Wet recovery method and device for oil-containing waste catalyst
A technology of waste catalyst and recovery method, which is applied in the direction of improvement of process efficiency, photographic process, instruments, etc., and can solve the problems of poor utilization of organic hydrocarbons, long deoiling or sodium roasting time, and harmful gas hazards Environmental problems, to avoid low current efficiency, simple liquid and solid phase components, and reduce extraction time
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Embodiment 1
[0050] The mass percentage of oil components in a spent catalyst for desulfurization and hydrogenation is 12%, and the contents of vanadium, nickel, molybdenum, cobalt, aluminum, and sulfur are 5.4%, 3.3%, 0.9%, 1.2%, 27.3%, and 8.3%, respectively. The content of other metals is less; the content of oil compounds and sulfur in the catalyst is more. Adopt the device in the embodiment of the present invention, use 5% sulfuric acid solution as the acidic electrolyte aqueous solution, input voltage, positive and negative potential difference is 3V, vanadium, nickel, cobalt can be soaked, after room temperature electrochemical reaction separation 120min, obtain 98% oil The molybdenum compounds are collected in the oil collection tank, and more than 90% of the molybdenum compounds and S are enriched in the hydrophobic inorganic particles in the form of simple substances, and the recovery rates of vanadium, nickel, cobalt, and aluminum deposited by the cathode are all above 98%.
Embodiment 2
[0052] Waste aluminum-based platinum palladium catalyst, which contains 2.5% oil. Using the device in the embodiment of the present invention, using 3.5% hydrochloric acid as the acidic electrolyte solution, the input voltage, the potential difference between the anode and the anode is 2V, electrochemically dissolving in the electrochemical reaction chamber, selectively removing oil and leaching the cathode to deposit platinum palladium, The extraction rate of platinum and palladium is more than 99%, while the leaching rate of aluminum is less than 20%. The remaining high-alumina products are discharged as leaching residue and used as high-purity alumina raw materials. The recovery rate of oil compounds reaches 95%.
Embodiment 3
[0054]For the spent SCR catalyst, the oil component is 4.5%. Adopt the device in the embodiment of the present invention, use 5% nitric acid as the acidic electrolyte aqueous solution, under 40 ℃, input voltage, the potential difference of cathode and anode is 1.5V, carry out electrochemical catalytic leaching, the recovery rate of vanadium and nickel reaches more than 97% , The recovery rate of oil compounds is above 96%.
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