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The degradation kinetic was fitted to a first-order kinetics model.
The rate constants for each kinetic was evaluated and the rate constant for OR kinetics, kOR, was found to be significantly higher than the rate constant for OA kinetics, kOA, under the reported conditions for the four different solvents used.
The pseudo-first-order abatement kinetic was relatively fitted.
For further exploring the adsorption mechanisms, adsorption kinetic was evaluated at 298 K and pH 1.08.
Adsorption kinetic was fitted well by the pseudo-second-order kinetic model.
The kinetic studies proved that the first-order kinetic was the best applicable model.
Likely because of this fact the adsorption kinetic was limited by liquid film mass transfer diffusion.
The adsorption kinetic was investigated using the pseudo-first-order and pseudo-second-order models.
The process kinetic was also evaluated by isotherm, pseudo-second-order and intra-particle diffusion models.
The regression results showed that the adsorption kinetic was more accurately represented by pseudo-second-order.
In both processes, adsorption kinetic was well described by a chemical adsorption onto a heterogeneous surface.
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