Heavy oil hydrotreating method
A technology for hydrogenation and treatment of heavy oil, applied in refining to remove heteroatoms, etc., can solve problems such as deactivation of downstream catalysts
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Embodiment 1-1
[0034] The preparation of the alumina support for the hydrodemetallization catalyst used in the present invention and its preparation method are described.
[0035] Take by weighing the dry rubber powder (dry basis is 73% that Changling Refinery Catalyst Factory produces, and wherein pseudo-boehmite content is 68%, and gibbsite content is 5 weight %, and surplus is amorphous alumina) 1000 gram, 27 grams of sage powder (product of Henan Lankao tianjing rubber factory), 25g of hydroxymethyl cellulose mixes, then adds 1200 milliliters of aqueous solutions containing 24g of nitric acid, and extrudes into outer diameter φ 1.1mm on a plunger extruder. Butterfly strips. The wet strip was dried at 120° C. for 4 hours and calcined at 930° C. for 3 hours to obtain carrier 1-Z1. The physical and chemical properties of carrier 1-Z1 are shown in Table 1-1.
Embodiment 1-2
[0037] The preparation of the alumina support for the hydrodemetallization catalyst used in the present invention and its preparation method are described.
[0038] Take by weighing 1000 grams of dry rubber powder produced by Shanxi Aluminum Plant (the dry basis is 69%, wherein the pseudo-boehmite content is 71%, the gibbsite content is 6% by weight, and the balance is amorphous alumina) 1000 grams, 27 Ke Tianjing powder (product of Henan Lankao Tianjing Rubber Factory), 25g polyvinyl alcohol (Changling Catalyst Factory) mixes, then adds 1200 milliliters of aqueous solutions containing nitric acid 24g, extrudes into outer diameter φ 1.1mm on the twin-screw extruder Clover shaped strips. The wet strip was dried at 120° C. for 4 hours and calcined at 750° C. for 3 hours to obtain carrier 1-Z2. The physical and chemical properties of carrier 1-Z2 are shown in Table 1-1.
[0039] Table 1-1
[0040] carrier number
Embodiment 1-3
[0042] The hydrodemetallization catalyst used in the present invention with alumina as the carrier and its preparation method are described.
[0043] Get 200 grams of carrier 1-Z1 prepared in Example 1-1, use 500 milliliters of MoO 3 80 g / l, V 2 o 5 The mixed solution of 16 g / L ammonium heptamolybdate and ammonium metavanadate was impregnated for 1 hour, filtered, dried at 120°C for 4 hours, and calcined at 430°C for 3 hours to obtain the hydrodemetallization catalyst 1-CZ1. The composition of hydrodemetallization catalyst 1-CZ1 is listed in Table 1-2.
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