amir shabanlo

Backgrond: Pharmaceutical products, particularly antibiotics such pollutants are evolving due to the cumulative effects, adverse effects and drug resistance is a major concern in the control environment. The purpose of this work is to investigate the feasibility and potential of iron nanoparticles in the aqueous solution being removed antibiotics.
In this study, the performance activated persulfate with zero-valent Zinc nanoparticles in the presence of ultrasound in the analysis of antibiotics was investigated. The effect of process parameters such as pH of the solution (2.97-10.53), concentration Potassium persulfate (194.33-1200mg/l) and the zero-valent zinc (12.73-147.27mg/l) in reaction time 0-180 min using a batch chamber ultrasonic were studied. A statistical procedure was used to optimize the parameters of the RSM model. Antibiotics are measured based on COD vials and DR-5000 spectrophotometer was used.
The results showed that the initial pH of the solution is the most important influential parameters. The addition of potassium persulfate and zero valent zinc in the samples was enhanced performance. Optimum efficiency achieved in 50 mg/l concentration antibiotics, potassium persulfate 1200 mg/l, the zero- zinc 120 mg /l, pH 4.5.
The results of this study demonstrate acceptable performance persulfate activated process with zero-valent iron and zinc nanoparticles on ultrasound in the presence of antibiotic.

The Azo dyes due to presence of aromatic rings in structure are considered major problems into the environment. In this experimental study, the synergistic effect of persulfate and nano zero-valent iron in degradation of Acid Blue 113 in presence of ultrasonic irradiation was investigated.
The effect of operating parameter such as initial pH, different concentration of S2O82-, nZVI and initial dye using a batch ultrasound reactor at 40 kHz frequency was investigated. After the optimize process, synergistic dye degradation and COD reduction of colored solution was studied. For characterization of the prepared nZVI particle, transmission electron microscope (TEM) image was used.
To remove 99% dye with initial concentration of 50 mg/L, the optimal condition in the end of 30 min of reaction was pH 3, concentration of S2O82- and nZVI 5 mM and 50 mg/L, respectively. In the same of condition with increasing pH to 11 the dye removal efficiency decreased to 17%, respectively. After 120 min of reaction in the optimal condition, the COD reduction was 95%. Synergistic dye degradation in US/S2O82-/Fe0 process was observed 59%. The TEM image of the synthesized nZVI confirmed the nanoscale Creation.
The US/S2O82-/Fe0 combined process due to high synergistic degradation, can be promising process to industrial wastewater treatment.

Phenol, or benzene hydroxyl is a toxic aromatic hydrocarbon discharged into the environment through certian industrial effluents which, thereby, pollute water resources. This study examines phenol removal from aqueous solutions through electro-Fenton and electro/persulfate processes using iron electrodes. For this purpose, a laboratory-scale electrochemical batch reactor was used that was equipped with four electrodes and a direct DC power supply. In the tests carried out, the effects of operational parameters such as initial pH; current density; and initial concentrations of phenol, hydrogen peroxide, and persulfate on the removal of phenol were investigated. The results showed that EPS and EF processes achieved phenol removal efficiencies of 95.18% and 93.99%, respectively, at operating conditions of pH = 3, initial phenol concentration of 100 mg/l, hydrogen peroxide and persulfate concentration of 0. 4 mM, and a current density 0.07A/dm2 over 45 min. Increasing persulfate and hydrogen peroxide concentration from 0.4 to 0.8 mM reduced phenol removal efficiencies from 95.18% and 93.99% to 43% and 85%, respectively. Generally speaking, EPS and EF processes exhibited almost identical phenol removal efficiencies. Finally, the integrated electrochemical and persulphate process was found to be more productive in producing electrical iron and persulphate activation than using each single process in isolation.

Two-valent iron ions can be used to activate persuphate anions. The objective of the present study was to investigate the electrical activation of persuphate anions and to determine the efficiency of electro-persulphate in the removal of ceftriaxone antibiotic from synthetic pharmaceutical effluents. For this purpose, a reactor (with an effective volume of 1 L) equipped with iron electrodes connected to a DC power supply was used and the effects of pH, voltage, persulphate content, and ceftriaxone initial concentration on the efficiency of the process were studied. Moreover, electrode corrosion, synergistic effects of the parameters studied, reaction kinetics, and chemical oxygen demand (COD) removal were studied. Results showed that the variables had a significant effect on process efficiency such that 96% of the ceftriaxone in the effluent was removed under the following optimum conditions: pH: 3, voltage: 10 V, a persulphate concentration of 50 mM/L, a ceftriaxone initial concentration of 0.18 mM/L, and a reaction time of 45 min. However, removal efficiency declined when the above conditions changed. It was also observed that COD removal was 72% in the optimum reaction time. Moreover, the process kintetics was found to be a first-order one. Application of an electrical process to active persulphate anion is assoiated with such advantages as reduced iron consumption and high antibiotic removal efficiency. Based on the results obtained, the proposed method may be recommended as an alternative for treating persistent pollutants to reduce environmental pollution.

