Hydrocracking catalyst with high activity and high-medium oil selectivity and preparation method of hydrocracking catalyst
A hydrocracking and catalyst technology, applied in physical/chemical process catalysts, molecular sieve catalysts, chemical instruments and methods, etc., can solve the problems of low catalyst hydrocracking activity, high catalyst hydrocracking activity, and high medium oil selectivity, Achieve the effect of reducing metal loss, preventing skeleton collapse, and improving oil selectivity
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example 1
[0024] Catalyst A is the catalyst prepared by the inventive method, and catalyst weight is composed of: WO 3 22.5%, NiO 8.5%, ZrO 2 6.5%, SiO 235.5%, Al 2 o 3 27.0%, of which the molecular sieve content is 25%, and the specific surface area is 260m 2 / g, the pore volume is 0.35ml / g.
[0025] Concrete preparation steps are as follows:
[0026] (1) Prepare Al-containing 2 o 3 600 ml of aluminum chloride solution with a concentration of 90 g / l, containing NiO 200 ml of nickel chloride solution with a concentration of 140 g / l, containing ZrO 2 150ml of 140g / l zirconium oxychloride solution was mixed in a 5 liter container and diluted with 2000ml of clean water.
[0027] (2) Prepare dilute water glass solution, containing SiO 2 550 milliliters of water glass solution of 75g / l, under stirring situation, (2) is added in (1);
[0028] (3) Add ammonia water to the mixture of (1) and (2) under stirring until the pH value is 5.2;
[0029] (4) Prepare 1000 ml of sodium tungs...
example 2
[0037] It is the hydrocracking catalyst B of the present invention, and the preparation method is the same as that of Example 1, except that 20% of the Y-type molecular sieve modified by hydrothermal treatment is added before aging, and the molecular sieve Y-B prepared by ZL96119840.0 Example 2 is used as a raw material for the molecular sieve, and the Hydrothermal treatment, hydrothermal treatment conditions are temperature 780 ° C, pressure 0.3 MPa, ammonia partial pressure 1000 Pa, time 22 hours, then acid treatment, using 2.0 M sulfuric acid 3000 ml, sulfuric acid and molecular sieve weight ratio is 1: 2, temperature 50 ° C , time 12 hours, obtained modified molecular sieve Y-B 1 , Y-B and Y-B 1 The properties are shown in Table 3. Catalyst weight composition is: WO 3 21.0%, NiO 7.5%, ZrO 2 6.5%, SiO 2 35.0%, Al 2 o 3 30.0%, the specific surface is 245m 2 / g, the pore volume is 0.34ml / g.
example 3
[0039] It is the hydrocracking catalyst C of the present invention, and the preparation method is the same as that of Example 1, except that 30% of the Y-type molecular sieve modified by hydrothermal treatment is added before aging, and the molecular sieve Y-C prepared by ZL96119840.0 Example 3 is used as a raw material for the molecular sieve, and the Hydrothermal treatment, hydrothermal treatment conditions are temperature 800 ° C, pressure 0.2MPa, ammonia partial pressure 2500Pa, time 28 hours, then carry out acid treatment, use 4.0M hydrochloric acid 8500 milliliters, hydrochloric acid and molecular sieve weight ratio is 1: 18, temperature 70 ℃, time 15 hours, obtained modified molecular sieve Y-C 1 , Y-C and Y-C 1 The properties are shown in Table 3. Catalyst weight composition is: WO 3 23.6%, NiO 7.4%, ZrO 2 7.0%, SiO 2 34.0%, Al 2 o 3 28.0%, the specific surface is 270m 2 / g, the pore volume is 0.35ml / g.
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