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Kinetics and mechanism of sorption of chloride ion from sodium carbonate manufacturing wastewater by Mg-Al oxide

机译:镁铝氧化物吸附碳酸钠生产废水中氯离子的动力学及机理

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摘要

In this article, the removal of chloride ion generated from industrial wastewater was examined by using magnesium-aluminum (Mg-Al) oxide obtained from Mg-Al layered double hydroxide. The influences of conditions for chloride ion uptake, including quantity of Mg-Al oxide, contact time and temperature on anion exchange has been investigated, respectively. The extent of the chloride, ion removal increased with an increase in the quantity of Mg-Al oxide, contact time, and temperature. Thermodynamic parameters including Gibbs free energy ( increment G degrees), standard enthalpy change ( increment H degrees), and standard entropy change ( increment S degrees) for the process were calculated using the Langmuir constants. Kinetic analyses were conducted using pseudo-first and second-order models. The regression results showed that the uptake process was more accurately represented by pseudo-second-order model. The calculated value of E-a was found to be 77.428 kJ/mol, which indicate that the process of uptake of chloride ion is controlled by the rate of reaction of chloride ion with the Mg-Al oxide rather than diffusion. Results suggested that the uptake process was feasible and endothermic.
机译:在本文中,通过使用从Mg-Al层状双氢氧化物获得的镁铝(Mg-Al)氧化物,研究了去除工业废水中产生的氯离子的方法。研究了氯离子的吸收条件,包括Mg-Al氧化物的量,接触时间和温度对阴离子交换的影响。氯化物的程度,离子的去除随着Mg-Al氧化物的量,接触时间和温度的增加而增加。使用Langmuir常数计算包括吉布斯自由能(增量G度),标准焓变(增量H度)和标准熵变(增量S度)的热力学参数。动力学分析使用伪一阶和二阶模型进行。回归结果表明,吸收过程更准确地表示为伪二级模型。发现E-a的计算值为77.428kJ / mol,这表明氯离子的吸收过程由氯离子与Mg-Al氧化物的反应速率而不是扩散来控制。结果表明摄取过程是可行的并且是吸热的。

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