Residual Azo dyes pose a major environment problem due to the benzene rings present in their structure. In this experimental study, the efficiencies of the US/H2O2/Fe2 and US/S2O82‒/Fe2 processes in degrading Acid Blue 113 Azo were investigated. For this purpose, the effects of the parameters involved in these processes such as initial solution pH in the range of 3 to 11, different concentrations of H2O2, and ‒S2O82 in the range of 1 to 10 mM, those of FeSO4 in the range of 0.1 to 1 mM, and different initial dye concenterations were investigated in a batch ultrasound reactor operated at 40 kHz. Also, the effects of aeration on process efficiency and fluctuations in the dye UV-Vis spectrum were investigated under optimum conditions. Based on the results obtained, dye removal efficiency decreased considerably in both processes with increasing pH such that maximum removal efficiency was obtained at pH 3 in both processes. Similarly dye removal efficiency decreased in both processes when FeSO4 concentration rose above 0.5 mM. The optimum conditions in the US/H2O2/Fe2 process to achieve a removal efficiency of 93.5% for an initial dye concentration of 50 mg/L involved H2O2 and FeSO4 concentrations of 2.5 and 0.05 mM, respectively. Under the same optimal conditions, the efficiency of the US/S2O82‒/Fe2 process was found to be 94.3% for a S2O82‒ concentration of 2.5 nM. These results suggest that the US/S2O82‒/Fe2 is more effective than the US/H2O2/Fe2 in reducing the 567 nm peak of the dye structure. Finally, examination of the changes in the UV-Vis spectra of Acid Blue 113 showed that the US/H2O2/Fe2 process led to greater declines in the 276 and 203 nm peaks.

A newly emerging environmental problem is the discharge of pharmaceutical effluents containing antibiotic compounds. Compared to common methods, the ozone/persulfate process is a novel measure for treating persistent pollutants. This process is highly efficient in removing pollutants by using the free radicals of sulfates as powerful oxidants. In this study, a semi-continuous reactor with a useful volume of 1 L was used to evaluate the performance of the ozone/persulfate process in treating the ciprofloxacin antibiotic at concentrations from 10 to 100 mg/L in the presence of 0 to 15 mM of persulfate in 30 min. The results showed that under the optimized operating conditions of pH = 3, persulfate dose = 10 mM, ozone dose = 1 g/h, and an initial antibiotic concentration of 10 mg/L, this method was capable of removing 96% of the contaminant. Moreover, the efficiency of the process was found to be a function of experimental conditions. Based on the results of this study, it may be concluded that the ozone/persulfate process can be considered as an appropriate process for treating persistent and non-biodegradable pollutants.

Nowadays, synthetic azo compounds as environmental pollutants are widely used in different application. In this research the treatability of effluent polluted with reactive black 5 azo dye using electrocoagulation (EC) and electrocoagulation/ flotation (ECF) processes with aluminum electrodes investigated in a lab scale batch experimental reactor.
In present study an electrocoagulation flotation reactor in a lab scale to an approximate volume of 1 liter which is equipped with four Al0Al electrodes with dimensions of 200*20*2 mm was proposed. The effects of operational parameters such as initial pH, current density, contact time, initial dye concentrations and flotation were evaluated.
Findings: The results indicated that the highest dye removal rates in the EC process were observed in natural pH of solutions, 12.71 mA/Cm2 current density and 100 mg/l initial dye concentration at 30 min contact time. In these conditions up to 81% of dye was removed in the EC process. Based on the result obtained in this study, it was found that much higher dyes removal could be achieved by ECF (86%) process than that by EC process in the same conditions.
EC and ECF processes using aluminum electrodes for dye removal could be a promising process.

