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Catalytic cracking catalyst and preparation method thereof

A catalytic cracking and catalyst technology, used in catalytic cracking, physical/chemical process catalysts, molecular sieve catalysts, etc., can solve problems such as low micropore volume, achieve low coke yield, high gasoline and liquefied gas yield, and excellent heavy oil. The effect of transforming power

Active Publication Date: 2018-05-01
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

The Y-type molecular sieve prepared by this method has ultra-high mesoporous content, but the micropore volume is low

Method used

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  • Catalytic cracking catalyst and preparation method thereof
  • Catalytic cracking catalyst and preparation method thereof
  • Catalytic cracking catalyst and preparation method thereof

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preparation example Construction

[0037] The present invention also provides a method for preparing a catalytic cracking catalyst, the preparation method comprising: mixing the raw materials used to prepare the catalytic cracking catalyst with water, and then performing beating and spray drying; wherein, in terms of dry weight, the raw materials include 25 - 75% by weight of phosphorus and rare earth-containing Y molecular sieve, 10-30% by weight of precursors of inorganic oxide binders and 15-65% by weight of natural minerals; crystals of said phosphorus and rare earth-containing Y molecular sieve The cell parameter is 24.35-24.55 angstrom; 2 o 5 Calculated and based on the dry weight of the molecular sieve, the phosphorus content of the molecular sieve is 0.3-10% by weight; 2 o 3 Calculated and based on the dry basis weight of the molecular sieve, the rare earth content of the molecular sieve is 0.5-19% by weight; the Al distribution parameter D of the molecular sieve satisfies: 0.4≤D≤0.9, wherein, D=Al(S)...

preparation Embodiment 1

[0066] Y molecular sieve (produced by Catalyst Qilu Branch, unit cell parameter 24.63 angstroms) and NH 4 Cl and distilled water were mixed and beaten evenly at a ratio of 1:1:10, ammonium was exchanged at 70°C for 1 hour, the sample was filtered, washed, and dried, and the sodium content of the molecular sieve was determined to be less than 5% by weight. The above-mentioned molecular sieves were calcined at 600°C for 2h. Take the calcined molecular sieve in an anhydrous dry environment, pass through SiCl 4Saturated dry gas, the reaction temperature is 550°C, and the reaction time is 2h; take 100g (dry basis mass) of the above-mentioned molecular sieve and add water to prepare a molecular sieve slurry with a solid content of 10% by weight, add 3g of citric acid during stirring, and then add 400g of hydrochloric acid (mass fraction 10%), the addition time was 30min; the temperature was raised to 75°C and stirred for 1h, filtered and washed until the filtrate was neutral; the f...

preparation Embodiment 2

[0072] Y molecular sieve (produced by Catalyst Qilu Branch, unit cell parameter 24.63 angstroms) and NH 4 Cl and distilled water were mixed and beaten evenly at a ratio of 1:1:10, ammonium was exchanged at 70°C for 1 hour, the sample was filtered, washed, and dried, and the sodium content of the molecular sieve was determined to be less than 5% by weight. The above-mentioned molecular sieves were calcined at 550°C for 3h. Take the calcined molecular sieve in an anhydrous dry environment, pass through SiCl 4 Saturated dry gas, the reaction temperature is 550°C, and the reaction time is 2h; take 100g (dry basis mass) of the above-mentioned molecular sieve and add water to prepare a molecular sieve slurry with a solid content of 10% by weight, add 5g of oxalic acid during stirring, and then add 200g of sulfuric acid (mass fraction 10 %), the addition time was 30 minutes; the temperature was raised to 30°C and stirred for 2 hours, filtered and washed until the filtrate was neutra...

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Abstract

The invention provides a catalytic cracking catalyst and a preparation method thereof, wherein the catalyst contains (calculated as the dry base weight) 25-75 wt% of a phosphorus-containing and rare earth-containing Y molecular sieve, 10-30 wt% of an inorganic oxide binder, and 15-65 wt% of natural minerals, wherein the unit cell parameter of the phosphorus-containing and rare earth-containing Y molecular sieve is 24.35-24.55 angstrom, the phosphorus content of the molecular sieve is 0.3-10 wt%, the rare earth content of the molecular sieve is 0.5-19 wt%, the Al distribution parameter D of themolecular sieve is more than or equal to 0.4 and is less than or equal to 0.9, the volume of the mesopores of the molecular sieve accounts for 20-65% of the total pore volume, the amount of the strong acid of the molecular sieve accounts for 20-60% of the total acid amount, and a ratio of the acid B to the acid L is 20-100. According to the present invention, the catalytic cracking catalyst has advantages of excellent heavy oil conversion capability, high gasoline yield, high liquefied gas yield and low coke yield in the catalytic cracking of heavy oil.

Description

technical field [0001] The invention relates to a catalytic cracking catalyst and a preparation method thereof. Background technique [0002] Catalytic cracking (FCC) is an important secondary processing process of crude oil and occupies a pivotal position in the oil refining industry. In the catalytic cracking process, heavy fractions such as vacuum distillate oil or residues of heavier components react in the presence of catalysts and are converted into high value-added products such as liquefied gas, gasoline, and diesel oil. In this process, it is usually necessary to use Catalytic material with high cracking activity. Molecular sieves are widely used in petroleum refining and processing industries due to their shape-selective properties, high specific surface area, and strong acidity. Y-type molecular sieves (HY, REY, USY) have been the main active components of catalytic cracking and hydrocracking catalysts since they were first used in the 1960s. However, with the ...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01J29/08C10G11/05
CPCB01J29/088C10G11/05
Inventor 庄立罗一斌朱玉霞欧阳颖陈振宇刘建强任飞舒兴田
Owner CHINA PETROLEUM & CHEM CORP
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