Hubicki Z, Wołowicz A, Leszczyńska M
Department of Inorganic Chemistry, Faculty of Chemistry, Maria Curie-Skłodowska University, Maria Curie-Skłodowska Square 2, 20-031 Lublin, Poland.
J Hazard Mater. 2008 Nov 30;159(2-3):280-6. doi: 10.1016/j.jhazmat.2008.02.017. Epub 2008 Feb 16.
Palladium and its compounds find wide application in industry as a catalytic agent in different manufacture processes. Recovery of precious metals from industrial wastes is difficult and time consuming but in spite of these disadvantages it becomes profitable. Palladium(II) ions sorption from various chloride solutions of the composition: 0.1-6.0M HCl-0.00056 M Pd(II), 1.0M ZnCl(2)-0.1M HCl-0.00056 M Pd(II), 1.0M AlCl(3)-0.1M HCl-0.00056 M Pd(II) on the weakly and strongly basic anion exchangers (Varion ATM, Varion ADM and Varion ADAM) was discussed. The sorption research of Pd(II) ions on these resins was carried out by means of static and dynamic methods. The dynamic processes were applied in order to determine the breakthrough curves of Pd(II) ions. Moreover, the working ion-exchange capacities as well as the weight and bed distribution coefficients were determined from the Pd(II) breakthrough curves. The recovery factors of Pd(II) ions (% R) depending on the phase contact time were obtained by means of static methods. The highest ion-exchange capacities for the 0.1-6.0M HCl-0.00056 M Pd(II) systems were obtained for the weakly basic ion-exchange resin Varion ADAM.
钯及其化合物作为不同制造过程中的催化剂在工业中有着广泛的应用。从工业废料中回收贵金属既困难又耗时,但尽管存在这些缺点,回收仍有利可图。本文讨论了在弱碱性和强碱性阴离子交换剂(Varion ATM、Varion ADM和Varion ADAM)上,从各种组成的氯化物溶液中吸附钯(II)离子的情况,这些溶液包括:0.1 - 6.0M HCl - 0.00056M Pd(II)、1.0M ZnCl₂ - 0.1M HCl - 0.00056M Pd(II)以及1.0M AlCl₃ - 0.1M HCl - 0.00056M Pd(II)。通过静态和动态方法对钯(II)离子在这些树脂上的吸附进行了研究。应用动态过程来确定钯(II)离子的穿透曲线。此外,根据钯(II)的穿透曲线确定了工作离子交换容量以及重量和床层分配系数。通过静态方法获得了取决于相接触时间的钯(II)离子回收因子(%R)。对于0.1 - 6.0M HCl - 0.00056M Pd(II)体系,弱碱性离子交换树脂Varion ADAM具有最高的离子交换容量。