4.3 Article

Adsorption of 2,4,6-trichlorophenol from aqueous solutions by a surfactant-modified zeolitic tuff: batch and continuous studies

Journal

DESALINATION AND WATER TREATMENT
Volume 57, Issue 13, Pages 5789-5799

Publisher

TAYLOR & FRANCIS INC
DOI: 10.1080/19443994.2015.1005693

Keywords

Adsorption; 2; 4; 6-trichlorophenol; Clinoptilolite; Batch system; Packed bed column

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In the present study, a clinoptilolite-rich tuff was modified with hexadecyl trimethyl ammonium chloride and was used for the removal of 2,4,6-trichlorophenol (TCP) from aqueous solutions. Kinetic and isotherm of TCP adsorption were studied in a batch system, and the continuous adsorption experiments were performed as a function of initial TCP concentration in a packed bed column. Kinetic experiments indicated that the TCP adsorption by the surfactant-modified zeolite (SMZ) was rapid and reached to equilibrium in 30min for all TCP concentrations. The pseudo-second-order rate equation best described the kinetic of TCP adsorption onto the SMZ (R-2>0.99). Isotherm experiments were conducted in an initial TCP concentration range of 25-200mg/L, and the isotherm data were found to be in the best fitness with the Langmuir model (R-2>0.99). According to the Langmuir model, the maximum adsorption capacity (q(m)) of TCP was obtained to be 12.9mg/g. In the packed bed column, by increasing the influent TCP concentration from 100 to 200mg/L, the adsorption capacity at complete exhaustion point drastically increased from 14.7 to 35.5mg/L. The breakthrough curves were predicted with the suitable fitness by both the Thomas and Yoon-Nelson models (R-2>0.93).

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