Modelling studies by adsorption for the removal of sunset yellow azo dye present in effluent from a soft drink plant

This paper reports a study on the adsorption of the dye sunset yellow, present in an aqueous synthetic solution and a real effluent from a soft drink plant, onto granular-activated carbon derived from coconut husks, using a batch system. The kinetic equilibrium was investigated using two different dye concentrations (102 and 103 mg L−1) at 25°C and 150 rpm. The adsorption isotherms and thermodynamics parameters were evaluated at 25°C, 35°C, 45°C and 55°C, using the synthetic and real effluents (5–103 mg L−1). Experimental data showed that the adsorbent was effective in the removal of sunset yellow dye and the contact time required to attain the adsorption equilibrium did not exceed 10 h. The adsorption capacity was not influenced within a wide range of pH values (1–12), although at high dye concentrations it increased with increasing temperature for both the synthetic and real effluents. The Redlich–Peterson isotherm best represented the equilibrium data of the system. The negative values obtained for Δ G0 and Δ H0 suggest that this adsorption process is spontaneous, favourable, and exothermic. The positive values for Δ S0 indicate an increase in the entropy at the solid/liquid interface. Based on the results of this study, adsorption appears to be a promising method for the removal of sunset yellow azo dye from effluent generated at soft drink plants.