Phenol removal from aqueous solution by adsorption and ion exchange mechanisms onto polymeric resins

• Published in: Journal of colloid and interface science 2009-10, Vol.338 (2), p.402-409
• Main Authors: Caetano, Michelle, Valderrama, César, Farran, Adriana, Cortina, José Luis
• Format: Article
• Language: English
• Subjects: Adsorption; Anion exchanging; Chemistry; Colloidal state and disperse state; Desorption; Diffusion coefficients; Exact sciences and technology; General and physical chemistry; Hydrogen-Ion Concentration; Industrial aqueous effluents; Ion exchange; Ion exchange resins; Ion Exchange Resins - chemistry; Kinetic; Mathematical models; Phenol; Phenol - chemistry; Phenol - isolation & purification; Phenol removal; Polymers; Polymers - chemistry; Resins; Solutions; Surface physical chemistry; Surface Properties; Water - chemistry
• ISSN: 0021-9797; 1095-7103
• DOI: 10.1016/j.jcis.2009.06.062

This figure represents experimental phenol removal by AuRIX 100 and Dowex XZ resins at pH 3 and 11, as well as the calculations done with the theoretical combined model (adsorption and ion exchange mechanisms). The removal of phenol from aqueous solution was evaluated by using a nonfunctionalized hyper-cross-linked polymer Macronet MN200 and two ion exchange resins, Dowex XZ (strong anion exchange resin) and AuRIX 100 (weak anion exchange). Equilibrium experimental data were fitted to the Langmuir and Freundlich isotherms at different pHs. The Langmuir model describes successfully the phenol removal onto the three resins. The extent of the phenol adsorption was affected by the pH of the solution; thus, the nonfunctionalized resin reported the maximum loading adsorption under acidic conditions, where the molecular phenol form predominates. In contrast both ion exchange resins reported the maximum removal under alkaline conditions where the phenolate may be removed by a combined effect of both adsorption and ion exchange mechanisms. A theoretical model proposed in the literature was used to fit the experimental data and a double contribution was observed from the parameters obtained by the model. Kinetic experiments under different initial phenol concentrations and under the best pH conditions observed in the equilibrium experiments were performed. Two different models were used to define the controlling mechanism of the overall adsorption process: the homogeneous particle diffusion model and the shell progressive model fit the kinetic experimental data and determined the resin phase mechanism as the rate-limiting diffusion for the phenol removal. Resins charged after the kinetic experiments were further eluted by different methods. Desorption of nonfunctionalized resin was achieved by using the solution (50% v/v) of methanol/water with a recovery close to 90%. In the case of the ion exchange resins the desorption process was performed at different pHs and considering the effect of the competitive ion Cl −. The desorption processes were controlled by the ion exchange mechanism for Dowex XZ and AuRIX 100 resins; thus, no significant effect for the addition of Cl − under acidic conditions was observed, while under alkaline conditions the total recovery increased, specially for Dowex XZ resin.