Recovery of platinum from diesel catalysts by combined use of H2O2/HCl leaching and adsorption

被引:21
作者
Trucillo, Paolo [1 ]
Lancia, Amedeo [1 ]
Di Natale, Francesco [1 ]
机构
[1] Univ Naples Federico II, Dept Chem, Mat & Ind Prod Engn, Piazzale V Tecchio 80, I-80125 Naples, Italy
来源
JOURNAL OF ENVIRONMENTAL CHEMICAL ENGINEERING | 2022年 / 10卷 / 03期
关键词
Waste catalysts management; Platinum group metals; Leaching; Adsorption; SPENT PETROLEUM CATALYSTS; PRECIOUS-METAL RECOVERY; PRINTED-CIRCUIT BOARDS; MUNICIPAL SOLID-WASTE; ACTIVATED CARBON; AQUEOUS-SOLUTIONS; HYDROGEN-PEROXIDE; PALLADIUM; IONS; OXIDATION;
D O I
10.1016/j.jece.2022.107730
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
Spent automotive catalysts are industrial non-hazardous wastes of high added values because of the presence of platinum group metals, whose recovery is gaining increasing attention in European countries. This paper pro -poses a hydrometallurgical process to recover platinum from diesel catalysts, based on a first leaching step with aqueous solutions of H2O2 (up to 0.2 M) and mild HCl concentrations (0.4 M), followed by a refining step in which platinum is deposited over a granular activated carbon. Tests were carried out at different H2O2 content, temperatures, and sizes of granulated catalyst. The use of H2O2 and low HCl content allows higher sustainability than conventional hydrometallurgical processes by reducing safety risks associated with the use of concentrated HCl and the emissions of NOx deriving from the use of nitrogen species in conventional leaching. Besides, the use of an adsorbent avoids the utilization of cyanides or other toxic organic solvents for the refining of the leaching solution. Experiments revealed that the low HCl concentration results in longer leaching times; however, process conditions can be tuned to completely recover platinum with negligible extraction of other metals on the catalyst, minimizing on the subsequent adsorption process. Optimal conditions appear as leaching at 20 ? with a 0.13 M H2O2 0.4 M HCl solution followed by an adsorption step at 20 C using an activated carbon with high BET surface area and high content of reducing surface groups. These findings suggest that the proposed recovery process can be a suitable candidate for future technology implementations.
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页数:11
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