Catalyst for catalytic cracking mixed waste plastic and preparation method thereof
A catalytic cracking and catalyst technology, used in the preparation of liquid hydrocarbon mixtures, physical/chemical process catalysts, molecular sieve catalysts, etc. The effect of good product quality, flexible process operation and high octane number
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Embodiment 1
[0019] Preparation of the catalyst for the first stage of waste plastic cracking: Add 150 parts of ferric nitrate aqueous solution with an iron content of 3.0wt% to 100 parts of acid white powder, soak for 2 hours at 60 ° C, leave it standing after soaking and pour out the supernatant, and pour the supernatant at 120 After drying at 480°C for 4 hours, and then activating at 480°C for 5 hours, it was determined that the iron oxide content was 2.2 wt%, so that the iron oxide-modified Baishi catalyst was obtained.
[0020] The preparation of the catalyst for catalytic cracking and upgrading of the second stage of crude oil: add 150 parts of lanthanum nitrate aqueous solution containing 1.5wt% lanthanum to 100 parts of hydrogen ZSM-5, soak for 2 hours at 80 ° C, let stand and pour after soaking The supernatant was taken out, dried at 120°C for 4 hours, and then activated at 500°C for 5 hours, and the content of lanthanum oxide was determined to be 1.3 wt%, that is, the lanthanum ox...
Embodiment 2
[0024] Preparation of the catalyst for the cracking of waste plastics in the first stage: Add 150 parts of ferric nitrate aqueous solution containing 6.0 wt% magnesium to 100 parts of acid white powder, soak for 2 hours at 60°C, let stand after soaking and pour out the supernatant, and pour the supernatant at 120 After drying at 480°C for 4 hours, and then activating at 480°C for 5 hours, the content of magnesium oxide was determined to be 6.7wt%, and the magnesium oxide-modified Baishi catalyst was obtained.
[0025] Preparation of the catalytic cracking and upgrading catalyst of the second stage of crude oil: Add 150 parts of cerium nitrate aqueous solution containing 4.0wt% cerium to 100 parts of hydrogen-type USY, soak at 80°C for 2 hours, let stand after soaking and pour out the upper layer The clear liquid was dried at 120°C for 4 hours, and then activated at 500°C for 5 hours, and the content of cerium oxide was determined to be 3.9 wt%, that is, the cerium oxide-modifie...
Embodiment 3
[0029] Preparation of the catalyst for the first stage of waste plastic cracking: add 150 parts of lanthanum nitrate aqueous solution containing 12.0 wt% of lanthanum to 100 parts of montmorillonite, soak at 60 ° C for 2 hours, let stand after soaking and pour out the supernatant, Dry at 120° C. for 4 hours, and then activate at 480° C. for 5 hours. The content of lanthanum oxide is determined to be 13.5 wt %, and the lanthanum oxide-modified montmorillonite catalyst is obtained.
[0030]The preparation of the catalyst of the second stage crude oil catalytic cracking upgrading: in 100 parts of commercially available hydrogen type MCM-22 (silicon-aluminum ratio 32), add 150 parts of zinc nitrate aqueous solution of zinc content 10.0wt%, in 80 ℃ impregnate After soaking for 2 hours, let it stand still and pour out the supernatant, dry it at 120°C for 4 hours, and then activate it at 500°C for 5 hours. The zinc oxide content is determined to be 8.6wt%, and the zinc oxide modified ...
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