Reverse micellar extraction of dyes based on fatty acids and recoverable organic solvents

被引:13
|
作者
Bukman, Lais [1 ]
De Souza, Vagner Roberto [1 ]
Camargo Fernandes, Nadia Regina [2 ]
Caetano, Wilker [1 ]
Batistela, Vagner Roberto [3 ]
Hioka, Noboru [1 ]
机构
[1] Univ Estadual Maringa, Dept Chem, 5790 Colombo Ave, BR-87020900 Maringa, PR, Brazil
[2] Univ Estadual Maringa, Dept Chem Engn, 5790 Colombo Ave, BR-87020900 Maringa, PR, Brazil
[3] Univ Estadual Maringa, Dept Technol, 1800 Dr Angelo Moreira da Fonseca Ave, BR-87506370 Umuarama, PR, Brazil
关键词
Reverse micelles; Extraction; Dyes; Wastewater; Fatty acids; Isopentanol; LIQUID-LIQUID-EXTRACTION; IONIC DYES; REMOVAL; WATER; POLLUTANTS; SYSTEMS;
D O I
10.1016/j.seppur.2020.116772
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Reverse micelle extraction occurs when a substrate is removed from the aqueous phase to an organic phase by reverse micelles in an immiscible solvent with water. In this work, three fatty acids: stearic acid (C-18), palmitic acid (C-16) and lauric acid (C-12) were investigated in the extraction of the methylene blue (MB+) dye, as a model of cationic compound, from aqueous solutions. Experiments were performed in quartz cuvettes with 2.0 mL of MB+ 6.25 x 10(-4) mol L-1 at pH 10, and 1.0 mL of surfactants in isopentanol, from 3.0 to 6.0 mmol L-1. At pH 10, the three fatty acids presented efficiency in MB+ removal superior to 99%. However, for all tested conditions, C-18 at 3.7 mmol L-1 presented the fastest separation of phases. By chemometric factorial design, the maximum efficiency of separation was superior to 99% and occurred with at least 21% of organic phase, the most important variable for this system. In optimal condition, the total time of separation of phases was around 5h. After the forward process, the organic phase containing reverse micelles and MB+ was acidified with diluted H2SO4 for protonation and precipitation of fatty acids. Therefore, in this case, reverse micelles were disrupted and MB+ was concentrated in a small volume of acid aqueous solution, thus allowing around 90% of recuperation of isopentanol for reuse. The main advantages of this process include selectivity, mild thermal conditions, low energy consumption, potential for use at the industrial scale and possibility of application in the removal of other cationic pollutants.
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页数:8
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