“…The catalytic activity was tested through several series of experiments (operated in triplicate) in 200 mL of Rhodamine B solution at a given concentration under magnetic stirring (300 rpm) with the required doses of catalyst and H 2 O 2 (30 wt%) in Erlenmeyer flasks. At the selected time, 1 mL was collected from the reaction solution and diluted in 4 mL of distilled water, and then, 0.3 mL of Na 2 SO 3 (0.1 mol/L) was added to deactivate the hydroxyl radicals (Li et al 2014). The solution was thus centrifuged with a centrifuge at 3000 rpm to recover the supernatant without fines particles and analyzed by UV-visible spectrophotometry (Cary scan 50) at 554 nm to determine the Rhodamine…”
Iron-based nanoparticles were formed in the pores of a micro-and mesoporous activated carbon made from banana spike by the impregnation of iron sulfate at various ratios and further pyrolysis, in order to prepare three catalysts AC@Fe/1, AC@ Fe/2, AC@Fe/3 having iron mass contents of 1.6%, 2.2% and 3.3%, respectively. The pore size distributions, transmission electron microscope observations and X-ray photoelectron spectroscopy analyses have revealed that iron-based nanoparticles of 1-50 nm diameter, containing O and P, are located mainly in the supermicropores and mesopores of the activated carbon. Catalysts have been used to remove Rhodamine B in an aqueous solution by the heterogeneous Fenton process. AC@Fe/3 catalyst has allowed achieving 93% of solution discoloration compared to 87.4% for AC@Fe/2 and 78.5% for AC@Fe/1 after 180 min in batch reaction. The catalytic efficiency of AC@Fe/3 is attributed to the highest dispersion of the iron-based nanoparticles in the activated carbon porosity. The effects of hydrogen peroxide and initial dye concentration, pH, catalyst amount and temperature on the Rhodamine B removal kinetics catalyzed by AC@Fe/3 were studied. This catalyst showed remarkable performances of the Rhodamine B mineralization and possibility of recycling.
“…The catalytic activity was tested through several series of experiments (operated in triplicate) in 200 mL of Rhodamine B solution at a given concentration under magnetic stirring (300 rpm) with the required doses of catalyst and H 2 O 2 (30 wt%) in Erlenmeyer flasks. At the selected time, 1 mL was collected from the reaction solution and diluted in 4 mL of distilled water, and then, 0.3 mL of Na 2 SO 3 (0.1 mol/L) was added to deactivate the hydroxyl radicals (Li et al 2014). The solution was thus centrifuged with a centrifuge at 3000 rpm to recover the supernatant without fines particles and analyzed by UV-visible spectrophotometry (Cary scan 50) at 554 nm to determine the Rhodamine…”
Iron-based nanoparticles were formed in the pores of a micro-and mesoporous activated carbon made from banana spike by the impregnation of iron sulfate at various ratios and further pyrolysis, in order to prepare three catalysts AC@Fe/1, AC@ Fe/2, AC@Fe/3 having iron mass contents of 1.6%, 2.2% and 3.3%, respectively. The pore size distributions, transmission electron microscope observations and X-ray photoelectron spectroscopy analyses have revealed that iron-based nanoparticles of 1-50 nm diameter, containing O and P, are located mainly in the supermicropores and mesopores of the activated carbon. Catalysts have been used to remove Rhodamine B in an aqueous solution by the heterogeneous Fenton process. AC@Fe/3 catalyst has allowed achieving 93% of solution discoloration compared to 87.4% for AC@Fe/2 and 78.5% for AC@Fe/1 after 180 min in batch reaction. The catalytic efficiency of AC@Fe/3 is attributed to the highest dispersion of the iron-based nanoparticles in the activated carbon porosity. The effects of hydrogen peroxide and initial dye concentration, pH, catalyst amount and temperature on the Rhodamine B removal kinetics catalyzed by AC@Fe/3 were studied. This catalyst showed remarkable performances of the Rhodamine B mineralization and possibility of recycling.
“…† Samples were taken at set time intervals: some sample was promptly quantied for H 2 O 2 concentration; Na 2 SO 3 was introduced to the remainder to impede the ongoing redox reaction before TOC (Total Organic Carbon) measurement. 27 In probing the oxygen radicals included in the heterogeneous MW-CWPO catalyzed by supported Cu/Ni bimetallic oxides, NB and carbon CT were utilized as scavengers for cOH and O2c À , respectively, assessing the variation of the removal rate of 100 mg L À1 quinoline with 22.75 mmol L À1 H 2 O 2 , 4 g L À1 Cu/Nicatalyst, temperature of 333 K, and initial pH of 7.0 under MW (500 W) irradiation to identify relevant radicals.…”
This article presents a study about the initial pH and H2O2dosage influence on TOC abatement by MW-CWPO with Cu/Ni-catalyst and reactive oxygen identification based on quinoline mineralization inhibition using the specific radical scavengers.
“…And most iron oxides are semiconductors, capable of exhibiting photocatalytic activity under solar irradiation [2][3]. γ-FeOOH seems to be a suitable representative among the iron oxides, because it has higher activity as a metastable phase [4].…”
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