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1.
Environ Technol ; 41(9): 1139-1150, 2020 Apr.
Article in English | MEDLINE | ID: mdl-30198817

ABSTRACT

This study evaluated the removal of silver nanoparticles (AgNPs), coated with different stabilizers, from aqueous media using the electrocoagulation technique. The AgNPs dispersions were synthesized by chemical reduction with silver nitrate as precursor, sodium borohydride as reducing agent and sodium carboxymethylcellulose (CMC), polyvinyl alcohol (PVA) and polyvinylpyrrolidone (PVP) as stabilizers with initial concentrations of 1 and 3% (w/v). The dispersions were named AgNPs-CMC1, AgNPs-CMC3, AgNPs-PVA1, AgNPs-PVA3, AgNPs-PVP1, and AgNPs-PVP3. Electrocoagulation treatments of AgNPs-PVA1, AgNPs-PVP1 and AgNPs-PVP3 dispersions resulted in total silver removals above 99.90% in 10 min. For the AgNPs-PVP3 dispersion 99.98% of removal was obtained in 20 min. After 15 min of electrolysis, The AgNPs-CMC1 and AgNPs-CMC3 dispersions showed a reduction in total silver concentration of 71.72 and 52.15%, respectively. Therefore, these results showed that the removal of AgNPs from the aqueous medium by electrocoagulation is possible, but their efficiency and viability depends on the nature, the molecular structure and the concentration of stabilizers. Furthermore, the toxicity analysis using the Vibrio fischeri bacteria demonstrated that only the dispersions stabilized with PVP became suitable for disposal after the electrocoagulation treatment.


Subject(s)
Metal Nanoparticles , Electrocoagulation , Polyvinyl Alcohol , Povidone , Silver
2.
Water Sci Technol ; 78(11): 2328-2337, 2018 Dec.
Article in English | MEDLINE | ID: mdl-30699084

ABSTRACT

This study evaluated the prednisone removal from aqueous solutions using adsorption by an activated carbon of vegetal origin (VAC). A central composite rotatable design (CCRD) and the response surface methodology (RSM) were used to verify the influence of the parameters: pH, adsorbent dose and prednisone concentration in a batch adsorption process. Among the analyzed parameters, only the adsorbent dose and the prednisone concentration were statistically significant (α = 0.05) and the critical values obtained were adsorbent dose: 1.87 g/L, pH 7.56 and prednisone concentration: 3.66 mg/L with 77.51% of prednisone removal by VAC. The kinetic study of the adsorption of prednisone reached the equilibrium in 4 h. The pseudo-first-order model described adequately the kinetics data behavior. The equilibrium experimental data obtained at different temperatures showed that the VAC has a maximum adsorption capacity of 18.04 mg/g at a temperature of 30 °C. The prednisone removal decreased by the increasing temperature and the Langmuir isotherm well described the experimental data (R² > 0.98). Thermodynamic results shown that the prednisone removal of aqueous solutions by VAC is spontaneous and favorable process.


Subject(s)
Charcoal , Prednisone/chemistry , Water Pollutants, Chemical/chemistry , Water Purification/methods , Adsorption , Hydrogen-Ion Concentration , Kinetics , Prednisone/analysis , Solutions , Temperature , Thermodynamics , Water Pollutants, Chemical/analysis
3.
Environ Technol ; 36(1-4): 496-506, 2015.
Article in English | MEDLINE | ID: mdl-25182075

ABSTRACT

In this work, the application of an iron electrode-based electrocoagulation (EC) process on the treatment of a real textile wastewater (RTW) was investigated. In order to perform an efficient integration of the EC process with a biological oxidation one, an enhancement in the biodegradability and low toxicity of final compounds was sought. Optimal values of EC reactor operation parameters (pH, current density and electrolysis time) were achieved by applying a full factorial 3(3) experimental design. Biodegradability and toxicity assays were performed on treated RTW samples obtained at the optimal values of: pH of the solution (7.0), current density (142.9 A m(-2)) and different electrolysis times. As response variables for the biodegradability and toxicity assessment, the Zahn-Wellens test (Dt), the ratio values of dissolved organic carbon (DOC) relative to low-molecular-weight carboxylates anions (LMCA) and lethal concentration 50 (LC50) were used. According to the Dt, the DOC/LMCA ratio and LC50, an electrolysis time of 15 min along with the optimal values of pH and current density were suggested as suitable for a next stage of treatment based on a biological oxidation process.


Subject(s)
Electrolysis/methods , Lactuca/drug effects , Wastewater/chemistry , Water Pollutants, Chemical/isolation & purification , Water Pollutants, Chemical/toxicity , Water Purification/methods , Biodegradation, Environmental , Industrial Waste/prevention & control , Textile Industry , Water Pollutants, Chemical/radiation effects
4.
Appl Radiat Isot ; 68(12): 2208-13, 2010 Dec.
Article in English | MEDLINE | ID: mdl-20561795

ABSTRACT

In this work granular activated carbon has been chosen as an absorbent in order to investigate the Cr(VI) reduced by adsorption experiments. Several batch chromium-sorption experiments were carried out using 0.25 g of granular activated carbon in 50 mL aqueous solution containing approximately 70 and 140 mg L(-1) of Cr(VI) and Cr(III), respectively. Cr-Kbeta fluorescence spectra of Cr adsorbed in a carbon matrix and Cr reference materials were measured using a high-resolution Johann-type spectrometer. Based on evidence from the Cr-Kb satellite lines, the Cr(VI) reduction process has actually happened during metal adsorption by the activated carbon.

