“…As the adsorption commenced with time there was exhaustion of adsorption sites with adsorbent. At his stage the phenomenon of migration of Adsorbate from the exterior to the interior sites of the adsorbent particles took the control of adsorption and the adsorption observed was less effective [55,56]. The result agrees with the findings of A.V.…”
“…As the adsorption commenced with time there was exhaustion of adsorption sites with adsorbent. At his stage the phenomenon of migration of Adsorbate from the exterior to the interior sites of the adsorbent particles took the control of adsorption and the adsorption observed was less effective [55,56]. The result agrees with the findings of A.V.…”
“…Similar results were observed by [16] who worked on rice husks and [17] who worked on treated sawdust of sissoo wood. [18] demonstrated that the adsorption of Pb (II) ions increased linearly as the amount of adsorbent (mixture of activated charcoal and peanut shell) increased from 1.0 g to 3.0 g and became constant from 3.0 g to 5.0 g.…”
Section: Effect Of Weight Of Adsorbent and Particle Size On Adsorptiosupporting
“…Figure 3 shows the plot of the effect of adsorbent dosage on the removal efficiency of zinc. It is evident from the plot that rate of removal increases with an increase in MISCBA dosage, literally this is attributed to the availability of more adsorption sites at increased attentiveness of the adsorbent material with regard to complexation of metal ions (Ahmad et al [16]). Removal percentage of zinc increased from 73.5% to 91.1% with an increase in MISCBA adsorbent at equilibrium condition.…”
In this particular research, microwave incinerated sugarcane bagasse ash (MISCBA) obtained by incinerating the sugarcane bagasse was utilized as a low cost adsorbent for the removal of ZnCl 2 metal ion from synthetic wastewater through the batch adsorption approach. It was realized that the thermal incineration of the sugarcane bagasse changed the morphological structure of the bagasse. In addition, the surface structure of the sugarcane bagasse has changed from non-porous to a porous surface after incineration. The effect of pH and contact time, adsorbent dosage and initial metal concentration was investigated in this study. A pH value of 6 was found to be optimum. Furthermore, the percentage of adsorption improves with an increase in contact time and a contact time of 180 mins was found to be optimum after attaining equilibrium with a removal efficiency of 96.3%. The equilibrium data was well described by Freudlich as well as the Langmuir model with a correlation coefficient of 0.997 and 0.984. The kinetic data fitted well into the pseudo-second order model.
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