Modeling of Adsorption Isotherms and Kinetics of Remazol Red RB Adsorption from Aqueous Solutions onto Modified Clay
Erişim
info:eu-repo/semantics/openAccessTarih
2012Erişim
info:eu-repo/semantics/openAccessÜst veri
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Karaca, S., Gürses, A., Açışlı, Ö., Hassanı, A., Kıranşan, M., Yıkılmaz, K. (2012) “ Modeling of Adsorption Isotherms and Kinetics of Remazol Red RB Adsorption from Aqueous Solutions onto Modified Clay”. (26 th National Chemistry Congress-(1-6 Ekim 2012) MUĞLA/TURKEY)Özet
There is an inaease in environmental pollution as a result of rapid industrialization. The biological effects of
dyes after biotransformation have been shown to be toxic, and in some cases these compounds are
carcinogenic and mutagenic. Due to low biodegradability of dyes, a conventional biological treatment
process is not very effective.Therefore, the treatment of effluents containing such dye is of prime
importancedueto its harmful impacts on receiving waters. Among the applied processes fort he remova I of
substances in waste waters, adsorption has been found to besuperiorto other techniques for wastewater
treatment in terms of initial cost, simplicity of design, ease of operation, and insensitivity to toxic
substances.
Jn this study, the adsorption of an anionic dye Remazol Red RB, from aqueous solution on modified day was
investigated at298, 313 and 333K. Different parameters that influence the adsorption process such as
contact time, initial dye concentration, solution pH and temperature were systematically studied. Adsorption
capacity increased with increasing of temperature, initia I dye concentration and pH. The value of zeta
potential decreased with increasing of pH. Experimental adsorption data were modeled by different
equilibrium isotherms such as Langmuir, Freundlich, Temkin, Dubinin-Radushkevich (D-R ), BET, Halsey,
Harkins-Jura, Smith and Henderson isotherms. The adsorption process followed the Langmuir isotherm
model with high coefficients of correlation (R2 >0.99) atdifferent temperatures. The pseudo~second order
kinetic model fitted well in correlation to the experimental results. Activation energy of the adsorption
process (Ea) were found to be 34.49 kJ mol-1and40.27 kJ mol-1 for inita1 dye concentrations of75 and 150
mg/L, respectively by using the Arrhenius equation, indicating the strong electrostatic interactions between
adsorbent and dye. Thermodynamic parameters suggest thatthe adsorption process is spontaneous and
endothermic in nature.