2005
DOI: 10.1016/j.jhazmat.2005.03.032
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Removal of lead (II) ions from synthetic and real effluents using immobilized Pinus sylvestris sawdust: Adsorption on a fixed-bed column

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Cited by 223 publications
(101 citation statements)
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“…This is attributed to the fact that as the flow rate becomes higher, the contact time between the adsorbate solutes and the adsorbent is minimized in time, and hence the adsorbate molecules do not have enough time to uptake the binding sites on the adsorbent surface or diffuse into the pores of the adsorbents, causing the adsorbate solutes to leave the column before equilibrium to occur and breakpoint time to be reached earlier. These results were corroborated with a number of reported findings [203][204][205].…”
Section: Effect Of Flow Ratesupporting
confidence: 92%
“…This is attributed to the fact that as the flow rate becomes higher, the contact time between the adsorbate solutes and the adsorbent is minimized in time, and hence the adsorbate molecules do not have enough time to uptake the binding sites on the adsorbent surface or diffuse into the pores of the adsorbents, causing the adsorbate solutes to leave the column before equilibrium to occur and breakpoint time to be reached earlier. These results were corroborated with a number of reported findings [203][204][205].…”
Section: Effect Of Flow Ratesupporting
confidence: 92%
“…In the bed operated at 5mL/min, Cd breakthrough was observed after 120 minutes of contact as there was insufficient time for intra-particle diffusion of metal ions into the pores of the zeolite resulting in earlier breakthrough [46]. Hence, the lower the flow rate, the better the metal removal performance of the column [25].…”
Section: Effect Of Flow Ratementioning
confidence: 99%
“…In shorter beds, mass transfer is governed by axial dispersion resulting in decreased diffusion of metal ions [46].…”
Section: Effect Of Bed Heightmentioning
confidence: 99%
“…The breakthrough curves were obtained by plotting the normalized concentration (C t /C 0 ) (ratio of influent and effluent concentrations) versus time or volume (Aksu and Gonen 2004). The total dye adsorbed Q 0 (mg/g) in the fixed-bed column was calculated using the following equation (Taty-Castodes et al 2005):…”
Section: Column Studymentioning
confidence: 99%