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The rate of adsorption and mass transfer kinetics exactly can be elucidated by pseudo second order model.
Adsorption kinetics was described by pseudo second order kinetic model while equilibrium study was represented by Langmuir isotherm with maximum adsorption capacity of 192.4 mg/g.
The process of removal was governed by pseudo second order rate equation and value of k2 was found to be 0.122 g mg−1 min−1 at 25 °C.
Therefore the adsorption kinetics is explained by pseudo second order mechanism.
For the evaluation of differences in sorption process, the kinetics of metal uptake were described by pseudo second order model (Ho and McKay 1999).
The adsorption kinetics of MG on CF nanoparticles is best explained by pseudo second order rate kinetics which is fitting with the results we got.
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Therefore, the SO4 2− removal was also represented by pseudo second-order kinetics according to Eq. 6.
The removal of both Cl− and SO4 2− by Mg−Al oxide (Mg/Al = 2) could be represented by pseudo second-order reactions.
Batch kinetic data have been well described by the pseudo second order model.
The dynamics of Cd2+ adsorption by bacterial cells were evaluated by applying pseudo first order and pseudo second order models.
The process kinetic was well fitted by pseudo first order kinetic model and electrical energy consumption of the process was obtained about 177.8 kWh/m3.
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