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The equilibrium adsorption followed Langmuir model and adsorption reaction was found to be pseudo-second order confirming chemisorption.
The adsorption kinetics follows the pseudo-second order model and adsorption isotherm follows the Langmuir model with maximum adsorption capacity of 145.98 and 47.892 mg g−1 for MG and Pb2+ ions, respectively.
The adsorption capacity of GO@Fe3O4@IL/PBA-SMIP to HRP was researched to be 8.8 g/g, and the adsorption model and adsorption kinetics of GO@Fe3O4@IL/PBA-SMIP to HRP followed Langmuir adsorption isotherm and pseudo second-order model while the washing process was superior with acetic acid than NaOH solutions.
Besides, its recycling performance was evaluated by mechanical extrusion, ethanol washing and calcined regeneration, and for emulsified oil, the adsorption process follows a pseudo-second-order kinetic model and adsorption isotherms are related well by the Freundlich model with a determination coefficient.
The NC isotherms well fitted the Langmuir model, and adsorption proceeded by physisorption.
The kinetic study also confirmed the compatibility between the pseudo-second-order model and adsorption.
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Except for the normal fitting of adsorption process with the Langmuir isotherm adsorption model, Freundlich isotherm adsorption model and secondary adsorption kinetics model, the solid liquid phase adsorption mechanism was also introduced to explain the Cu2+ adsorption process.
The adsorption isotherm data fitted better to the Langmuir adsorption model, and the adsorption kinetics was better described by the pseudo-second order equation.
Both adsorption reaction models and adsorption diffusion models are now widely employed for fitting kinetic data (Qiu et al. 2009).
In addition, kinetic models and adsorption isotherms of the process were determined and analyzed.
In the past decades, several mathematical models have been proposed to describe adsorption data, which can usually be categorized as adsorption reaction models and adsorption diffusion models.
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