Azo dyes are a major environmental concern due to the presence of benzene rings in their structure. The present experimental study investigates the capability of the Electro-Fenton process as an Electrochemical advanced Oxidation Process for degrading Acid Black 1 and Acid Blue 113 in an aquatic environment. In this study, a lab-scale EF batch reactor equipped with four electrodes and a DC power supply was used for removing the dye. The effects of such operating parameters as pH, voltage, H2O2, initial dye concentration, cathode materials, and operation time were evaluated. The results showed that initial pH of the solution, initial H2O2 concentration, as well as different applied voltages and reaction times were highly effective in the dye removal efficiency of the process so that the 98% of both dyes were removed after 10 min of reaction at pH=3.0, a voltage of 20 V, and a H2O2 concentration of 100 mg/L. Removal efficiency decreased dramatically when pH was increased from 3 to 11, and voltage from 20 to 40 V. The presence of H2O2 was found to be the prerequisite to this process since the maximum dye removal obtained at an H2O2 concentration of zero was 7% for both dyes. The results of this study indicate that the Electro-Fenton method can be considered as an alternative process for the traditional treatment processes used.

In this study, the applicability of the Electrocoagulation/Flotation (ECF) process in batch operation was investigated for the simultaneous removal of turbidity and Humic acid (HA) using Fe and Al electrodes. The effects of solution pH (3 - 12), electrical potentials (10 - 30 V), initial turbidity concentration (300 - 1200 NTU), and reaction time (10 - 30 minutes) with or without HA were investigated in an attempt to achieve higher turbidity removal efficiency. The batch experimental results revealed that with initial turbidity of 300 NTU, at voltage of 30 V, after 30 minutes reaction times, and at pH values of 6 and 8, the ECF process for Fe and Al electrodes removed over 97% and 88% of turbidity, respectively. The percentage of turbidity removal from solution dropped with a decrease in voltages for both electrodes. The results displayed that the Fe-Fe electrode arrangement attained the highest performance for turbidity removal rate. As a result, ECF process was shown to be a very efficient, cost-effective, and promising process for efficient treatment of high turbid water. Regarding HA, the results showed that in ECF process over 67% and 43% of UV254 has been removed for Al and Fe electrodes, respectively at the optimum pH, 30 minutes reaction time and 30 V applied voltage. Thus, it can be considered that Fe and Al are the best electrodes for removing turbidity and HA, respectively.

Background and In Electro/Fe2+/persulfate process, persulfate radicals are produced as powerful oxidizing agents which increase the efficiency of this process. The aim of this study was to investigate the efficiency removal of COD, TSS and dye from industrial effluent in Buali industrial area in Hamedan. In this study, the batch experiment was performed using a reactor equipped with four iron electrodes. We studied the effects of some operating parameters including pH (3-11), divalent iron ion dose (0.1 to 0.5 g/L), concentration of persulfate anion (0.5-2 g/L) and direct current electric rate (1-5 A) in removal of COD, TSS and dye from wastewater. The COD, TSS and dye measurement was done according to the standard methods. The results showed that under optimum conditions (pH: 3, Fe+2 dosage: 0.1 g/L and density: 5A) the removal efficiencies of process in COD, TSS and dye were 91.6, 73.5 and 93.1%, respectively. By making changes in the parameters, the efficiency of process also changed. The removal efficiency of single application of electrooxidation was 58.2%, 52.2% and 68% for COD, TSS and dye, respectively. The electro/Fe2+/persulfate process showed acceptable performance in removal of COD, TSS and dye. Therefore, this process could be used as a pretreatment unit to reduce the load of raw wastewater pollution before entering the conventional treatment units. Furthermore, the assessment of synergistic effects of persulfate revealed that single application of electrochemical degradation in optimum conditions had a much lower efficiency compared to electro/Fe+2/persulfate process.

Electrochemical methods as one of the advanced oxidation processes (AOPs), have been applied effectively to degrade recalcitrant organics in aqueous solutions. In the present work, the performance of electro-Fenton (EF) method using iron electrodes on the degradation of phenol was studied. In this study, a lab-scale EF batch reactor equipped with four electrodes and a DC power supply was used for removing phenol. The effect of operating parameters such as pH, voltage, H2O2 and initial phenol concentration and operating time were evaluated. We added H2O2 manually to the reactor while iron anode electrode was applied as a ferrous ion source. It was found that initial pH of the solution, initial H2O2 concentration, applied voltages were highly effective on the phenol removal efficiency in this process, so that 87% of phenol after 15 min of reaction at pH=3.0, voltage 26 V and H2O2 100 mg/L was removed. Phenol removal efficiency decreased with increasing pH, so that at pH 10, after 15 min, efficiency was 11%. To remove 99.99% phenol at pH 3, 100 mg/L concentration of H2O2 and voltage 26 V for 60 min was required. Electro-Fenton process using iron electrodes for phenol degradation and remediation of wastewater could be a promising process.

