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Oxidative leaching process with cupric ion in hydrochloric acid mediafor recovery of Pd and Rh from spent catalytic converters

机译:盐酸介质中铜离子的氧化浸出工艺从废催化转化器中回收Pd和Rh

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摘要

The recycling of platinum-group metals from wastes such as autocatalytic converters is getting growing attention due to the scarcity of these precious metals and the market pressure originated by increase of demand in current and emerging applications. Hydrometallurgical treatment of such wastes is an alternative way to the most usual pyrometallurgical processes based on smelter operations. This paper focuses on the development of a leaching process using cupric chloride as oxidising agent, in HCl media, for recovery of palladium and rhodium from a spent catalyst. The chloride media allows the adequate conditions for oxidising and solubilising the metals, as demonstrated by equilibrium calculations based on thermodynamic data. The experimental study of the leaching process revealed that Pd solubilisation is clearly easier than that of Rh. The factors temperature, time, and HCl and Cu2+ concentrations were significant regarding Pd and Rh leaching, the latter requiring higher factor values to achieve the same results. Leaching yields of 95% Pd and 86% Rh were achieved under optimised conditions (T = 80.C, t = 4 h,[HCl] = 6 M, [Cu2+] = 0.3 M).
机译:由于这些贵金属的稀缺以及当前和新兴应用需求的增长所带来的市场压力,从诸如自动催化转化器之类的废物中回收铂族金属越来越受到关注。对此类废物进行湿法冶金处理是基于冶炼厂操作的最常用火法冶金工艺的替代方法。本文着重于开发一种在HCl介质中使用氯化铜作为氧化剂的浸出工艺的方法,用于从废催化剂中回收钯和铑。氯化物介质为氧化和溶解金属提供了适当的条件,这是基于热力学数据进行的平衡计算所证明的。浸出过程的实验研究表明,钯的溶解明显比Rh容易。温度,时间以及HCl和Cu2 +浓度的因素对于Pd和Rh浸出而言均很重要,后者需要较高的因子值才能达到相同的结果。在最佳条件下(T = 80.C,t = 4 h,[HCl] = 6 M,[Cu2 +] = 0.3 M),浸出率达到95%Pd和86%Rh。

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