Paraffin hydrofining catalyst and preparation method thereof
A hydrorefining and catalyst technology, applied in petroleum wax refining, catalyst activation/preparation, molecular sieve catalysts, etc., can solve the problems of not improving the dispersion of active metal nickel, not reducing the distribution of active metals, and low utilization of active metals. Achieve the effects of weakening capillary pressure, reducing polarity and free energy, and high utilization
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Embodiment 1
[0040] (1) Weigh 500g of pseudo-boehmite and 30g of montmorillonite, mix well;
[0041] (2) Weigh 5g hydrogen-type Y-type molecular sieve (SiO 2 / Al 2 o 3 The molar ratio is 4.7), added to 400g deionized water, mixed and beaten;
[0042] (3) Add the slurry obtained in step (2) to the mixture obtained in step (1), add 10g of turnip powder, 20g of methylcellulose, 15g of acetic acid, add an appropriate amount of deionized water, and knead at room temperature to form. After forming, dry at 120°C for 4 hours, and bake at 600°C for 4 hours. The specific surface area of the carrier after calcination is 365 m 2 / g, the pore volume is 0.90 mL / g, and the average pore diameter is 12nm;
[0043] (4) Weigh 100 g of the catalyst carrier prepared in step (3), spray and soak it with 100 ml of Span-80 ethanol solution with a concentration of 0.3 g / 100 mL, and then dry it in vacuum at 60 ° C for 5 hours;
[0044] (5) Dissolve ammonium molybdate, nickel nitrate and phosphoric acid in wa...
Embodiment 2
[0047] Others are the same as in Example 1, except that in step (1), 50 g of montmorillonite is weighed and mixed with pseudo-boehmite to obtain paraffin hydrotreating catalyst B.
Embodiment 3
[0049] Others are the same as in Example 1, except that in step (2), 10 g of hydrogen-type Y-type molecular sieves are weighed and added to 400 g of deionized water, mixed and beaten to obtain paraffin hydrorefining catalyst C.
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