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

被引:8
|
作者
Hamidi, Roya [1 ]
Kazemi, Pezhman [2 ]
机构
[1] Sahand Univ Technol, Inst Environm Engn, Tabriz, Iran
[2] Islamic Azad Univ, Dept Chem Engn, South Tehran Branch, Tehran, Iran
关键词
Anion exchange; Chloride; Layered double hydroxide; Isotherm; Thermodynamic; MAGNESIUM-ALUMINUM-OXIDE; LAYERED DOUBLE HYDROXIDES; AQUEOUS-SOLUTION; HYDROCHLORIC-ACID; SIMULTANEOUS REMOVAL; DISTILLER WASTE; METHYLENE-BLUE; ANION-EXCHANGE; ADSORPTION; HYDROTALCITE;
D O I
10.1080/19443994.2014.880658
中图分类号
TQ [化学工业];
学科分类号
0817 ;
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.
引用
收藏
页码:332 / 341
页数:10
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