Journal
DESALINATION AND WATER TREATMENT
Volume 57, Issue 30, Pages 14188-14212Publisher
DESALINATION PUBL
DOI: 10.1080/19443994.2015.1061455
Keywords
Activated carbon; Adsorbent; Isotherm models; Equilibrium; Kinetics
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Adsorption of phenol from its aqueous solutions using activated carbon, prepared from tomato stem, in a batch process was investigated. The preparation of charred tomato stem (CTS) activated carbon involved carbonization of the precursor previously impregnated with ortho-phosphoric acid activating agent (activating agent volume (ml) by precursor weight (g) ratio set at 1:1) at 470 degrees C for 2h. Equilibrium and kinetic studies were carried out using phenol solutions of various concentrations (20-100mg/L). The adsorbent was characterized via electron probe microanalysis (EPMA) associated with energy dispersive spectrometry (EDS), Fourier transform Infrared analysis, pore volume and BET surface area determinations. Parametric study of the adsorption process was also conducted. The equilibrium adsorption data were elucidated using Langmuir, Freundlich, Dubinin-Radushkevich and Temkin isotherm models. Equilibrium data fitted satisfactorily to the Langmuir model; the maximum adsorption capacity was 41.6667mg/g at 308K. Pseudo-first-order and pseudo-second-order models suitably validated the adsorption kinetics while the intraparticle diffusion model and Boyd kinetic model examined the diffusion mechanism involved therein. Desorption studies were conducted using water, absolute ethanol (100% v/v) and 0.1 (N) NaOH solution as desorbing agents. Thermogravimetric analysis examined the thermal stability and regeneration potential of the CTS activated carbon.
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