Journal
PROCESSES
Volume 11, Issue 7, Pages -Publisher
MDPI
DOI: 10.3390/pr11072045
Keywords
activated carbons; adsorption; kinetic modelling; p-Nitrophenol
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This study investigated the solvent adsorption of p-Nitrophenol (PNP) onto activated carbons for wastewater treatment. It analyzed the influence of adsorbate concentration and adsorbent size on equilibrium isotherms and removal rates, and developed efficient adsorption processes. The study examined adsorption isotherms using different models and kinetics using various kinetic models, providing insights into the adsorption mechanism and aiding the design of wastewater treatment processes. The study also observed slight differences in maximum adsorption capacity with particle size and highlighted the significance of inlet velocity and carbon mass in dynamic adsorption systems.
The study focused on investigating the solvent adsorption of p-Nitrophenol (PNP) onto activated carbons for wastewater treatment. It explored the influence of adsorbate concentration and adsorbent size on equilibrium isotherms and removal rates to develop efficient adsorption processes. The study examined adsorption isotherms under equilibrium conditions utilizing both the Langmuir and Double-Langmuir models and the Dubinin-Radushkevich equation. Remarkably, all the models demonstrated equally excellent fitting to the experimental data. Kinetics of PNP adsorption were investigated using pseudo-first-order, pseudo-second-order, and intraparticle diffusion kinetic models. This provided insights into the dominant adsorption mechanism and mass transfer phenomena, aiding the design of efficient wastewater treatment processes. Strong correlations (correlation coefficients > 0.9) were found between the models and experimental data for three types of activated carbons under batch conditions. This validation enhances the reliability and applicability of the models, supporting their practical use. The study also observed a slight increase in maximum adsorption capacity (q(max)) with decreasing particle size, although there is not a significant difference: 340, 350, and 365 mg & BULL;g(-1), for CB-L, CB-M, and CB-S, respectively. This insight helps in selecting appropriate activated carbon for effective PNP removal, considering both adsorption capacity and particle size. Furthermore, the analysis of PNP adsorption under dynamic conditions in fixed-bed columns highlighted the significance of inlet velocity and carbon mass in determining breakthrough time, with particle size playing a secondary role. This information aids in optimizing the design and operation of fixed-bed adsorption systems for efficient PNP removal. In summary, this study's significant contributions lie in enhancing our understanding of PNP adsorption in wastewater treatment. By investigating equilibrium isotherms, kinetics, and mass transfer phenomena, it provides validated models, insights into adsorption capacity and particle size, and practical guidance for dynamic adsorption systems. These findings contribute to the development of efficient and sustainable wastewater treatment methods.
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