Mutual Separation of Palladium (II) and Platinum (IV) from Hydrochloric Acid Solutions Using m-Phenylene Diamine-Containing Agents

Kazuya Matsumoto, Sumito Yamakawa, Tatsuya Aoyagi, Kazutoshi Haga, M. Jikei, A. Shibayama
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引用次数: 2

Abstract

Platinum group metals (PGMs), especially Pd and Pt, are important industrial elements owing to their extensive use in electrical devices, dental materials, catalysts, and jewelry [1,2]. Given the scarcity of the PGMs primary resources, the recycling of these metals from secondary sources or post-consumer scrap is essential [3]. Solvent extraction is regarded as a typical and practical method to recover PGM ions [4-8]. For example, Pd(II) and Pt(IV) can be extracted from hydrochloric acid (HCl) solutions with di-n-octyl sulfide [9] and tri-n-butyl phosphate [10] extractant agents, respectively. However, the use of volatile organic solvents as extractant diluents negatively affects the recovery process owing to their toxicity and environmental load. Mutual separation of PGMs, which is required in the recovery process, is complicated because of the similar physical and chemical properties of the metal components. PGM ions are known to be recovered via coordination or ion-pair mechanisms [11]. Pd and Pt are typically recovered following a coordination mechanism with the trend Pd(II) >> Pt(IV) [12]. On the other hand, Pd and Pt chloro-complex anions (i.e., [PdCl4] 2and [PtCl6] ) were extracted to a similar extent via an ion-pair mechanism [11,13]. Therefore, mutual separation of Pd and Pt is generally performed by combining coordination and ion-pair recovery strategies, respectively. However, the utilization of different mechanisms within the recovery process requires several recovery agents specially designed for the corresponding recovery mechanism. In addition, the recovery of PGMs via a coordination mechanism is typically accompanied with base metals such as Cu, Fe, Al, and Zn [12]. In this study, we report on the selective precipitation and mutual separation of Pd and Pt using new precipitating agents (i.e., m-phenylene diamine-containing compounds). These precipitating agents were prepared by condensation of aniline or 4-phenoxyaniline with 3,5-bis(trifluoroacetamido)benzoyl chloride followed by deprotection with hydrazine. The precipitation behaviors of Pd and Pt with the as-prepared precipitating agents were examined by using Pdand Pt-containing HCl solutions with or without base metals. The precipitating agents prepared in this study enabled mutual separation of Pd and Pt from a HCl solution containing base metals via an ion-pair mechanism.
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含间苯二胺剂对盐酸溶液中钯(II)和铂(IV)的相互分离
铂族金属(铂族金属),特别是钯和铂,是重要的工业元素,广泛应用于电气器件、牙科材料、催化剂和珠宝[1,2]。鉴于铂基金属初级资源的稀缺性,从次级来源或消费后废料中回收这些金属至关重要。溶剂萃取被认为是回收PGM离子的一种典型而实用的方法[4-8]。例如,Pd(II)和Pt(IV)可以分别用二正辛酯硫化物[9]和磷酸三正丁酯[10]萃取剂从盐酸(HCl)溶液中萃取。然而,使用挥发性有机溶剂作为萃取剂稀释剂,由于其毒性和环境负荷对回收过程产生负面影响。由于金属组分的物理和化学性质相似,回收过程中需要对PGMs进行相互分离,这是复杂的。已知PGM离子可通过配位或离子对机制回收[11]。Pd和Pt的恢复通常遵循Pd(II) >> Pt(IV)[12]趋势的协调机制。另一方面,Pd和Pt氯络合物阴离子(即[PdCl4] 2和[PtCl6])通过离子对机制被提取到类似的程度[11,13]。因此,Pd和Pt的相互分离通常分别采用配位策略和离子对恢复策略相结合的方式进行。但是,在恢复过程中使用不同的机制,需要针对相应的恢复机制专门设计几种恢复代理。此外,通过配位机制回收的PGMs通常伴随着贱金属,如Cu, Fe, Al和Zn[12]。在这项研究中,我们报道了使用新的沉淀剂(即含间苯二胺的化合物)选择性沉淀和相互分离Pd和Pt。这些沉淀剂是由苯胺或4-苯氧苯胺与3,5-二(三氟乙酰胺)苯甲酰氯缩合制备的,然后用肼脱保护。用含钯和不含贱金属的HCl溶液考察了钯和铂在沉淀剂中的析出行为。本研究制备的沉淀剂通过离子对机制使Pd和Pt从含贱金属的HCl溶液中相互分离。
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