High-activity hydrodemetallization catalyst and preparation method thereof
A hydrodemetallization and catalyst technology, applied in the direction of metal/metal oxide/metal hydroxide catalysts, chemical instruments and methods, physical/chemical process catalysts, etc., can solve the problem of pore volume, specific surface area reduction, macropore collapse and sintering, mechanical strength deterioration and other problems, to achieve the effect of appropriate pore distribution, large pore volume, and prevention of collapse and sintering
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example 1
[0024] (1) Weigh 100g of pseudo-boehmite dry rubber powder (manufactured by Shenyang Catalyst Factory, with an alumina dry basis content of 65%), add 2g of asparagus powder, 3g of carbon black powder and mix well, dissolve 1.5g of phosphoric acid in 80mL of distilled water In the process, mix the obtained solution with the above materials evenly, extrude it into a clover-shaped strip with a diameter of 1.8mm on a screw extruder, and dry it at 120°C for 3 hours. Nitrogen purging at ℃ for 0.75 hours, calcined at 600°C for 4 hours under the condition of nitrogen protection, then stop the nitrogen protection and feed air, calcined at 600°C for 1 hour to prepare alumina carrier. (2) Weigh 100 grams of the above-mentioned alumina carrier, add 150ml Mo-Ni-NH 3 solution (with MoO 3 10.0wt%, NiO3.0 wt%) impregnated for 2 hours, filtered off excess solution, dried at 120°C for 2 hours, and then calcined at 550°C for 5 hours to obtain the hydrodemetallization catalyst C1 of the present ...
example 2
[0026] Same as example 1, except that the addition of carbon black powder is 5g, the addition of phosphoric acid is 1g, the molded product after drying is placed in a tube-type high-temperature furnace, purged with nitrogen for 1 hour at 100°C, and under the condition of nitrogen protection Calcined at 700°C for 3 hours, then stopped the nitrogen protection and introduced air, and calcined at 650°C for 1 hour to prepare an alumina carrier. Using the alumina as a carrier, the same method as in Example 1 was used to prepare the hydrodemetallization catalyst C2 of the present invention. Catalyst properties are listed in Table 1.
example 3
[0028] Same as Example 1, except that the addition of carbon black powder is 8g, the addition of phosphoric acid is 0.5g, the molded product after drying is placed in a tube-type high-temperature furnace, and nitrogen is purged for 0.5 hours at 200°C, and the condition of nitrogen protection Calcined at 800°C for 3 hours, then stopped the nitrogen protection and fed air, and calcined at 700°C for 1 hour to prepare an alumina carrier. Using the alumina as a carrier, the same method as in Example 1 was used to prepare the hydrodemetallization catalyst C3 of the present invention. Catalyst properties are listed in Table 1.
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