Adsorption of 2, 4, 6-trichlorophenol from aqueous solutions by a surfactant-modified zeolitic tuff: batch and continuous studies. Issue 13 (15th March 2016)

• Record Type: Journal Article
• Authors: Naddafi, Kazem; Rastkari, Noushin; Nabizadeh, Ramin; Saeedi, Reza; Gholami, Maryam; Sarkhosh, Maryam
• Is Part Of: Desalination and water treatment. Volume 57:Issue 13(2016)
• Page Start: 5789
• Page End: 5799
• Publication Date: 2016-03-15
• Subjects: Adsorption -- 2, 4, 6-trichlorophenol -- Clinoptilolite -- Batch system -- Packed bed column; Saline water conversion -- Periodicals; Saline water conversion; Water -- Purification; Periodicals; 628.167
• DOI: 10.1080/19443994.2015.1005693
• Languages: English
• ISSNs: 1944-3994

Abstract

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 ( R 2 > 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 ( R 2 > 0.99). According to the Langmuir model, the maximum adsorption capacity ( q m ) 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 ( R 2 > 0.93).