Adsorption of acid orange 7 dye in aqueous solutions by spent brewery grains

Spent brewery grains (SBG), a by-product of the brewing process, were tested as an adsorbent of acid orange 7 dye (AO7), a monoazo acid dye currently used in paper and textile industries. The presence of AO7 in these effluents causes obvious environmental problems. Kinetics studies of adsorption of AO7 to SBG (3.75%, m/v) were carried out at 20degreesC, using aqueous solutions with different AO7 concentrations (30-834 mg/L). For every situations tested, no significant variation in residual AO7 concentration in solution was detected after 1 h contact between the dye and the adsorbent. The adsorption process followed a pseudo-first order model. The equilibrium process showed to be well described by both Freundlich and Langmuir isotherm models, at 20 and 30degreesC. The maximum adsorption capacity was estimated to be 30.5 mg AO7/g SBG, at 30degreesC. Free energy of adsorption (DeltaGdegrees), enthalpy (DeltaHdegrees), and entropy (DeltaSdegrees) changes were calculated to predict the nature of adsorption. The estimated values for DeltaGdegrees were -22.78 and -24.53 kJ/mol, respectively, at 293.3 K (20degreesC) and 303.3 K (30degreesC), which are rather low indicating that a spontaneous process occurred. The enthalpy changes and entropy of adsorption were 28.66 and 175.36 J/mol K, respectively. The positive value for DeltaHdegrees indicates that the adsorption of AO7 dye to SBG is an endothermic process. The positive value of entropy reflects the affinity of the adsorbent for AO7 dye. The obtained results are very promising since: (i) high levels of colour removal (>90%) were achieved with low contact times adsorbent/dye (less than 1 h contact); and (ii) the whole SBG can be successfully used as adsorbent of AO7 dye in aqueous solution without needing any previous treatments such as milling and/or sieving. Spent grains, being a cheap, and easily available material, can be an alternative for more costly adsorbents used for dye removal in wastewater treatment processes. (C) 2004 Elsevier B.V. All rights reserved.