5.
Water Sci Technol ; 60(8): 2173-85, 2009.
Article in English | MEDLINE | ID: mdl-19844065

ABSTRACT

An electro-coagulation laboratory scale system using aluminium plates electrodes was studied for the removal of organic and inorganic pollutants as a by-product from leather finishing industrial process. A fractional factorial 2(3) experimental design was applied in order to obtain optimal values of the system state variables. The electro-coagulation (EC) process efficiency was based on the chemical oxygen demand (COD), turbidity, total suspended solid, total fixed solid, total volatile solid, and chemical element concentration values. Analysis of variance (ANOVA) for final pH, total fixed solid (TFS), turbidity and Ca concentration have confirmed the predicted models by the experimental design within a 95% confidence level. The reactor working conditions close to real effluent pH (7.6) and electrolysis time in the range 30-45 min were enough to achieve the cost effective reduction factors of organic and inorganic pollutants' concentrations. An appreciable improvement in COD removal efficiency was obtained for electro-coagulation treatment. Finally, the technical-economical analysis results have clearly shown that the electro-coagulation method is very promising for industrial application.


Subject(s)
Aluminum/chemistry , Electrochemical Techniques/methods , Tanning , Waste Disposal, Fluid/methods , Water Purification/methods , Analysis of Variance , Calcium/analysis , Costs and Cost Analysis , Electricity , Electrochemical Techniques/economics , Electrodes , Electrolysis , Hydrogen-Ion Concentration , Iron/chemistry , Kinetics , Nephelometry and Turbidimetry , Time Factors , Volatile Organic Compounds/analysis , Waste Disposal, Fluid/economics , Water Pollutants, Chemical/isolation & purification , Water Purification/economics
6.
J Hazard Mater ; 172(1): 330-7, 2009 Dec 15.
Article in English | MEDLINE | ID: mdl-19640647

ABSTRACT

In this study the pollutant removal from a textile dyeing wastewater has been investigated by using the electro-coagulation technique with iron electrodes. In order to obtain optimal values of the system state variables, a 3(3) full factorial experimental design was applied. The electro-coagulation (EC) process response was evaluated on the basis of COD removal and decolourization values. The electrolysis time and density current were statistically significant for the COD removal and decolourization. Based on the lettuce seeds (Lactuca sativa) and brine shrimp (Artemia salina), the lowest toxicity level was achieved in 5 min of electrolysis time. Due to the remaining high toxicity level above 30 min of electrolysis time, the EC process is not adequate to be used in a single effluent treatment, suggesting that this electrochemical process of up to 5 min could be used as part of a complete effluent treatment system.


Subject(s)
Biological Assay/methods , Coloring Agents/chemistry , Coloring Agents/isolation & purification , Electrocoagulation/methods , Water Pollutants, Chemical/isolation & purification , Water Purification/methods , Animals , Artemia , Biodegradation, Environmental , Electrochemistry/methods , Electrolysis/methods , Industrial Waste , Textiles , Time Factors , Waste Disposal, Fluid/methods , Water Pollutants, Chemical/chemistry
7.
Water Res ; 43(17): 4159-66, 2009 Sep.
Article in English | MEDLINE | ID: mdl-19595427

ABSTRACT

Aquatic macrophytes Salvinia auriculata, Pistia stratiotes and Eichhornia crassipes were chosen to investigate the Cr(VI) reduced by root-based biosorption in a chromium uptake experiment, using a high-resolution XRF technique. These plants were grown in hydroponics medium supplied with non-toxic Cr concentrations during a 27-day metal uptake experiment. The high-resolution Cr-Kbeta fluorescence spectra for dried root tissues and Cr reference material (100% Cr, Cr(2)O(3), and CrO(3)) were measured using an XRF spectrometer. For all species of aquatic plant treated with Cr(VI), the energy of the Cr-Kbeta(2,5) line was shifted around 8 eV below the same spectral line identified for the Cr(VI) reference, but it was also near to the line identified for the Cr(III) reference. Moreover, there was a lack of the strong Cr-Kbeta'' line assigned to the Cr(VI) reference material within the Cr(VI)-treated plant spectra, suggesting the reduction of Cr(VI) for other less toxic oxidation states of Cr. As all Cr-Kbeta spectra of root tissue species were compared, the peak energies and lineshape patterns of the Cr-Kbeta(2,5) line are coincident for the same aquatic plant species, when they were treated with Cr(III) and Cr(VI). Based on the experimental evidence, the Cr(VI) reduction process has happened during metal biosorption by these plants.


Subject(s)
Chromium/pharmacokinetics , Plant Roots/metabolism , Spectrometry, Fluorescence/methods , Water Pollutants, Chemical/pharmacokinetics , Hydrogen-Ion Concentration , Oxidation-Reduction , X-Rays
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