2013
DOI: 10.1016/j.desal.2013.07.017
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Adsorption kinetics of nitrate ions on ion exchange resin

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Cited by 53 publications
(27 citation statements)
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References 35 publications
(71 reference statements)
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“…For all experimental data shown in this figure, it can be seen that the removal efficiency was increased with the increase of algal biomass weight from 0.05 to 1 g, implying that the optimum amount of biosorbent is 1 g algal biomass/200 ml solution, then beyond 1 g algal biomass dose the removal efficiency reached a plateau which demonstrating the equilibrium state. The reason being that an increase in the biosorbent quantity in the aqueous solution results in a larger exchangeable sites or surface area for Pb(II) sorption, hence the rise in the removal percentage (Hekmatzadeh, et al, 2013). By further increment in sorbent dose, the removal capacity was not increased possibly due to the aggregation of sorbent particles and low surface area.…”
Section: Resultsmentioning
confidence: 99%
“…For all experimental data shown in this figure, it can be seen that the removal efficiency was increased with the increase of algal biomass weight from 0.05 to 1 g, implying that the optimum amount of biosorbent is 1 g algal biomass/200 ml solution, then beyond 1 g algal biomass dose the removal efficiency reached a plateau which demonstrating the equilibrium state. The reason being that an increase in the biosorbent quantity in the aqueous solution results in a larger exchangeable sites or surface area for Pb(II) sorption, hence the rise in the removal percentage (Hekmatzadeh, et al, 2013). By further increment in sorbent dose, the removal capacity was not increased possibly due to the aggregation of sorbent particles and low surface area.…”
Section: Resultsmentioning
confidence: 99%
“…After this time, the adsorbent separation from the solution is carried out by the filter paper and the concentration of the solution is determined. Then the amount and adsorption efficiency are determined from relations 1 and 2 (Bhatnagar et al, 2010;Hekmatzadeh et al, 2013). 2,3,4,5,10,15,20,30,40 and 50 g of wheat straw is added to 100 mL of solution at a concentration of 20 mg/L.…”
Section: Methodsmentioning
confidence: 99%
“…It is generally assumed that the ion-exchange reactions between the adsorbed ions and functional groups are instantaneous, and thus, the sorption process is restricted by film transfer and intraparticle diffusion. Consequently, the particle diffusion model was adopted to investigate the real sorption rate [38], where the relevant parameters, the film mass-transfer coefficient k f (m/s), and pore diffusivity D p (m/s 2 ) were also calculated.…”
Section: Mathematical Modelsmentioning
confidence: 99%