2004
DOI: 10.1016/j.chemosphere.2003.12.025
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Removal of arsenic from water by electrocoagulation

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Cited by 523 publications
(66 citation statements)
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“…Only the highest current density of 45 A m −2 was selected to exemplify the EC process for GW because the treatment time was relatively large (>15 min) when lower current densities were applied. These used current density values are consistent with those reported in the literature for this process (Kumar et al 2004;Yu et al 2005;Yilmaz et al 2005).…”
Section: Electrocoagulation Experimentssupporting
confidence: 83%
“…Only the highest current density of 45 A m −2 was selected to exemplify the EC process for GW because the treatment time was relatively large (>15 min) when lower current densities were applied. These used current density values are consistent with those reported in the literature for this process (Kumar et al 2004;Yu et al 2005;Yilmaz et al 2005).…”
Section: Electrocoagulation Experimentssupporting
confidence: 83%
“…In high voltages, size and growth rate of produced flocs increase and this in turn affects the efficiency of the process [19]. By electrical potential increase the amount of oxidized aluminum increases and consequently hydroxide flocs with high adsorption rate increase and this leads to an increase in the efficiency of pollutant removal [43]. On the other hand, by electrical current increase, the density of bubbles increases while their size decreases hence the flotation efficiency increases [44].…”
Section: Turbidity Removalmentioning
confidence: 98%
“…Among the 11 chemical decontamination processes developed, the solubilization 12 of As, Cr, Cu, PCP and DF using alkaline solutions and a bio- 13 surfactant seemed to be very promising in terms of contaminant 14 removal efficiencies and operational costs. Indeed, Reynier et al [6] 15 highlighted that more than 60% of As, 32% of Cr, 77% of Cu and 87% 16 of PCP can be removed from contaminated soils after 3 leaching 17 steps of 2 h each carried out at 80 C with a pulp density fixed at 18 10% in the presence of sodium hydroxide (0.5 M) and a surfactant 19 ([BW] = 2%). For the DF, the removal yields ranged from 25 to 74% 20 depending on the nature of the soil and the initial contaminant 21 levels.…”
Section: Introductionmentioning
confidence: 99%
“…50 Therefore, it is best to oxidize As(III) to As(V) before precipitation 51 to obtain better removal rates as the solubility of As(V) is lower 52 than the solubility of As(III). To enhance the removal of chromium 53 from effluents, it is better to reduce Cr(VI) in Cr(III) as the solubility 54 of Cr(III) is lower than the solubility of Cr(VI) [16,17]. However, As 55 (V) and Cr(III) are the preponderant forms found in contaminated 56 soils and the chemical leaching processes developed allowed 57 the solubilization of As and Cr in their more easily forms to be 58 precipitated without any oxidation or reduction.…”
Section: Introductionmentioning
confidence: 99%