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Adsorptive selenite removal from water using iron-coated GAC adsorbents

机译:铁涂层GAC吸附剂从水中的吸附性亚硒酸盐去除

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Removal of selenite from aqueous phase using iron-coated granular activated carbons (GAC) was investigated in this study. Five different types of GAC were used for iron coating by oxidizing ferrous chloride with sodium hypochlorite and the iron-coated GAC (Fe-GAC) were tested for selenite removal. Nitrogen adsorption-desorption analyses indicated that Brunauer-Emmett-Teller (BET) specific surface area, pore size, and pore volume decreased with the iron coating. The Darco 12 × 20 GAC was shown to be the most effective adsorbent among the five tested GACs after iron coating. Among the different concentrations used for iron coating, the Darco 12 × 20 GAC coated with 0.1 M ferrous chloride achieved the highest selenite removal (97.3%). High removal efficiency of selenite occurred in a wide range of pH (i.e., 2-8), but the efficiency decreased when pH was higher than 8. Adsorption kinetics showed that selenite removal efficiency reached more than 90% after 6-h adsorption for initial selenium concentration of 2 mg/L and equilibrium was obtained after 48 h. A pseudo-second-order kinetic model was found to characterize the adsorption kinetics well for all the initial selenium concentrations and temperatures tested (R~2 ≥ 0.9969). Three temperatures (25, 35, 45 ℃) were used to examine temperature effect on the adsorption behavior of the Fe-GAC with initial selenium concentration of 1 mg/L. Activation energy was calculated to be 30.42 kJ/mol. Adsorption isotherms for initial selenium concentration of 2 mg/L at various temperatures and ionic strengths were developed and the data generally fit the Langmuir model well (R~2 ≥ 0.994). The adsorption capacity reached as high as 2.50 mg-Se/g-adsorbent at equilibrium for initial concentration of 2 mg/L at 25 ℃. The Gibbs free energy was determined to be negative, indicating the spontaneous nature of the adsorption reaction. Oxyanion competitive adsorption showed that sulfate (0.1-5 mM) barely affected selenite adsorption. Other anions (phosphate, silicate and carbonate) impact selenite adsorption to various degrees with phosphate completely excluded selenite adsorption at 5 mM. The possible adsorption mechanisms were discussed.
机译:在这项研究中,研究了使用铁包被的颗粒活性炭(GAC)从水相中去除亚硒酸盐。通过用次氯酸钠氧化氯化亚铁,将五种不同类型的GAC用于铁涂层,并测试了铁涂层GAC(Fe-GAC)去除亚硒酸盐的能力。氮吸附-解吸分析表明,Brunauer-Emmett-Teller(BET)的比表面积,孔径和孔体积随铁涂层的增加而降低。在涂覆铁之后,Darco 12×20 GAC被证明是五个测试的GAC中最有效的吸附剂。在用于铁涂层的不同浓度中,用0.1 M氯化亚铁涂层的Darco 12×20 GAC的亚硒酸盐去除率最高(97.3%)。在较宽的pH范围(即2-8)下,亚硒酸盐的去除效率很高,但当pH高于8时,效率降低。吸附动力学表明,吸附6小时后,亚硒酸钠的去除效率达到90%以上。硒浓度为2 mg / L,在48 h后达到平衡。发现伪二级动力学模型可以很好地表征所有初始硒浓度和测试温度下的吸附动力学(R〜2≥0.9969)。三种温度(25、35、45℃)用于考察温度对初始硒浓度为1 mg / L的Fe-GAC吸附行为的影响。活化能经计算为30.42kJ / mol。建立了在不同温度和离子强度下初始硒浓度为2 mg / L的吸附等温线,该数据通常很好地拟合了Langmuir模型(R〜2≥0.994)。在25℃初始浓度为2 mg / L时,吸附量在平衡时高达2.50 mg-Se / g吸附剂。吉布斯自由能被确定为负,表明吸附反应的自发性质。富氧离子竞争性吸附表明,硫酸盐(0.1-5 mM)几乎不影响亚硒酸盐的吸附。其他阴离子(磷酸根,硅酸根和碳酸根)在不同程度上影响亚硒酸盐的吸附,而磷酸盐完全排除了5 mM的亚硒酸盐吸附。讨论了可能的吸附机理。

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