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Removal of 2,4,6-Trichlorophenol From Aqueous Solutions by Cetylpyridinium Bromide (Cpb)-Modified Zeolite in Batch and Continuous Systems Publisher



Naddafi K1, 2 ; Rastkari N2 ; Nabizadeh R1, 2 ; Saeedi R3 ; Gholami M1, 4
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 Health Sciences, School of Health, Safety and Environment, Shahid Beheshti University of Medical Sciences, Tehran, Iran
  4. 4. Environmental Science and Technology Research Center, Department of Environmental Health Engineering, Shahid Sadoughi University of Medical Sciences, Yazd, Iran

Source: Desalination and Water Treatment Published:2017


Abstract

In this study, 2,4,6-trichlorophenol (TCP) was removed from aqueous solutions by clinoptilolite-rich tuff modified with cetylpyridinium bromide (CPB). CPB modification significantly increased the TCP adsorption capacity, so that the highest adsorption capacities of the natural zeolite and cetylpyridinium bromide-modified zeolite (CPB-MZ) at the same experimental conditions were determined to be 1.6 and 8.5 mg/g, respectively. Kinetic and isotherm of TCP adsorption were studied in a batch system in which kinetic experiments revealed that the TCP adsorption by the CPB-MZ reached to equilibrium in 45 min for all TCP concentrations. The kinetic of TCP adsorption onto the CPB-MZ was best described by the pseudo-second-order equation (R2 > 0.99) while the isotherm data were best fitted with the Langmuir model (R2 > 0.99). The continuous adsorption experiments were performed in a packed bed column. The maximum adsorption capacity (qm) of TCP was 16.34 mg/g according to the Langmuir model. In this system, by increasing the influent TCP concentration from 100 to 200 mg/L, the adsorption capacity increased from 19.35 to 40.78 mg/g at complete exhaustion point. © 2017 Desalination Publications. All rights reserved.