Catalyst for heavy oil fixed bed hydrogenating treatment and its preparation process
A hydrogenation treatment and catalyst technology, applied in the direction of naphtha catalytic reforming, etc., can solve the problems of clogging the catalyst bed, low level of impurity removal, failure to improve the activity of the protection catalyst and demetallization catalyst, etc. Effect of Hydrogen Saturation Capacity
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Embodiment 1
[0013] Weigh 298g Si-Al 2 o 3 (dry basis 67w%, silicon content is 13%) powder, powdered activated carbon 24.5g Tianqing powder 5g, the three are mixed uniformly, add by 208g water, 22.0g contain 17w%TiCl 3 TiCl 3 Acidic solution mixed with 22g HAc (acetic acid), kneaded for 1.5 hours, and the obtained plastic body was made into Φ2.58~2.64mm special-shaped strips with an extrusion machine, and the strips were dried at 108°C for 4 hours , and calcined at 880°C for 3 hours to obtain a catalyst carrier.
[0014] Using a general impregnation method, impregnate the carrier in two steps with an active metal solution (ammonium metatungstate + nickel nitrate solution; ammonium molybdate + ammonia solution), and then dry at 80°C / 120°C for 5 hours / 3 hours, respectively. Calcined at 480°C / 530°C for 3 hours / 2 hours to make catalyst CAT-1. The composition and main properties of the catalyst are shown in Table 1.
Embodiment 2
[0016] In the carrier preparation process of Example 1, no powdered activated carbon was used, the carrier calcination temperature was 980° C., and other conditions remained unchanged, that is, the catalyst CAT-2 of this example was prepared. The composition and main properties of the catalyst are shown in Table 1.
Embodiment 3
[0018] In the carrier preparation process of Example 1, Si-Al containing silicon dioxide of 15w% was used 2 o 3 powder, increasing the amount of titanium, and extruding the plastic body into a special-shaped strip of Φ1.10-1.35mm. The strip was dried at 108°C for 4 hours and roasted at 750°C for 4 hours to obtain a carrier. Catalyst preparation conditions remain unchanged, that is, the catalyst CAT-3 of this example is prepared. The composition and main properties of the catalyst are shown in Table 1.
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