High-activity hydrocracking catalyst and preparation method thereof
A hydrocracking and catalyst technology, applied in physical/chemical process catalysts, chemical instruments and methods, hydrocarbon oil cracking, etc., can solve the problem of increasing the diffusion resistance of reactants and products, increasing the possibility of secondary cracking The probability of cracking reaction increases and other problems, to achieve the effect of excellent sulfur and nitrogen resistance, easy implementation and few steps
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Embodiment 1
[0018] Embodiment 1: 140ml concentration is 0.03mol L -1 cesium carbonate solution, 135ml concentration is 1mol L -1 The concentration of nickel nitrate solution and 90ml is 3mol·L -1 citric acid solution to prepare a mixed solution, then add 140ml tetraethyl orthosilicate, stir at 60°C for 0.5h, then add 50g aqueous solution of phosphotungstic acid, stir at 80°C to evaporate the solution, and dry the obtained solid for 24h . Dry the dried solid in a muffle furnace at 2°C min -1 The speed is increased to 400 ° C, and the temperature is kept for 4 hours to produce 8% Ni-50% Cs 0.5 h 2.5 PW 12 o 40 / SiO 2 Catalyst, wherein the molar ratio of citric acid to nickel is 2.
[0019] Put the catalyst into the reaction tube, feed hydrogen, and the volume space velocity is 1500h -1 , the pressure of the reaction system is gradually increased to 2.0MPa. After checking that there is no air leakage, the temperature of the reaction system is raised to 300°C, and the heating rate is...
Embodiment 2
[0020] Embodiment 2: in embodiment 1, cesium carbonate solution is changed into 280ml, tetraethyl orthosilicate is changed into 135ml, and all the other are the same as embodiment 1, and gained catalyst is 8%Ni-50%CsH 2 PW 12 o 40 / SiO 2 .
[0021] The evaluation of the catalyst is the same as in Example 1, and the results of the conversion rate and the selectivity of cracked products are shown in Table 1.
Embodiment 3
[0022] Embodiment 3: in embodiment 1, cesium carbonate solution is changed into 420ml, tetraethyl orthosilicate is changed into 130ml, all the other are the same as embodiment 1, gained catalyst is 8%Ni-50%Cs 1.5 h 1.5 PW 12 o 40 / SiO 2 .
[0023] The evaluation of the catalyst is the same as in Example 1, and the results of the conversion rate and the selectivity of cracked products are shown in Table 1.
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