Abstract

This work focused on the removal of As(V) using chitosan-coated bentonite (CCB) from groundwater in a fixed-bed system. Thomas and Yoon–Nelson models were applied to the experimental data in order to predict breakthrough curves and assess model parameters. Response surface methodology based on Box–Behnken design was utilized to optimize parameters such as adsorbent mass (6.0–8.0 g), flow rate (0.6–1.0 mL/min), and initial concentration (100–500 μg/g) and to evaluate the interactive effects of the variables on the As(V) adsorption capacity at breakthrough point. Results showed that the optimum As(V) uptake capacity at breakthrough point of 10.57 μg/g could be attained at initial concentration of 418.12 μg/g, CCB mass of 6.6 g, and flow rate of 0.65 mL/min. Based on the analysis of variance, the high value of coefficient of determination (R2 ≥ 0.9712) indicates that the quadratic model best describes the experimental data, and the initial concentration is a significant factor on the As(V) adsorption capacity at breakthrough point.

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