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从氯化介质中用过的催化剂中用强碱性阴离子交换树脂回收铂、锡和铟。

Recovery of platinum, tin and indium from spent catalysts in chloride medium using strong basic anion exchange resins.

机构信息

Analytical Chemistry Department, Institute of Chemistry, Federal University of Rio de Janeiro, Av Athos da Silveira Ramos, 149 room A509, 21941-909 Ilha do Fundão, Rio de Janeiro, Brazil.

出版信息

J Hazard Mater. 2011 Sep 15;192(3):1155-60. doi: 10.1016/j.jhazmat.2011.06.021. Epub 2011 Jul 8.

DOI:10.1016/j.jhazmat.2011.06.021
PMID:21784579
Abstract

This work describes a route for platinum recovery from spent commercial Pt and PtSnIn/Al(2)O(3) catalysts using strong basic mesoporous and macroporous anion exchange resins (Cl(-) form). The catalysts were leached with aqua regia (75 °C, 20-25 min). Platinum adsorption was influenced by the presence of other metals which form chlorocomplexes (tin, indium) and also base metals (aluminum). However, it was possible to overcome this fact by a sequential desorption procedure. Aluminum was selectively removed from the resins by elution with 3 mol L(-1) HCl. Platinum was desorbed passing 1 mol L(-1) Na(2)S(2)O(3) (pH 9). Tin was removed by elution with 0.1 mol L(-1) ascorbic acid. Indium was removed using 0.1 mol L(-1) EDTA as eluent. Desorption efficiency exceeded 99% for all metals. Metals were recovered in high yields (>98 wt%).

摘要

本工作描述了一种从废商用 Pt 和 PtSnIn/Al(2)O(3)催化剂中回收铂的方法,使用强碱性中孔和大孔阴离子交换树脂(Cl(-)形式)。催化剂用王水(75°C,20-25 分钟)浸出。铂的吸附受形成氯络合物的其他金属(锡、铟)和基础金属(铝)的存在影响。然而,通过顺序解吸程序可以克服这一事实。铝通过用 3 mol L(-1) HCl 洗脱从树脂中选择性去除。铂通过用 1 mol L(-1) Na(2)S(2)O(3)(pH 9)洗脱解吸。锡通过用 0.1 mol L(-1)抗坏血酸洗脱去除。铟用 0.1 mol L(-1) EDTA 作为洗脱剂洗脱。所有金属的解吸效率均超过 99%。金属以高收率(>98wt%)回收。

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