A kind of completely deactivated hydrocracking catalyst recovery and reuse method
A hydrocracking and catalyst technology, applied in the direction of catalyst regeneration/reactivation, physical/chemical process catalyst, molecular sieve catalyst, etc., can solve the problems of high pollution and low recovery rate, and achieve simple process, environmental protection and recycling. Effect
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Embodiment 1
[0026] Take the FC-12 flexible hydrocracking catalyst (regenerated twice, with a total service life of 9 years) that has completed the industrial operation life cycle, grind it into powder, and sieve it with a 200 standard sieve. Then the catalyst powder was placed in a muffle furnace, and nitrogen-oxygen mixed gas with an oxygen content of 2.5% was passed into the muffle furnace, and calcined at 460°C for 6h. Put 200g of calcined powder into a dilute nitric acid solution with a concentration of 1.0mol / L for beating at a temperature of 65°C for 60 minutes; add 200g of macroporous alumina (pore volume 0.83mL / g, specific surface area 330m 2 / g), 80g modified Y-type molecular sieve-1 (unit cell constant 2.440nm, crystallinity 90%), 90g tungstic acid, 82g nickel nitrate, 12g dimethylglyoxime, and a small amount of squid powder etc. Squeeze paste paste, extrude into a cylindrical shape with a diameter of 1.5mm. Then, it was dried at 120°C for 4 hours and calcined at 480°C for 3 ho...
Embodiment 2
[0028] The chelating agent in the example 1 is changed into dithizone, the addition is 10g, the metal component is added into the impregnation method by the kneading method, the catalyst is impregnated with the metal, dried at 120°C for 4 hours, and roasted at 480°C for 3 hours, The obtained catalyst number is LH22-2.
Embodiment 3
[0030] The catalyst molding material in the example 1 is changed to the powder after the roasting of 200g certain high and medium type hydrocracking catalyst D-39, 48g modified Y molecular sieve-2 (unit cell constant 24.30, crystallinity 95%), 160g amorphous silicon aluminum ( The silica content is 45%, the pore volume is 0.76mL / g, and the specific surface area is 291m 2 / g), 82g of macroporous alumina, 90g of tungstic acid, 82g of nickel nitrate, 10g of acetylacetone added, other preparation methods are the same as in Example 1, and the obtained catalyst number is RD39-1.
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