2015
DOI: 10.1039/c5ra03339j
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Adsorption of herbicide 2-(2,4-dichlorophenoxy)propanoic acid by electrochemically generated aluminum hydroxides: an alternative to chemical dosing

Abstract: This research article presents an in situ electrosynthesis of aluminum hydroxides by anodic dissolution of sacrificial aluminum anode and their application towards the adsorption of herbicide 2-(2,4dichlorophenoxy)propanoic acid (2,4-DP) from aqueous solution. Different sacrificial anode material like iron, magnesium, zinc and aluminum are tested and stainless steel is used as the cathode. The optimization of different experimental parameters like current density, pH, temperature and interelectrode distance on… Show more

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Cited by 69 publications
(28 citation statements)
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“…It turned out that the adsorption equilibrium of nitrate on the NPs was accomplished in 180 min.Two simplified kinetic models, including pseudo‐first‐order and pseudo‐second‐order equations, were checked out. The rate constant of adsorption can be defined using the pseudo‐first‐orderequation given by Langergren : log(qnormaleqnormalt)= logqnormale[k12.303t], where k 1 is the pseudo‐first‐order rate constant (min −1 ), and q e and q t are the amounts of nitrate adsorbed (mg g −1 ) at equilibrium and at time t (min).…”
Section: Resultsmentioning
confidence: 99%
See 1 more Smart Citation
“…It turned out that the adsorption equilibrium of nitrate on the NPs was accomplished in 180 min.Two simplified kinetic models, including pseudo‐first‐order and pseudo‐second‐order equations, were checked out. The rate constant of adsorption can be defined using the pseudo‐first‐orderequation given by Langergren : log(qnormaleqnormalt)= logqnormale[k12.303t], where k 1 is the pseudo‐first‐order rate constant (min −1 ), and q e and q t are the amounts of nitrate adsorbed (mg g −1 ) at equilibrium and at time t (min).…”
Section: Resultsmentioning
confidence: 99%
“…It turned out that the adsorption equilibrium of nitrate on the NPs was accomplished in 180 min.Two simplified kinetic models, including pseudo-first-order and pseudosecond-order equations, were checked out. The rate constant of adsorption can be defined using the pseudo-firstorderequation given by Langergren [36,37]: logðq e 2q t Þ5 logq e 2 k 1 2:303 t ;…”
Section: Adsorption Kinetic Modelmentioning
confidence: 99%
“…The trend of removal ratio curve illustrated that with the expansion of inter‐electrode distance, the resistance enlarged and the electron transfer was blocked, thus slowing down the degradation of AR1. Short distance between anode and cathode required low energy for motion of ions, which due to that shorter travel path of electrons could decrease the resistance of electrons transfer, and then the productive rate of active groups was accelerated . But if the gap between two electrodes is too narrow, the system would result in short circuit and the too high electron transfer velocity causes the drastic oxygen evolution reaction which inhibits the direct oxidation of AR1.…”
Section: Resultsmentioning
confidence: 99%
“…The linear form of the pseudo-second-order kinetic model is given as following equation [48], The linear form of the pseudo-second-order kinetic model is given as following equation [48],…”
Section: Effect Of Temperature and Adsorption Kineticsmentioning
confidence: 99%
“…Where q e is defined above, q t (mg g 21 ) is the amount of Ni(II) adsorbed at any time (min) and k 1 (min 21 ) is the rate constant. The linear form of the pseudo-second-order kinetic model is given as following equation [48],…”
Section: Effect Of Temperature and Adsorption Kineticsmentioning
confidence: 99%