2005
DOI: 10.1016/j.procbio.2005.02.026
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Equilibrium studies for the sorption of chromium and nickel from aqueous solutions using raw rice bran

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Cited by 221 publications
(80 citation statements)
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“…3 The use of alternative materials in retaining or removing pollutants from aqueous systems has been studied to lower the expenses of materials and to reduce the treatment of some wastes and contaminated solutions. 4 Activities such as electroplating and industries that process materials such as leather, cement, steel, and fertilizer are responsible for releasing toxic heavy metals that can cause severe damages to human health and the environment. 5 One such pollutant, chromium, and its compounds persist in the environment in oxidization states of Cr 3 + and the more toxic Cr 6+ .…”
Section: Introductionmentioning
confidence: 99%
“…3 The use of alternative materials in retaining or removing pollutants from aqueous systems has been studied to lower the expenses of materials and to reduce the treatment of some wastes and contaminated solutions. 4 Activities such as electroplating and industries that process materials such as leather, cement, steel, and fertilizer are responsible for releasing toxic heavy metals that can cause severe damages to human health and the environment. 5 One such pollutant, chromium, and its compounds persist in the environment in oxidization states of Cr 3 + and the more toxic Cr 6+ .…”
Section: Introductionmentioning
confidence: 99%
“…The chemical activity of these species, with adjacent hydroxyl groups, contributes to the capture of cations, enabling to form chelates. The formation of complex compounds can also occur with the carbonyl or hydroxyl compound polyphenols (Oliveira et al, 2005).…”
Section: Resultsmentioning
confidence: 99%
“…The initial and final concentration of phenol was analyzed on UV-Vis spectrophotometer-Perkin Elmer Lambda 25" at λ max 660 nm. The amount of adsorption at equilibrium (Q e mg/g) and sorption efficiency (%) were calculated according to the expressions; Where C o and C e are the initial and equilibrium concentration (mg/L), V the volume of solution (L), m the weight of almond shells activated carbon (g) and C is the solution concentration at the end of the sorption process (mg/L) 15 . Figure 1 shows the B.E.T isotherms obtained for phenol adsorption on ASAC and F-400 that illustrate the synthesis of microporous structures with a good surface area and micropore volume.…”
Section: Adsorption Isothermmentioning
confidence: 99%