2010
DOI: 10.5714/cl.2010.11.3.224
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Utilization of Cotton Stalks-Biomass Waste in the Production of Carbon Adsorbents by KOH Activation for Removal of Dye-Contaminated Water

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Cited by 23 publications
(11 citation statements)
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“…Also, these results were analyzed using two principal isotherm models, Langmuir and Freundlich. It was found that the equilibrium isotherms were well described by the Langmuir equation, giving a maximum adsorption capacity of 19.2 mg/g by sawdust at 30 • C. Furthermore, the adsorption kinetics can be well represented by the pseudo-second-order model equation (24)(25)(26)(27) .…”
Section: Discussionmentioning
confidence: 94%
See 1 more Smart Citation
“…Also, these results were analyzed using two principal isotherm models, Langmuir and Freundlich. It was found that the equilibrium isotherms were well described by the Langmuir equation, giving a maximum adsorption capacity of 19.2 mg/g by sawdust at 30 • C. Furthermore, the adsorption kinetics can be well represented by the pseudo-second-order model equation (24)(25)(26)(27) .…”
Section: Discussionmentioning
confidence: 94%
“…The adsorption kinetic process is largely dependent on the physical and/or chemical characteristics of both the adsorbent and adsorbate (24)(25)(26)(27) . Figure 9 shows the controlling mechanism in the adsorption of the basic blue 41 (BB41) with initial concentration of 100 mg/L at 30 o C examined using various kinetic models such as pseudo-first order, pseudo-second order and Elovich models in order to determine whether the process is such as mass transfer and/or chemical reaction were evolved:…”
Section: Kinetics Of Adsorptionmentioning
confidence: 99%
“…The micropore volume was determined via Dubinin-Radushkevich equation (V DR ) considering N 2 adsorption data at relative pressure lower than 0.1. The N 2 volume adsorbed at relative pressure close to 0.10 (V 0.10 ) was calculated in order to obtain the mesopore volume (V meso ) of the samples using the equation V meso = V net − V 0.10 (Fathy et al, 2010).…”
Section: Characterization Of Activated Carbonsmentioning
confidence: 99%
“…This mixture was admitted into stainless steel reactor and heated at different heat treatment temperatures of 700, 750 and 800 o C. At each activation temperature, the sample was kept for 30 min in a self-generated atmosphere. Then the obtained ACs were thoroughly washed with 1 N HCl solution, followed by hot water washing for several times until pH 6 and dried at 100 o C overnight [28].…”
Section: Preparation Of Acsmentioning
confidence: 99%
“…The cotton is the main crop in Egypt, and the planting area is approximately 3 million ha, and the estimated amounts of CS are more than 1.6 million tonnes are generated annually [27]. Therefore, indigenous-low-cost CS-ACs with plenty of surface oxygencontaining functional groups were prepared by KOH activation of semicarbonized CS as described in previous investigation [28]. In this paper, a mild concentration of acid was used with KOH-ACs, in order to improve the adsorption capacity of these carbons for removal of Pb (II) ions from aqueous solution by batch method.…”
Section: Introductionmentioning
confidence: 99%