Method for separating enriched palladium from waste Pd/Al2O3 catalyst chloride leaching solution
A technology of chlorination leaching, separation and enrichment, applied in the field of separation and enrichment of palladium, which can solve the problems of difficult filtration, interference of impurity ions, and difficult control of the end point, and achieve the effects of high precipitation efficiency, broad application prospects, and rapid reaction process
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Embodiment 1
[0022] Example 1: Add NaOH solution to adjust the pH of the leaching solution to 11.0, and continue to add Na 2 The pH of the S solution is controlled to be 12.0, and the molar ratio of the amount of sodium sulfide to the content of palladium is 1. At this time, the whole solution system is black and fine-grained, and there is no bubble generation and no hydrogen sulfide smell in the whole process. Let it stand for 3 minutes, and the solution is separated. , the upper layer is clear and transparent, and the lower layer is tightly black precipitated, and the precipitate is separated by filtration and washed with 1.0 mol / L hydrochloric acid. Finally, the recovery rate of palladium was 88.65%, and the purity was 75%.
Embodiment 2
[0023] Embodiment 2: Add NaOH solution to adjust the pH of the leaching solution to 11.0, and continue to add Na 2 The pH of the S solution is controlled to be 12.5 to stop, and the amount of sodium sulfide is such that the molar ratio of the palladium content is 1.5. At this time, the whole solution system is black and fine-grained, and there is no bubble generation and no hydrogen sulfide smell in the whole process. Let it stand for 3 minutes, and the solution is separated. , the upper layer is clear and transparent, and the lower layer is tightly black precipitated, and the precipitate is separated by filtration and washed with 1.0 mol / L hydrochloric acid. Finally, the recovery rate of palladium was 100%, and the purity was 95%.
Embodiment 3
[0024] Embodiment 3: Add NaOH solution to adjust the pH of the leaching solution to 11.5, and continue to add Na 2 The pH of the S solution is controlled to be 12.5, and the molar ratio of the amount of sodium sulfide to the content of palladium is 1.2. At this time, the whole solution system is black and fine-grained, and there is no bubble generation and no hydrogen sulfide smell in the whole process. Let it stand for 3 minutes, and the solution is separated. , the upper layer is clear and transparent, and the lower layer is tightly black precipitated, and the precipitate is separated by filtration and washed with 1.0 mol / L hydrochloric acid. Finally, the recovery rate of palladium was 98.18%, and the purity was 92%.
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