Abstract
Abstract
Fixed-bed columns filled with modified corn stalk (CS-AE) were developed to remove Cr(VI) from aqueous solution and electroplating wastewater. Effects of height–diameter ratio (H/D), flow rate, and Cr(VI) concentration on breakthrough curves were investigated, and different models were adopted to describe the dynamic adsorption performance. Experimental results showed that both breakthrough time and exhaustion time increased with the increase of bed H/D and with the decrease of flow rate and influent Cr(VI) concentration. Thomas model agreed well with experimental data under different conditions, and the rate constant
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