“…On the other hand, when the H 2 O 2 dosage was deficient (0.5 mM), the removal of NAP also showed a dramatic decrease due to the oxidizing agent ( • OH) concentration in the reaction not being enough. These results are in good agreement with the results obtained by Wang et al [41]. Figure 6c,d shows the combined effect between temperature and pH on the removal efficiency of NAP.…”
This work presents a study of the assessment of the operating parameters of the catalytic wet peroxide oxidation (CWPO) of naproxen (NAP) using magnetite/multi-walled carbon nanotubes (Fe3O4/MWCNTs) as a catalyst. The effect of pH, temperature, and H2O2 dosage on CWPO process was evaluated by using the response surface model (RSM), allowing us to obtain an optimum NAP removal of 82% at the following operating conditions: pH = 5, T = 70 °C, [H2O2]0 = 1.5 mM, and [NAP]0 = 10.0 mg/L. Therefore, NAP degradation kinetics were revealed to follow a pseudo-second-order kinetic model, and an activation energy value of 4.75 kJ/mol was determined. Adsorption and using only H2O2 experiments, both considered as blank tests, showed no significant removal of the pollutant. Moreover, Fe3O4/MWCNTs material exhibited good recyclability along three consecutive cycles, finding an average NAP removal percentage close to 80% in each cycle of 3 h reaction time. In addition, the scavenging tests confirmed that the degradation of NAP was mainly governed by •OH radicals attack. Two reaction sequences were proposed for the degradation mechanism according to the detected byproducts. Finally, the versatility of the catalyst was evidenced in the treatment of different environmentally relevant aqueous matrices (wastewater treatment plant effluent (WWTP), surface water (SW), and a hospital wastewater (HW)) spiked with NAP, obtaining total organic carbon (TOC) removal efficiencies after 8 h in the following order: NAP-SW > NAP-HW > NAP-WWTP.
“…On the other hand, when the H 2 O 2 dosage was deficient (0.5 mM), the removal of NAP also showed a dramatic decrease due to the oxidizing agent ( • OH) concentration in the reaction not being enough. These results are in good agreement with the results obtained by Wang et al [41]. Figure 6c,d shows the combined effect between temperature and pH on the removal efficiency of NAP.…”
This work presents a study of the assessment of the operating parameters of the catalytic wet peroxide oxidation (CWPO) of naproxen (NAP) using magnetite/multi-walled carbon nanotubes (Fe3O4/MWCNTs) as a catalyst. The effect of pH, temperature, and H2O2 dosage on CWPO process was evaluated by using the response surface model (RSM), allowing us to obtain an optimum NAP removal of 82% at the following operating conditions: pH = 5, T = 70 °C, [H2O2]0 = 1.5 mM, and [NAP]0 = 10.0 mg/L. Therefore, NAP degradation kinetics were revealed to follow a pseudo-second-order kinetic model, and an activation energy value of 4.75 kJ/mol was determined. Adsorption and using only H2O2 experiments, both considered as blank tests, showed no significant removal of the pollutant. Moreover, Fe3O4/MWCNTs material exhibited good recyclability along three consecutive cycles, finding an average NAP removal percentage close to 80% in each cycle of 3 h reaction time. In addition, the scavenging tests confirmed that the degradation of NAP was mainly governed by •OH radicals attack. Two reaction sequences were proposed for the degradation mechanism according to the detected byproducts. Finally, the versatility of the catalyst was evidenced in the treatment of different environmentally relevant aqueous matrices (wastewater treatment plant effluent (WWTP), surface water (SW), and a hospital wastewater (HW)) spiked with NAP, obtaining total organic carbon (TOC) removal efficiencies after 8 h in the following order: NAP-SW > NAP-HW > NAP-WWTP.
“…Figure 4 (a) displays that Acid treatment is a comparatively better option for the enhancement of catalytic activity or activation of catalyst (coal fly ash). Wang et al recommended that the 12 h of impregnation is necessary for the good catalyst [66]. Material like activated carbon can be used as a modifier.…”
Section: Wet Impregnation Methodsmentioning
confidence: 99%
“…It can be judged by taking modifier or activator. Wang et al demonstrated that acid modified catalyst is more efficient than alkali [66]. They investigated that during the acid wash, alkaline catalyst gets neutralized by acid and also observed the increased surface area and pore volume, i.e.…”
Section: Effect Of Phmentioning
confidence: 99%
“…Wang et al used three different temperatures to study the rigidity of metal coal fly ash. The optimized temperature was 723 K (Figure 13 (a)), as at this temperature pores have not been broken and along with that surface area was also increased with rigidity [66]. With the increase in calcinations temperature, evaporation occurs, gas produced and spread rapidly over the surface.…”
“…Therefore, neutral pH can be used to reduce effluent costs. Also, Wang et al [68] had used HNO3-modified coal fly ash (HFA) to perform an oxidation reaction in the treatment of p-Nitrophenol pollutants, in which it is proven to be effective, stable, and reusable up to 9 runs of application with retaining removal percentage of > 91% after 9 runs. Increasing the temperature of the system does increase the efficacy of the treatment, but it is also imperative that the cost of said higher temperature be taken into account.…”
The improper treatment of wastewater has cost humanity a large amount of access to clean water. Treating wastewater, by definition, means to remove pollutants, either physically or chemically. A chemical method of treating wastewater, the Fenton process, was deemed useful for the job. It includes a solution-based reaction that produces radicals to oxidize and break pollutants down. Variations of the Fenton process, each with their unique method, have been developed to increase the process’s efficacy and efficiency further. Admittedly, however, the information on this subject is relatively few, when compared to other more recent methods of treatment. This paper aims to present and discuss a wide variety of information on the Fenton process and its derivatives, including Electro-Fenton, Sono-Fenton, and Photo-Fenton among others.
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