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RECOVERY OF PALLADIUM FROM SPENT Pd/Al_2O_3 CATALYST BY HYDROCHLORIC ACID LEACHING

机译:通过盐酸浸出回收来自Pd / Al_2O_3催化剂的钯

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Spent Pd/Al_2O_3 catalyst is an important secondary resource of palladium metals. The highly efficient recovery of palladium was hard to implement due to the wrapping of catalyst carriers, accumulating carbon on surface and existing as stable palladium oxide. An effective process for recovery of palladium was investigated. Samples were initially roasted to eliminate carbon. Then, the roasted mass was reduced with reductive agent for the purpose of transferring palladium oxide to palladium. The reduced residue was further leached using hydrochloric acid with -uitable oxidizing agent to recover palladium. The results showed that the palladium extraction only reached tol6.24% by direct leaching process and 43.51% by roasting-leaching process. However, it achieved 98.71% by roasting-reduction-leaching process under the appropriate teaching conditions of HCl 5M, NaClO_3 2.5g/L at 95° C for 2h.Additionally, the feasible conditions involved in roasting and reduction steps were also investigated.
机译:CDEN PD / AL_2O_3催化剂是钯金属的重要二级资源。由于催化剂载体的包裹,累积碳表面和现有的稳定亚氧化钯,钯的高效回收仍然是难以实施的。研究了钯的有效方法。最初烤样品以消除碳。然后,通过还原剂降低烘烤的质量,以便将氧化钯转移到钯。使用盐酸与盐酸具有含有盐酸的还原残余物以回收钯。结果表明,钯萃取仅通过直接浸出过程达到甲醛6.24%,通过焙烧浸出方法达到43.51%。然而,通过在HCl 5M的适当教学条件下通过焙烧还原浸出方法实现了98.71%,在95℃下进行2小时,也研究了焙烧和还原步骤的可行条件。

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