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Adsorption of 2,4,6-Trichlorophenol From Aqueous Solutions by a Surfactant-Modified Zeolitic Tuff: Batch and Continuous Studies Publisher



Naddafi K1 ; Rastkari N1, 2 ; Nabizadeh R1 ; Saeedi R3 ; Gholami M1, 4 ; Sarkhosh M1
Authors
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Authors Affiliations
  1. 1. Department of Environmental Health Engineering, School of Public Health, Tehran University of Medical Sciences, Tehran, Iran
  2. 2. Center for Air Pollution Research (CAPR), Institute for Environmental Research (IER), Tehran University of Medical Sciences, Tehran, Iran
  3. 3. Department of Public Health, Shahid Beheshti University of Medical Sciences, Tehran, Iran
  4. 4. Department of Environmental Health Engineering, Abarkouh Paramedical College, Shahid Sadoughi University of Medical Sciences, Yazd, Iran

Source: Desalination and Water Treatment Published:2016


Abstract

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 30 min for all TCP concentrations. The pseudo-second-order rate equation best described the kinetic of TCP adsorption onto the SMZ (R2 > 0.99). Isotherm experiments were conducted in an initial TCP concentration range of 25–200 mg/L, and the isotherm data were found to be in the best fitness with the Langmuir model (R2 > 0.99). According to the Langmuir model, the maximum adsorption capacity (qm) of TCP was obtained to be 12.9 mg/g. In the packed bed column, by increasing the influent TCP concentration from 100 to 200 mg/L, the adsorption capacity at complete exhaustion point drastically increased from 14.7 to 35.5 mg/L. The breakthrough curves were predicted with the suitable fitness by both the Thomas and Yoon–Nelson models (R2 > 0.93). © 2015 Balaban Desalination Publications. All rights reserved.
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