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Application of strongly basic anion exchangers for removal of heavy metal ions in the presence of green chelating agent

机译:强碱性阴离子交换剂在绿色螯合剂存在下用于去除重金属离子的应用

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Sorption properties of strongly basic polystyrene and polyacrylate anion exchangers towards Cu(II), Zn(II), Cd(II) and Pb(II) in the presence of the green chelating agent of a new generation ethylenediamine-N,N'-disuccinic acid (EDDS) were investigated in the batch and column systems. Batch sorption experiments were performed using commercial forms of Amberlite IRA 402, Lewatit MonoPlus MP 500, Amberlite IRA 458 and Amberlite IRA 958. The amount of resin, e.g. the anion exchanger dose (0.1-1.0 g), the initial solution pH (2-12), the initial concentration of sorbed complexes in the M(II)-EDDS = 1:1 system (2 x 10~(-3) to 1.5 x 10~(-2) M), temperature (293-333 K) as well as the contact time (1-120 min) were changed. The sorption capacities of these anion exchangers increased with the increasing initial solution pH, temperature and concentration of complexes. Levels of sorption rapidly approached an equilibrium state within 20-30 min. The equilibrium data of the experiments show that Amberlite IRA 402 and Lewatit MonoPlus MP 500 are good anion exchangers for the removal of EDDS complexes. The sorption characteristics of metal complexes with EDDS onto these anion exchangers were based on the Langmuir and Freundlich isotherms. However, the values of correlation coefficients (R~2) higher than 0.99 show that in the studied concentration range the data were more suitable for the Langmuir model. The maximum sorption capacities (q_0) were 104.17, 62.11, 119.54, 134.93 mg/g for Cu(II), Zn(II), Cd(II) and Pb(II) complexes with EDDS on Amberlite IRA 402, respectively. For Lewatit MonoPlus MP 500 the obtained values were almost analogous. The values of calculated thermodynamic parameters (ΔG°, ΔH° and ΔS°) indicate that the sorption process is endothermic and spontaneous. The sorption kinetic of studied anion exchangers fitted well to the pseudo second-order model. These data were also evaluated based on the Boyd equation. Furthermore, the anion exchangers were characterized by Fourier transform infrared (FT-IR) and scanning electron microscope (SEM).
机译:在新一代乙二胺-N,N'-二琥珀酸的绿色螯合剂存在下,强碱性聚苯乙烯和聚丙烯酸酯阴离子交换剂对Cu(II),Zn(II),Cd(II)和Pb(II)的吸附性能在间歇和塔系统中研究了酸(EDDS)。使用商业形式的Amberlite IRA 402,Lewatit MonoPlus MP 500,Amberlite IRA 458和Amberlite IRA 958进行批量吸附实验。阴离子交换剂剂量(0.1-1.0 g),初始溶液pH(2-12),M(II)-EDDS = 1:1系统中吸附复合物的初始浓度(2 x 10〜(-3)至改变1.5 x 10〜(-2)M),温度(293-333 K)和接触时间(1-120分钟)。这些阴离子交换剂的吸附能力随初始溶液pH,温度和络合物浓度的增加而增加。在20-30分钟内,吸附水平迅速达到平衡状态。实验的平衡数据表明,Amberlite IRA 402和Lewatit MonoPlus MP 500是去除EDDS络合物的良好阴离子交换剂。具有EDDS的金属络合物在这些阴离子交换剂上的吸附特性基于Langmuir和Freundlich等温线。然而,相关系数(R〜2)大于0.99的值表明,在所研究的浓度范围内,数据更适合于朗缪尔模型。在Amberlite IRA 402上,具有EDDS的Cu(II),Zn(II),Cd(II)和Pb(II)配合物的最大吸附容量(q_0)分别为104.17、62.11、119.54、134.93 mg / g。对于Lewatit MonoPlus MP 500,获得的值几乎类似。计算出的热力学参数(ΔG°,ΔH°和ΔS°)的值表明吸附过程是吸热的并且是自发的。研究的阴离子交换剂的吸附动力学很好地拟合了拟二阶模型。这些数据也基于博伊德方程式进行了评估。此外,阴离子交换剂的特征在于傅立叶变换红外光谱(FT-IR)和扫描电子显微镜(SEM)。

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