Abstract
Adsorption of tartrazine yellow food dye, in a fixed-bed column, was carried out using a single system, a binary system (in the presence of sunset yellow food dye), and in a real effluent provides from an ice cream industry. Chitosan was used to coat sand particles by the dip-coating technique, and these particles were applied in fixed-bed adsorption. The assays were performed in flow rates of 3mLmin-1 and 5mLmin-1. The best performance was reached at 3mLmin-1. In this flow rate, for single and binary systems, the breakthrough time was 95min and 65min, and the maximum capacity of the column was around 595mgg-1 and 497mgg-1, respectively. In the assay conducted with the real effluent, the breakthrough time was 10min, and the maximum adsorption capacity of the column was reduced to 191mgg-1 for tartrazine dye. The dynamic models of Thomas and Yoon-Nelson were used, and both were suitable to represent the breakthrough curves.
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