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首页> 外文期刊>Journal of Hazardous Materials >Ion-exchange of Pb~(2+), Cu~(2+), Zn~(2+), Cd~(2+), and Ni~(2+) ions from aqueous solution by Lewatit CNP 80
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Ion-exchange of Pb~(2+), Cu~(2+), Zn~(2+), Cd~(2+), and Ni~(2+) ions from aqueous solution by Lewatit CNP 80

机译:利用Lewatit CNP 80从水溶液中进行Pb〜(2 +),Cu〜(2 +),Zn〜(2 +),Cd〜(2+)和Ni〜(2+)离子的离子交换

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摘要

Removal of trace amounts of heavy metals can be achieved by means of selective ion-exchange processes. The newly developed resins offered a high resin capacity and faster sorption kinetics for the metal ions such as Pb~(2+), Cu~(2+), Zn~(2+), Cd~(2+), and Ni~(2+) ions. In the present study, the removal of Pb~(2+), Cu~(2+), Zn~(2+), Cd~(2+), and Ni~(2+) ions from aqueous solutions was investigated. Experimental investigations were undertaken using the ion-exchange resin Lewatit CNP 80 (weakly acidic) and were compared with Lewatit TP 207 (weakly acidic and chelating). The optimum pH range for the ion-exchange of the above mentioned metal ions on Lewatit CNP 80 and Lewatit TP 207 were 7.0-9.0 and 4.5-5.5, respectively. The influence of pH, contact time, metal concentration and amount of ion-exchanger on the removal process was investigated. For investigations of the exchange equilibrium, different amounts of resin were contacted with a fixed volume of Pb~(2+), Cu~(2+), Zn~(2+), Cd~(2+), and Ni~(2+) ion containing solution. The obtained sorption affinity sequence in the presented work was Ni~(2+) > Cu~(2+) > Cd~(2+) > Zn~(2+) > Pb~(2+). The metal ion concentrations were measured by AAS methods. The distribution coefficient values for metal ions of 10~3 M initial concentration at 0.1 mol/L ionic strength show that the Lewatit CNP 80 was more selective for Ni~(2+), Cu~(2+) than it was for Cd~(2+), Zn~(2+) and Pb~(2+). Langmuir isotherm was applicable to the ion-exchange process and its contents were calculated. The uptake of metal ions by the ion-exchange resins was reversible and thus has good potential for the removal of Pb~(2+), Cu~(2+), Zn~(2+), Cd~(2+), and Ni~(2+) from aqueous solutions. The amount of sorbed metal ion per gram dry were calculated as 4.1, 4.6, 4.7, 4.8, and 4.7mequiv./g dry resin for Pb~(2+), Cu~(2+), Zn~(2+), Cd~(2+), and Ni~(2+), respectively. Selectivity increased in the series: Cd~(2+) > Pb~(2+) > Cu~(2+) > Ni~(2+) > Zn~(2+). The results obtained showed that Lewatit CNP 80 weakly acidic resin had shown better performance than Lewatit TP 207 resin for the removal of metals. The change of the ionic strength of the solution exerts a slight influence on the removal of Pb~(2+), Cu~(2+), Zn~(2+), Cd~(2+), and Ni~(2+). The presence of low ionic strength or low concentration of NaNC>3 does not have a significant effect on the ion-exchange of these metals by the resins. We conclude that Lewatit CNP 80 can be used for the efficient removal of Pb~(2+), Cu~(2+), Zn~(2+), Cd~(2+), and Ni~(2+) from aqueous solutions.
机译:可以通过选择性离子交换工艺除去痕量的重金属。新开发的树脂为Pb〜(2 +),Cu〜(2 +),Zn〜(2 +),Cd〜(2+)和Ni〜等金属离子提供了高树脂容量和更快的吸附动力学(2+)个离子。本文研究了从水溶液中去除Pb〜(2 +),Cu〜(2 +),Zn〜(2 +),Cd〜(2+)和Ni〜(2+)离子的方法。使用离子交换树脂Lewatit CNP 80(弱酸性)进行了实验研究,并与Lewatit TP 207(弱酸性和螯合)进行了比较。 Lewatit CNP 80和Lewatit TP 207上上述金属离子进行离子交换的最佳pH范围分别为7.0-9.0和4.5-5.5。研究了pH,接触时间,金属浓度和离子交换剂用量对去除工艺的影响。为了研究交换平衡,将不同量的树脂与固定体积的Pb〜(2 +),Cu〜(2 +),Zn〜(2 +),Cd〜(2+)和Ni〜( 2+)含离子溶液。在本文中获得的吸附亲和力顺序为Ni〜(2+)> Cu〜(2+)> Cd〜(2+)> Zn〜(2+)> Pb〜(2+)。通过AAS方法测量金属离子浓度。在离子强度为0.1 mol / L时,初始浓度为10〜3 M的金属离子的分布系数值表明,Lewatit CNP 80对Ni〜(2 +),Cu〜(2+)的选择性高于对Cd〜的选择性。 (2 +),Zn〜(2+)和Pb〜(2+)。 Langmuir等温线适用于离子交换过程,并计算了其含量。离子交换树脂对金属离子的吸收是可逆的,因此具有去除Pb〜(2 +),Cu〜(2 +),Zn〜(2 +),Cd〜(2+),和水溶液中的Ni〜(2+)。对于Pb〜(2 +),Cu〜(2 +),Zn〜(2+),每克干树脂吸附金属离子的量计算为每克干树脂4.1、4.6、4.7、4.8和4.7mequiv。 Cd〜(2+)和Ni〜(2+)。 Cd〜(2+)> Pb〜(2+)> Cu〜(2+)> Ni〜(2+)> Zn〜(2+)选择性增加。所得结果表明,Lewatit CNP 80弱酸性树脂在去除金属方面表现出比Lewatit TP 207树脂更好的性能。溶液离子强度的变化对Pb〜(2 +),Cu〜(2 +),Zn〜(2 +),Cd〜(2+)和Ni〜(2)的去除影响很小+)。低离子强度或低浓度NaNC> 3的存在对树脂对这些金属的离子交换没有显着影响。我们得出的结论是,Lewatit CNP 80可用于有效去除Pb〜(2 +),Cu〜(2 +),Zn〜(2 +),Cd〜(2+)和Ni〜(2+)。水溶液。

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