2012
DOI: 10.1016/j.cej.2012.03.047
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Equilibrium, thermodynamics and kinetics studies for the removal of alpha and beta endosulfan by adsorption onto bentonite clay

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Cited by 36 publications
(18 citation statements)
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“…The factor of linear correlation was higher for the pseudo-second-order model (0.9966), so that in the adsorption process with eggshell present best fit to this model. The chemisorption in this adsorption system is apparently present [23]. Moreover, the q e value obtained experimentally (17.98 mg•g −1 ) with Langmuir isotherm was closest to that obtained applying the kinetic of pseudo-second-order (19.76 mg•g −1 ).…”
Section: Adsorption Kinetics Of Leaching (Previously Oxidized) Using supporting
confidence: 72%
“…The factor of linear correlation was higher for the pseudo-second-order model (0.9966), so that in the adsorption process with eggshell present best fit to this model. The chemisorption in this adsorption system is apparently present [23]. Moreover, the q e value obtained experimentally (17.98 mg•g −1 ) with Langmuir isotherm was closest to that obtained applying the kinetic of pseudo-second-order (19.76 mg•g −1 ).…”
Section: Adsorption Kinetics Of Leaching (Previously Oxidized) Using supporting
confidence: 72%
“…Generally, the adsorption processes include three stages. The first is considered as a diffusion of adsorbate through the solution to the external surface of 6 Journal of Nanomaterials [32]. It is important to note that the correlation coefficients are lower than 0.81 for ACSH at different temperatures, which suggest a nonlinear relationship.…”
Section: Adsorption Kineticsmentioning
confidence: 99%
“…For adsorption isotherms, dye solutions of different concentrations were agitated with the known amount of adsorbent until the equilibrium was achieved. Various experimental parameters such as pH (2)(3)(4)(5)(6)(7)(8)(9)(10)(11), temperature (25-45 °C), adsorbent mass (0.1-2 g/L), initial BY28 concentration (25-300 mg/L) and contact time were investigated. The amount of dye removed and the amount of dye adsorbed on per unit of adsorbent (q e ) at the sampling time were calculated using the following equations:…”
Section: Experimental Adsorption Isothermsmentioning
confidence: 99%
“…Textile industries are one of the largest consumers of water and hence producers of liquid effluents. The dyeing and finishing processes generate volumes of wastewaters in the range 45-450 m 3 per ton of product, 1 containing salts, acids, bases, additives and unfixed dyes. A suitable treatment of these complex wastewaters should lead to a strong decline on the organic load, and desirably to a complete elimination of the residual color.…”
Section: Introductionmentioning
confidence: 99%