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Preparation of a novel Fe3O4/HCO composite adsorbent and the mechanism for the removal of antimony (III) from aqueous solution

机译:新型Fe3O4 / HCO复合吸附剂的制备及其从水溶液中除去锑(III)的机制

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A novel adsorbent (Fesub3/subOsub4/sub/HCO) was prepared via co-precipitation from a mix of ferriferrous oxide and a Ce-rich waste industrial sludge recovered from an optical polishing activity. The effect of system parameters including reaction time, pH, dose, temperature as well as initial concentration on the adsorption of Sb(III) were investigated by sequential batch tests. The Sb(III)/Fesub3/subOsub4/sub/HCO system quickly reached adsorption equilibrium within 2?h, was effective over a wide pH (3-7) and demonstrated excellent removal at a 60?mg/L Sb(III) concentration. Three isothermal adsorption models were assessed to describe the equilibrium data for Sb(III) with Fesub3/subOsub4/sub/HCO. Compared to the Freundlich and dubinin-radushkevich, the Langmuir isotherm model showed the best fit, with a maximum adsorption capacity of 22.853?mg/g, which exceeds many comparable absorbents. Four kinetic models, Pseudo-first-order, Pseudo-second-order, Elovich and Intra-particle, were used to fit the adsorption process. The analysis showed that the mechanism was pseudo-second-order and chemical adsorption played a dominant role in the adsorption of Sb(III) by Fesub3/subOsub4/sub/HCO (correlation coefficient Rsup2/sup?=?0.993). Thermodynamic calculations suggest that adsorption of Sb(III) ions was endothermic, spontaneous and a thermodynamically feasible process. The mechanism of the adsorption of Sb(III) on Fesub3/subOsub4/sub/HCO could be described by the synergistic adsorption of Sb (III) on Fesub3/subOsub4/sub, FeCesub2/subOsub4/sub and hydrous ceric oxide. The Fesub3/subOsub4/sub/HCO sorbent appears to be an efficient and environment-friendly material for the removal of Sb(III) from wastewater.
机译:通过来自氧化铁混合物的共沉淀和从光学抛光中恢复的CE的富含废物工业污泥的共沉淀制备了一种新型吸附剂(Fe 3 / o /亚> / hco)活动。通过顺序批量试验研究了系统参数包括反应时间,pH,剂量,温度以及初始浓度的初始浓度的效果。 Sb(iii)/ Fe 3 O 4 / hco系统在2℃内快速达到吸附平衡,在宽pH(3-7)上有效,并展示优异以60×mg / L Sb(III)浓度去除。评估了三种等温吸附模型,以用Fe 3 O 4 / hco描述Sb(III)的平衡数据。与Freundlich和Dubinin-Radushkevich相比,Langmuir等温线模型显示出最合适的,最大吸附容量为22.853Ωmg/ g,超过许多可比吸收剂。使用四种动力学模型,伪一阶,伪二阶,ELOVICH和颗粒,适用于吸附过程。分析表明,该机制是伪二阶,化学吸附在通过Fe 3 O 4 / hco的吸附中发挥了显性作用,在Sb(III)的吸附中起作用的作用系数R 2 ?=?0.993)。热力学计算表明,Sb(III)离子的吸附是吸热的,自发性和热力学上可行的过程。 Sb(III)对Fe 3 O 4 / hco的机制可以通过SB(III)对Fe 3的协同吸附来描述 3 < /亚> O 4 ,FECE 2 O 4 和含水凝氧氧化物。 Fe 3 O 4 / hco吸附剂似乎是一种高效且环保的材料,用于从废水中去除Sb(III)。

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