2019
DOI: 10.1002/ep.13118
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Effective Parameters, Equilibrium, and Kinetics of Fluoride Adsorption on Prosopis cineraria and Syzygium cumini Leaves

Abstract: This study was designed to present a facile and effective biosorbent from Prosopis cineraria and Syzygium cumini leave (PCL and SCL) for fluoride removal. The test was done in batch mode and the effect of contact time (5, 25, 60, 90, and 120 min), initial fluoride concentration level (3, 5, 8, and 12 mg/L), and biosorbent dose (1, 3, 5, 10, and 25 g/L) on the biosorption process were examined. The optimum conditions for the maximum fluoride removal were occurred at 1 g/L biosorbent dose and contact time of 120… Show more

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Cited by 19 publications
(9 citation statements)
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“…Keshtkar et al . investigated the fluoride removal efficiency by increasing the dose of Prosopis cineraria leaves from 1 to 25 g L −1 20 . Fluoride removal increased with the adsorbent dose from 1 to 10 g L −1 followed by a plateau.…”
Section: Resultsmentioning
confidence: 99%
See 1 more Smart Citation
“…Keshtkar et al . investigated the fluoride removal efficiency by increasing the dose of Prosopis cineraria leaves from 1 to 25 g L −1 20 . Fluoride removal increased with the adsorbent dose from 1 to 10 g L −1 followed by a plateau.…”
Section: Resultsmentioning
confidence: 99%
“…In recent years, several efforts have been made in order to develop practical adsorbents. Modified pumice, 14 Moringa oleifera seed ash, 15 Padina sanctae‐crucis algae, 16 cuttlebone, 17 bauxite, 18 decyltrimethylammonium bromide/H 2 O 2 solution‐treated organic matter‐rich clay, 19 Prosopis cineraria and Syzygium cumini leaves, 20 MgFe 2 O 4 –chitosan–CaAl composite, 13 washed and dried montmorillonite 4 and three‐dimensional porous Ca‐modified Mg–Zr mixed metal oxides 21 are some of the adsorbents investigated. A major difficulty in achieving high percentages of fluoride removal is the need to modify water pH which has outcomes for potability 12 .…”
Section: Introductionmentioning
confidence: 99%
“…This model assumed that the amount of change in the solute content over time is logarithmically proportional to changes in the saturation concentration and the content of biosorbent over time. 39 The pseudo-second-order supposed that the sorption process can be controlled by chemical biosorption. 39 Elovich kinetic model assumes that the active sites of biosorption surface are energetically heterogenous in nature; therefore it is one of the important models for describing the chemisorption process.…”
Section: Adsorption Kineticmentioning
confidence: 99%
“…39 The pseudo-second-order supposed that the sorption process can be controlled by chemical biosorption. 39 Elovich kinetic model assumes that the active sites of biosorption surface are energetically heterogenous in nature; therefore it is one of the important models for describing the chemisorption process. 59 The biosorption process follows three ordinal steps:…”
Section: Adsorption Kineticmentioning
confidence: 99%
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