Method for recovering ruthenium catalyst carried by active carbon
A technology of ruthenium catalyst and recovery method, which is applied in chemical recovery, chemical instruments and methods, catalyst regeneration/reactivation, etc., to achieve the effects of improving economic and ecological benefits, reducing the consumption of heavy metal resources, and simple operation
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Embodiment 1
[0035] 24.0 g of spent ruthenium catalyst (containing Ba and K promoters) supported on activated carbon was soaked in 10% hydrochloric acid solution by mass percentage for 12 hours, and filtered to obtain filtrate and filter residue. Add appropriate amount of dilute sulfuric acid to the filtrate to make BaSO 4 The precipitation is complete, and BaSO is obtained by filtration and drying. 4 2.1423g, the Ba recovery rate is 87.8%; the remaining filtrate is evaporated to dryness to obtain KCl 4.8485g, and the K recovery rate is 77.7%.
[0036] Ruthenium recovery: the filter residue was calcined in a muffle furnace at 800°C for 10 hours to obtain 0.9882 g of a gray-black mixture. Mix the gray-black mixture with 2 g of KOH and KNO at a mass ratio of 1:1 3 The solid mixture was packed in a crucible and placed in a muffle furnace for alkali fusion at 650°C for 1 hour. After the alkali melt is cooled, it is washed with cold water to neutrality, and then filtered to obtain a filter ...
Embodiment 2
[0039] Activated carbon-supported ruthenium catalyst (containing Ba promoter) 20g was soaked with 10% dilute hydrochloric acid solution for 16 hours, and filtered to obtain filtrate and filter residue. Add appropriate amount of dilute sulfuric acid to the filtrate to make BaSO 4 The precipitation is complete, and BaSO is obtained by filtration and drying. 4 2.1737g, Ba recovery rate is 89.8%. Other operations are the same as the ruthenium recovery step in Example 1. The recovery rate of ruthenium was 93.05%.
Embodiment 3
[0041] Activated carbon-supported ruthenium catalyst (containing K promoter) 20g was soaked in 10% dilute hydrochloric acid solution by mass percentage for 6 hours, and filtered to obtain filtrate and filter residue. The filtrate was dried to obtain KCl4.5737g, and the K recovery rate was 81.8%. Other operations are the same as the ruthenium recovery step in Example 1. The recovery rate of ruthenium was 95.55%.
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