collected from two geographical regions in Northern Greece. The two regions are close to the Nestos and Strymon Rivers. Throughout 2015, samples from 13 sites were collected and analyzed with a frequency of three times per each quarter for the following parameters: chloride, calcium, nitrate, potassium, electric conductivity and total hardness. The main objective of this study was to investigate the effects of the geographical region and seasonal influence on the above parameters regarding the limits of the 98/83/EC Directive. The findings of the Linear Mixed Effects modeling revealed statistically significant main effects of both factors on the examined parameters. © 2021 School of Science, IHU. All rights reserved