Preparation method of roasting-free pre-vulcanized hydrogenation catalyst
A hydrogenation catalyst, catalyst technology, applied in catalyst activation/preparation, physical/chemical process catalyst, metal/metal oxide/metal hydroxide catalyst, etc., can solve the problem of low activity phase I and uneven dispersion of active components , the problem of high cost, to achieve the effect of increasing the number of active centers, excellent hydrogenation activity, and reducing the interaction
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Embodiment 1
[0024] Take 10g of basic nickel carbonate and 20g of molybdenum trioxide, add a certain amount of phosphoric acid and heat to dissolve, then add butanol and citric acid to adjust the solution to clarify, at this time, the pH is 2.5, then add 100g of alumina carrier for impregnation, after impregnation, dry at 180°C for 6 hours for later use , which is catalyst A. Wherein NiO content is 4.5wt%, MoO 3 The content is 20%, the amount of butanol is 0.5 times of the total amount of Ni+Mo metal, and the amount of citric acid is 0.5 times of the total amount of Ni+Mo metal.
[0025] Disperse sulfur powder and additive ethanolamine in the solvent of catalytic diesel oil, keep the temperature at 120°C for 2 hours, the amount of solvent used is 20% of the weight of the catalyst, the amount of sulfur used is 1.1 times the theoretical amount of sulfur required by the catalyst containing metal, and the amount of ethanolamine used is 20% of the weight of the solvent 5%, add the above-prepar...
Embodiment 2
[0027] Take 9.50g of nickel nitrate and 23.5g of ammonium metatungstate, heat and dissolve, add sorbitol and aminotriacetic acid to adjust the solution to clarify, at this time the pH is 3.0, then add 100g of alumina carrier for impregnation, after impregnation, dry at 220°C for 4 hours for later use, that is For Catalyst B. Wherein NiO content is 5wt%, WO 3 The content is 20%, the amount of sorbitol is 1 times of the total amount of Ni+W metal, and the amount of citric acid is 1 time of the total amount of Ni+W metal.
[0028] Disperse sulfur powder and additive DPTT in a biodiesel solvent, keep the temperature at 125°C for 3 hours, the amount of solvent is 10% of the weight of the catalyst, the amount of sulfur is 1.2 times the theoretical sulfur content of the catalyst containing metal, and the amount of DPTT is 1% of the weight of the solvent 8%, add the above-prepared catalyst B into this solvent and stir at a constant temperature of 125°C for 2 hours, then raise the tem...
Embodiment 3
[0030] Take 8g of basic nickel carbonate and 17.6g of molybdenum trioxide, add a certain amount of phosphoric acid to heat and dissolve, then add 19.6g of ammonium metatungstate, then add trimethylolethane and malic acid to adjust the solution to clarify, at this time the pH is 2.2, then add 100g The alumina carrier is impregnated, and dried at 250°C for 3 hours after impregnation, which is Catalyst C. . Wherein NiO content is 4.0wt%, MoO 3 The content is 17.0%, WO 3 The content is 16.7%, the amount of trimethylolethane is 0.2 times of the total amount of Ni+Mo+W metals, and the amount of malic acid is 2 times of the total amount of Ni+Mo+W metals.
[0031] Disperse sulfur powder and additive TMTD in a solvent of vegetable oil, keep the temperature at 130°C for 2.5 hours, the amount of solvent is 5% of the weight of the catalyst, the amount of sulfur is 1.4 times the theoretical amount of sulfur required by the catalyst containing metal, and the amount of TMTD is 5% of the w...
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