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Kinetics Of Mn(II) Extraction By D2EHPA

机译:D2EHPA萃取Mn(II)的动力学

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The kinetics of forward extraction of Mn(II) from 0.1 M SO_4~= medium by D2EHPA solution in kerosene have been investigated by the Lewis and Hahn cell techniques. For kinetic data treatment both pseudo - rate constant, 'q' or 'rate/area' and flux, 'F' methods have been applied. The empirical rate equations have been derived. Results have been compared among themselves and other published works on Mn(II) - D2EHPA systems. The rate constants obtained from the 'q' and 'F' methods differ in magnitude and unit and an explanation on this has been given. An analysis of the rate equations obtained from the Lewis cell technique suggests that the reaction: Mn~(2+)+ HA~-_(2(I)) → [Mn(HA_2)]~+_((I)) occuring at the interface is the slowest. High activation energy, E_a in the lower temperature region (53 kJ/mol) supports the above mechanism. But the low E_a value in the higher temperature region (10 kJ/mol) suggests a diffusion control reaction at the interface. In the Hahn cell experiments, E_a never exceeds 12 kJ/mol and so the process is entirely diffusion controlled in this cell at any temperature. The rate constant obtained from the Lewis and Hahn cell techniques using either 'F' or 'q' method differ widely (k_(L.C.) = 100 k_(H.C.)) and an explanation has been given.
机译:用路易斯和哈恩电池技术研究了D2EHPA溶液在煤油中从0.1 M SO_4〜=介质中正萃取Mn(II)的动力学。对于动力学数据处理,伪速率常数“ q”或“速率/面积”以及通量,“ F”方法均已应用。得出了经验率方程。他们之间以及与其他有关Mn(II)-D2EHPA系统的已发表著作进行了比较。从“ q”和“ F”方法获得的速率常数在大小和单位上有所不同,并对此进行了解释。对通过路易斯电池技术获得的速率方程的分析表明,反应发生:Mn〜(2 +)+ HA〜-_(2(I))→[Mn(HA_2)]〜+ _((I))在界面上最慢。在较低温度区域(53 kJ / mol)的高活化能E_a支持上述机制。但是在较高温度区域(10 kJ / mol)中较低的E_a值表明在界面处有扩散控制反应。在Hahn电池实验中,E_a从未超过12 kJ / mol,因此该过程在任何温度下都完全受控于该电池中的扩散。从路易斯和哈恩电池技术使用“ F”或“ q”方法获得的速率常数相差很大(k_(L.C。)= 100 k_(H.C。)),并给出了解释。

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