A method for producing high-clean gasoline with full fraction high-sulfur inferior gasoline
A technology of inferior gasoline, whole distillate
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Embodiment 1
[0053] Example 1: Preparation of catalyst carrier: Take 500 grams of aluminum hydroxide powder, 500 grams of pseudoboehmite powder, and dissolve 100 grams of citric acid in 800 mL of aqueous solution containing 3% nitric acid, knead and extrude into a φ1.5mm The cylinder was dried at 80-120°C for 6-12h, calcined at 400-600°C for 6-12h, and cooled to room temperature to obtain catalyst-supported Z1.
Embodiment 2
[0054] Embodiment 2: the preparation method of catalyst 1:
[0055] Impregnate 100 g of alumina carrier Z1 with 96 ml of a solution containing 0.56 g of lithium hydroxide, dry at 80-120 °C and bake at 500 °C, then impregnate with a co-impregnation solution containing 8.25 g of nickel nitrate and 10.23 g of ammonium molybdate milliliters, after drying at 110°C and roasting at 500°C, Catalyst 1 was obtained, and its composition was NiO1.92wt%-MO 3 7.53wt%-Li 2 O0.32wt% / Al 2 o 3 , Al 2 o 3 margin. The preparation method of catalyst 1 used in the rest of the examples is the same, but the components and contents are different.
Embodiment 3
[0056] Embodiment 3: the preparation method of catalyst 2:
[0057] Impregnate 100 grams of alumina carrier Z1 with 100 ml of an aqueous solution prepared by 2.92 grams of magnesium nitrate, 5 grams of phosphoric acid (and / or boric acid) and 10 grams of citric acid. After drying at 110 °C and roasting at 500 °C, impregnate with cobalt nitrate 80 ml of co-impregnation solutions of 12.53 g and 13.72 g of ammonium molybdate were dried at 110 °C and calcined at 500 °C to obtain catalyst 2, whose composition was CoO2.7wt%-MoO 3 9.44wt% -MgO3.88wt% -P 2 o 5 3.05wt% / Al 2 o 3 , al 2 o 3 margin. The preparation method of catalyst 2 of the remaining embodiments is the same, but each component and content are different.
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