Background and Nitrate contamination in aqueous solution has become an increasingly serious environmental problem. Hence, in this study removal of nitrate in aqueous solution was reviewed using electrocoagulation (EC) and electro-fenton (EF) processes for Fe electrodes. In the present study, an EC and EF reactor in a lab scale to an approximate volume of 1 liter was proposed for removing of nitrate polluted water which was equipped with four Fe-Fe electrodes with dimensions 200 × 20 × 2 mm. The effects of operating parameters such as initial nitrate concentration, applied voltage (10-30 V), initial pH of the solution (3-12), different initial hydrogen peroxide (for EF process) and reaction times (5-30 minutes) were evaluated. The batch experimental results showed that initial nitrate concentration, initial pH of the solution, different applied voltages, initial H2O2 concentration and reaction times were highly effective on the nitrate removal efficiency in these processes. Based on the results, over 88% of nitrate in optimum condition (pH = 8, applied voltage = 30 V, initial nitrate concentration of 100 mg/l) have been removed in EC process. In addition, the application of EF process can remove 93% of nitrate at pH = 3, applied voltage = 30 V, initial nitrate concentration of 100 mg/l and 5 ml H2O2/l. Both EC and EF technologies can highly remove nitrate in aqueous solution. However, it was found that much better nitrate removal efficiency could be achieved by EF process than by EC process at the same condition.

Electrocoagulation (EC) and Electrocoagulation/flotation (ECF) processes are simple and efficient in water and wastewater treatment. In recent years, many investigations have focused on the use of these processes for treating of polluted water. The purpose of this study was to investigate the efficiency of EC and ECF processes in removal of high turbidity water using different electrodes in different circumstances. In present study an electrocoagulation and electrocoagulation/ flotation reactor in a lab scale to an approximate volume of 6 liters which is equipped with four Al-AL and Fe-Fe electrodes (200 * 20 * 2 mm) was used for removing of highturbidity water. The effects of operating parameters such as type of electrodes, initial water turbidity, applied voltage (10 to 30 v), initial pH of the solution (3 to 12) and reaction times (5 to 30 minutes) were evaluated. The batch experimental results showed that initial turbidity water, initial pH of the solution, different applied voltagesup to %88 turbidity as initial turbidity of 1200 NTU have been removed when using Al-Al and Fe-Fe electrodes and reaction times highly effective on the turbidity removal efficiency in these processes. In ECF process, 84%in optimum condition. However, in EC process the maximum removal was found up to 68% of initial turbidity when using Al-Al and Fe-Fe electrodes in same operation. Based on the result obtained in this study, the type of electrodes in EC and ECF processes significantly affect the removal rate of high turbid water. Also, it was found that much higher turbidity removal could be achieved by ECF process than that by EC process in the same condition.

cyanides as carbon-nitrogen radicals are very toxic compounds and highly harmful to humans and aquatic organisms. The efficacy of eggshells (ES) was investigated in this research work as an adsorbent for the elimination of cyanide from polluted streams. In this experimental study، the capability of ES to adsorb cyanide ions was conducted using a series of batch tests in a shaker-incubator instrument. For each batch run، 100 mL of solution containing a known initial concentration of cyanide and with the preferred level of pH was shacked. The effects of selected parameters such as pH (11-3)، reaction time (60–5 min) cyanide concentrations (150–50 mg/L) and the adsorbent dosage (2–0. 25 g/L) were investigated on the removal cyanide as a target contaminate. Chemical composition ES were analyzed using a Philips model XL- 30 scanning electron microscope (SEM) with energy-dispersive X-ray microanalysis (EDX). The specific surface and pore size distributions of ES were measured via Brunauer-Emmett-Teller (BET) isotherm and Barrett-Joyner-Halenda (BJH) methods using a Micrometrics particle size analyzer. The concentration of cyanide in solution before and after treatment was determined using the titrimetric method as described in the standard methods. Analysis of the ES component using the EDX technique showed that the main part of it consisted of calcium and its other components were magnesium، iron، aluminum and silicate. The experimental data showed that the maximum cyanide removal occurred at pH of 11، adsorbent dose (0. 5 g/L) and 40 min contact time. The kinetic evaluation indicated that the pseudo-second-order kinetic had the best fit to the experimental results predicting a chemisorptions process. The equilibrium adsorption of cyanide onto ES was well represented by the Langmuir equation. As a result، ES as waste materials was revealed as a very efficient and low-cost adsorbent and a promising option for removing cyanide from industrial wastewaters.