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Recovery of Platinum from Chloride Leaching Solutions of Spent Reforming Catalysts by Ion Exchange

机译:离子交换从废重整催化剂的氯化浸出液中回收铂

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Platinum and base metals (Al, Fe, Si) are present in the chloride leaching solutions of spent reforming catalysts. In order to develop a process to recover platinum from such leaching solutions, batch and continuous ion exchange experiments were performed using a strong anionic resin (DiaionSA10AP). The adsorption equilibrium data of Pt are described by the Langmuir adsorption isotherm. Batch experiments indicate that it is possible to separate Pt and Fe from other metal ions in the present leaching solution. Fe was selectively removed from the loaded resin using diluted HCl, while Pt was eluted using thiourea after Fe removal. The results of column experiments verified the feasibility of the separation and recovery of platinum from leaching solutions using the present process. The elution efficiency exceeded 99% for both Pt and Fe. The recovery percentage of Pt from the leaching solution using this method was 99.3%.
机译:废重整催化剂的氯化物浸出溶液中存在铂和贱金属(Al,Fe,Si)。为了开发一种从这种浸提液中回收铂的方法,使用强阴离子树脂(DiaionSA10AP)进行了分批和连续的离子交换实验。 Pt的吸附平衡数据由Langmuir吸附等温线描述。分批实验表明,可以在本浸出溶液中将Pt和Fe与其他金属离子分离。用稀盐酸选择性地从负载的树脂中除去铁,而除去铁后,用硫脲洗脱铂。柱实验的结果证实了使用本方法从浸出溶液中分离和回收铂的可行性。 Pt和Fe的洗脱效率均超过99%。使用该方法从浸出液中回收的Pt为99.3%。

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