Preparation method of high-activity hydrodemetalization catalyst for residuum
A technology for hydrogenation and demetallization of residual oil, which is applied in the direction of catalyst activation/preparation, metal/metal oxide/metal hydroxide catalysts, chemical instruments and methods, etc., can solve the problems of unsatisfactory mechanical strength of catalysts, and achieve easy Effects of vulcanization, desulfurization activity improvement, and demetallization activity improvement
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example 1
[0023] Weigh 100 grams of the above-mentioned self-made clover-shaped alumina (water content 25%) and transfer it to the polytetrafluoroethylene lining of the autoclave, add 150 ml of aqueous solution containing 228 grams of xylitol to it, and make the alcohol and Al 3+ The molar ratio is 1:1, impregnated for 60 minutes, the autoclave is sealed and transferred to an oven at 150°C, heat treated under autogenous pressure for 9 hours, and naturally cooled to room temperature. The alumina carrier after hydrothermal treatment was dried at 120° C. for 3 hours. Use 150ml with MoO 3 105 grams, 15 grams of NiO impregnating solution impregnated the above-mentioned carrier for 3 hours, filtered off the excess solution, and dried at 110°C for 8 hours. Baking at 350°C for 2 hours. The residue hydrodemetallization catalyst C1 of the present invention was prepared.
example 2
[0025] With example 1, just alumina support is dissolved with the aqueous solution impregnation of 136.5 gram sorbitols with 150ml, makes alcohol and Al 3+ The mole ratio is 0.5:1, immersion for 80 minutes, heat treatment temperature is 200°C, and treatment time is 6 hours to obtain residue hydrodemetallization catalyst C2 of the present invention.
example 3
[0027] Same as Example 1, except that the alumina carrier is impregnated with 81.9 grams of mannitol in 150ml of aqueous solution, so that alcohol and Al 3+ The mole ratio is 0.3:1, the impregnation is 90 minutes, the temperature during heat treatment is 175°C, and the treatment time is 12 hours to obtain the residual oil hydrodemetallation catalyst C3 of the present invention.
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