Solvent Polarity Effect when Amberlite-LA2 Is Used in the Extraction of Picric Acid

被引:2
作者
Uslu, Hasan [1 ,3 ]
Datta, Dipaloy [2 ]
Bamufleh, Hisham S. [3 ]
机构
[1] Istanbul Esenyurt Univ, Fac Engn & Architecture, Dept Ind Engn, TR-34510 Istanbul, Turkey
[2] Malaviya Natl Inst Technol, Dept Chem Engn, Jaipur 302017, Rajasthan, India
[3] King Abdulaziz Univ, Fac Engn, Chem & Mat Engn Dept, Jeddah 23218, Saudi Arabia
关键词
SIMULTANEOUS BACK-EXTRACTION; SUPPORTED LIQUID-MEMBRANE; AQUEOUS-SOLUTIONS; SAMPLE CLEANUP; P-NITROPHENOL; WASTE-WATER; DEGRADATION; PHENOL; PRECONCENTRATION; MICROEXTRACTION;
D O I
10.1021/acs.jced.6b00970
中图分类号
O414.1 [热力学];
学科分类号
摘要
The separation and recovery of picric acid (0.061 mol-kg(-1)) from its aqueous solution was studied at a fixed temperature of 298 K. The extraction experiments were performed by using a secondary amine, Amberlite-LA2 (ALA2), dissolved in five different solvents such as dichloromethane (DCM), dodecanol, toluene, benzene, and dodecane. Physical extraction data were also produced by pure solvent alone. The experimental data obtained from the batch studies were analyzed by calculating the distribution coefficient (K-D), extraction efficiency (%E), and loading factor (Z). The highest synergistic effect was achieved with DCM in ALA2 at a concentration of 0.588 mol.kg(-1) as 83.61%. The equilibrium constants for the complex formation between acid and amine (1:1 and 2:1) were calculated for all the solvents applying the mass action law.
引用
收藏
页码:1125 / 1129
页数:5
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