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用离子交换树脂 Diaion WA21J 从氯化废汽车催化剂浸出得到的氯化溶液中吸附 Pd(II) 络合物。

Adsorption of Pd(II) complexes from chloride solutions obtained by leaching chlorinated spent automotive catalysts on ion exchange resin Diaion WA21J.

机构信息

Key Laboratory of Ecological and Recycling Metallurgy, Ministry of Education of China, Beijing 100083, China.

出版信息

J Colloid Interface Sci. 2010 May 1;345(1):12-8. doi: 10.1016/j.jcis.2010.01.049. Epub 2010 Jan 25.

Abstract

It was found that Rh, Pd and Pt contained in the spent ceramic automotive catalysts could be effectively extracted by dry chlorination with chlorine. In order to concentrate Pd(II) contained in the chloride solution obtained from the dry chlorination process, thermodynamic and kinetics studies for adsorption of Pd(II) complexes from the chloride solutions on anionic exchange resin Diaion WA21J were carried out. It was found that Pd, Pt, Rh, Al, Fe, Si, Zn and Pb from the chloride solution could be adsorbed on the resin. The isothermal adsorption of Pd(II) was found to fit Freundlich, Langmuir and Dubinin-Kaganer-Radushkevich models under the adsorption conditions. The adsorption of Pd(II) on the resin was favorable according to the values of 1/n and R(L) from Freundlich and Langmuir adsorption isotherms, respectively. The maximum monolayer adsorption capacities Q(max) based on Langmuir adsorption isotherms were 5.70, 4.84 and 4.05 mg/g and the corresponding value X(m) based on Dubinin-Kaganer-Radushkevich were 5.55, 4.69 and 4.01 mg/g at temperatures 18 degrees C, 28 degrees C and 40 degrees C, respectively. The apparent adsorption energies (E(ad)) based on Dubinin-Kaganer-Radushkevich isotherm were -15.43, -16.22 and -23.57 kJ/mol for the temperatures 18 degrees C, 28 degrees C and 40 degrees C, respectively. Chemical adsorption was a main mechanism involved in the adsorption process. Pd(II) adsorption on the resin could be accelerated by increasing the adsorption temperature. The adsorption of Pd(II) from the chloride solution on the resin underwent pseudo-first order kinetic process and the apparent adsorption activation energy E(a) was 15.0 kJ/mol. The intra-particle diffusion was a main rate controlling step in the Pd(II) adsorption process under the adsorption conditions.

摘要

研究发现,用氯气进行干法氯化可以有效地从废陶瓷汽车催化剂中提取铑、钯和铂。为了浓缩从干法氯化过程中获得的氯化溶液中所含的钯(II),对从氯化溶液中吸附钯(II)络合物到阴离子交换树脂 Diaion WA21J 的热力学和动力学进行了研究。结果表明,从氯化溶液中可以吸附钯、铂、铑、铝、铁、硅、锌和铅。在吸附条件下,发现 Pd(II)的等温吸附符合 Freundlich、Langmuir 和 Dubinin-Kaganer-Radushkevich 模型。根据 Freundlich 和 Langmuir 吸附等温线的 1/n 和 R(L)值,钯(II)在树脂上的吸附是有利的。基于 Langmuir 吸附等温线的最大单层吸附容量 Q(max)分别为 5.70、4.84 和 4.05mg/g,基于 Dubinin-Kaganer-Radushkevich 的相应值 X(m)分别为 5.55、4.69 和 4.01mg/g,温度分别为 18°C、28°C 和 40°C。基于 Dubinin-Kaganer-Radushkevich 等温线的表观吸附能(E(ad))分别为-15.43、-16.22 和-23.57kJ/mol,温度分别为 18°C、28°C 和 40°C。化学吸附是吸附过程中的主要机制。升高吸附温度可以加速钯(II)在树脂上的吸附。从氯化溶液中吸附钯(II)到树脂上的过程符合准一级动力学过程,表观吸附活化能 E(a)为 15.0kJ/mol。在吸附条件下,钯(II)吸附过程的内扩散是主要的速率控制步骤。

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