Recovery of Pt, Pd, and Rh from spent automotive catalysts through combined chloride leaching and ion exchange: A review

IF 4.8 2区 材料科学 Q1 METALLURGY & METALLURGICAL ENGINEERING
Mostafa Hosseinzadeh, Jochen Petersen
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引用次数: 0

Abstract

Three platinum group metals (PGMs), platinum (Pt), palladium (Pd), and rhodium (Rh), are key components in automotive catalytic convertors, playing a pivotal role in controlling harmful emissions. The recycling and recovery of Pt, Pd, and Rh from spent automotive catalysts (SACs) have gained increasing attention as essential measures to mitigate resource depletion, supply risks, and environmental impacts. Due to the growing demand for automobiles and increasingly stricter environmental regulations, a substantial amount of spent automotive catalysts is generated annually, leading to increased interest in their efficient recycling and recovery of the PGMs they contain. Hydrometallurgical processes, particularly chloride leaching and ion exchange, have emerged as promising methods for efficient PGM extraction and separation from these discarded catalysts.

This review includes a critical examination of recent advances and innovations in both chloride leaching and ion exchange methods, highlighting their effectiveness in terms of Pt, Pd, and Rh recyclability and recovery efficiency from spent catalysts. The study offers valuable insights into the efficacy of their recycling from SACs through various processes. The importance of investigating the solution chemistry of PGMs in chloride media is highlighted and the leaching of SACs has been explored using various chloride media, including AlCl3, NaCl, CaCl2, MgCl, and NH4Cl, alongside a range of inorganic and organic leaching agents such as HCl, H2SO4, HNO3, acetic acid, citric acid, and oxidizing agents like H2O2, NaClO, NaClO3, Fe3+, Cl2, and Cu2+. This work is critically reviewed, examining the influence of key parameters investigated on the leaching efficiency of PGMs, such as HCl, Cl, and oxidizing concentrations, temperature, solid-to-liquid ratio (S/L), particle size, and leaching time. Furthermore, it evaluates the effectiveness of pretreatment techniques such as calcination, salt roasting, and pre-reduction methods involving high temperatures, hydrogen gas flow, formic acid, hydrazine hydrate, and Zn-vapor treatments. The review then turns to the efficacy of the ion exchange method, utilizing a diverse range of anion exchange resins for the selective adsorption of PGMs as well as various elution reagents for the selective desorption of PGMs from loaded resins, aiming to recover them selectively from chloride leach solutions. Therefore, this study seeks to contribute to the development of strategies for recycling and reusing PGMs from SACs, with a view to reducing the industry's dependence on primary raw materials and promoting principles of the circular economy.

通过氯化物浸出和离子交换相结合的方法从废汽车催化剂中回收铂、钯和铑:综述
铂(Pt)、钯(Pd)和铑(Rh)这三种铂族金属(PGM)是汽车催化转化器的关键成分,在控制有害气体排放方面发挥着举足轻重的作用。作为缓解资源枯竭、供应风险和环境影响的重要措施,从废旧汽车催化剂(SAC)中回收铂、钯和铑的工作日益受到关注。由于对汽车需求的不断增长和日益严格的环保法规,每年都会产生大量的废汽车催化剂,因此人们对其有效回收利用和回收其中所含的 PGM 越来越感兴趣。水冶工艺,尤其是氯化浸出和离子交换,已成为从这些废弃催化剂中高效提取和分离 PGM 的有前途的方法。本综述对氯化浸出和离子交换方法的最新进展和创新进行了严格审查,重点介绍了它们在铂金、钯金和铑的可回收性以及从废催化剂中回收效率方面的有效性。这项研究为通过各种工艺从 SACs 中回收铂、钯和铑的有效性提供了宝贵的见解。研究强调了研究 PGM 在氯化物介质中的溶液化学性质的重要性,并使用各种氯化物介质(包括 AlCl3、NaCl、CaCl2、MgCl 和 NH4Cl)以及一系列无机和有机浸出剂(如 HCl、H2SO4、HNO3、醋酸、柠檬酸)和氧化剂(如 H2O2、NaClO、NaClO3、Fe3+、Cl2 和 Cu2+)探索了 SAC 的浸出过程。对这项工作进行了批判性回顾,研究了所调查的关键参数对 PGMs 浸出效率的影响,如 HCl、Cl- 和氧化剂浓度、温度、固液比 (S/L)、粒度和浸出时间。此外,它还评估了煅烧、盐焙烧等预处理技术以及涉及高温、氢气流、甲酸、水合肼和锌蒸汽处理的预还原方法的有效性。随后,我们将讨论离子交换法的功效,利用各种阴离子交换树脂选择性地吸附 PGMs,并使用各种洗脱试剂选择性地解吸负载树脂中的 PGMs,从而从氯化物浸出液中选择性地回收 PGMs。因此,本研究旨在为制定从 SAC 中回收和再利用 PGM 的战略做出贡献,以减少该行业对初级原材料的依赖,促进循环经济原则。
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来源期刊
Hydrometallurgy
Hydrometallurgy 工程技术-冶金工程
CiteScore
9.50
自引率
6.40%
发文量
144
审稿时长
3.4 months
期刊介绍: Hydrometallurgy aims to compile studies on novel processes, process design, chemistry, modelling, control, economics and interfaces between unit operations, and to provide a forum for discussions on case histories and operational difficulties. Topics covered include: leaching of metal values by chemical reagents or bacterial action at ambient or elevated pressures and temperatures; separation of solids from leach liquors; removal of impurities and recovery of metal values by precipitation, ion exchange, solvent extraction, gaseous reduction, cementation, electro-winning and electro-refining; pre-treatment of ores by roasting or chemical treatments such as halogenation or reduction; recycling of reagents and treatment of effluents.
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