Preparation method and application of a hydrocracking catalyst
A hydrocracking and catalyst technology, applied in physical/chemical process catalysts, metal/metal oxide/metal hydroxide catalysts, chemical instruments and methods, etc. Complexity and other issues, to achieve the effect of short preparation cycle, low equipment investment and simple operation process
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Embodiment 1
[0025] This embodiment provides a method for preparing a hydrocracking catalyst, comprising the following steps:
[0026] (1) Dry distillation of biomass charcoal by acidification treatment, washing treatment and drying treatment to obtain a biomass charcoal carrier
[0027] Choose H + Sulfuric acid, hydrochloric acid or nitric acid solution with a molar concentration of 0.5mol / L~5mol / L, the volume ratio of biomass charcoal and acidic medium is 1:5~1:15, the acidification temperature is 30℃~80℃, and the acidification time is 1h ~10h;
[0028] The biochar after the acidification treatment is washed with deionized water, and the biochar is washed to neutrality;
[0029] The washed biochar is dehydrated and dried, wherein the drying temperature is 80°C-120°C, the drying time is 2h-12h, and the water content of the biochar carrier obtained after drying treatment is 5%-10%, and the specific surface 50m 2 / g~200m 2 / g, the pore diameter is 1nm~20nm, the pore volume is 0.01cm 3...
Embodiment 2
[0039] This embodiment provides a method for preparing a hydrocracking catalyst, comprising the following steps:
[0040] (1) Dry distillation of biomass charcoal by acidification treatment, washing treatment and drying treatment to obtain a biomass charcoal carrier
[0041]Use nitric acid for acidification, the concentration is 0.5mol / L; the volume ratio of biomass charcoal and nitric acid is 1:5, the acidification temperature is 80°C, and the acidification time is 10 hours; after acidification, it is washed with deionized water until neutral, dehydrated, and dried. The drying temperature is 80°C and the drying time is 2 hours to obtain a water content of 10% and a specific surface area of 200m 2 / g, pore diameter 1nm, pore volume 0.1cm 3 / g of biochar carrier.
[0042] (2) Mix and grind the biochar carrier and the catalyst active component to prepare the hydrocracking catalyst
[0043] The cobalt oxide and the biomass carbon carrier were mixed, added into a vibrating gr...
Embodiment 3
[0048] This embodiment provides a method for preparing a hydrocracking catalyst, comprising the following steps:
[0049] (1) Dry distillation of biomass charcoal by acidification treatment, washing treatment and drying treatment to obtain a biomass charcoal carrier
[0050] Sulfuric acid was used for acidification with a concentration of 3.5mol / L; the volume ratio of biomass charcoal and sulfuric acid was 1:15, the acidification temperature was 30°C, and the acidification time was 1 hour; after acidification, it was washed with deionized water until neutral, dehydrated, and dried. The drying temperature is 120°C and the drying time is 12 hours to obtain a water content of 5% and a specific surface area of 50m 2 / g, pore diameter 20nm, pore volume 0.01cm 3 / g of biochar carrier.
[0051] (2) Mix and grind the biochar carrier and the catalyst active component to prepare the hydrocracking catalyst
[0052] Mix the tungsten oxide and the biochar carrier, put them into a plan...
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