2021
DOI: 10.3390/molecules26227046
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Adsorption Capacities of Iron Hydroxide for Arsenate and Arsenite Removal from Water by Chemical Coagulation: Kinetics, Thermodynamics and Equilibrium Studies

Abstract: Arsenic (As)-laden wastewater may pose a threat to biodiversity when released into soil and water bodies without treatment. The current study investigated the sorption properties of both As(III, V) oxyanions onto iron hydroxide (FHO) by chemical coagulation. The potential mechanisms were identified using the adsorption models, ζ-potential, X-ray diffraction (XRD) and Fourier Transform Infrared Spectrometry (FT-IR) analysis. The results indicate that the sorption kinetics of pentavalent and trivalent As species… Show more

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Cited by 10 publications
(4 citation statements)
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“…Kinetic adsorption equations such as the pseudo-first order (PFO) and pseudo-second order (PSO) models were used to examine the pollutant adsorption profiles [ 17 ]. The non-linear forms of the PFO and PSO kinetic models are expressed by Equations (1) and (2), respectively [ 18 ]: where q t (mg g −1 ) and q e (mg g −1 ) indicate the adsorption capacity of ferric sulfate towards pollutant removal at the time (t) and equilibrium. k 1 (min −1 ) and k 2 (g mg −1 min −1 ) are the respective rate constants for the PFO and PSO models.…”
Section: Methodsmentioning
confidence: 99%
“…Kinetic adsorption equations such as the pseudo-first order (PFO) and pseudo-second order (PSO) models were used to examine the pollutant adsorption profiles [ 17 ]. The non-linear forms of the PFO and PSO kinetic models are expressed by Equations (1) and (2), respectively [ 18 ]: where q t (mg g −1 ) and q e (mg g −1 ) indicate the adsorption capacity of ferric sulfate towards pollutant removal at the time (t) and equilibrium. k 1 (min −1 ) and k 2 (g mg −1 min −1 ) are the respective rate constants for the PFO and PSO models.…”
Section: Methodsmentioning
confidence: 99%
“…With the gradual rise in the pollutant concentration, there was a drop in the efficacy of EBT adsorption; Figure 5(b) shows that the optimum removal performance of EBT was at 10 mg.L -1 . Higher pollutant concentration leads to decrease in percentage of dye elimination at the same adsorption time (Khan et al, 2021;Y. Wu et al, 2013).…”
Section: Initial Dye Concentrationmentioning
confidence: 99%
“…The untreated wastewater discharge of these dyes into the water bodies give serious threats to aquatic life and human being (Manzar, Waheed, Qazi, Blaisi, & Ullah, 2019). Therefore, introducing new effective methods and materials for removing the pollutants and dyes from wastewater is drastically required (Akram et al, 2023;Bano et al, 2024;Inam et al, 2021;Kishore et al, 2023).…”
Section: Introductionmentioning
confidence: 99%
“…The methods that are currently used for As remediation include ion exchange, phytoremediation, , adsorption, chemical precipitation, , electrokinetic, , and electrocoagulation. , Within the adsorption methods, application of affordable iron-based material, such as iron-hydroxide, zero-valent iron, iron oxide, , and bimetal oxides, is noteworthy. In brief, the adsorption process on these materials is associated with electrostatic attraction, ion exchange, and surface complexation, with a further oxidation/reduction reaction over the surface, depending on the material composition and the adsorbing As species. ,, …”
Section: Introductionmentioning
confidence: 99%