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Preparation method of sulfur-reducing catalytic cracking aid

A catalytic cracking aid and sulfur reduction technology, used in catalyst activation/preparation, catalytic cracking, molecular sieve catalysts, etc., can solve the problems of reducing gasoline yield, declining gasoline production efficiency, catalytic cracking catalyst poisoning, etc., and reducing sulfur content. , The effect of reducing sulfur content and promoting catalytic conversion

Pending Publication Date: 2021-01-08
HUNAN JULI CATALYST
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

[0004] At present, although there are sulfur-reducing additives that can reduce the sulfur content in FCC gasoline, which can reduce the sulfur content in FCC gasoline, the use of existing sulfur-reducing additives will also reduce the yield of gasoline, and some even It will have a poisoning effect on the catalytic cracking catalyst and reduce the efficiency of gasoline production in the catalytic cracking process

Method used

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  • Preparation method of sulfur-reducing catalytic cracking aid

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0025](1) Mix 99g of catalyst residue, 792g of kaolin, 45g of titanium tetrachloride, 44g of sodium silicate with 3000mL of water to make a slurry, spray-dry to form microspheres, the microsphere particles are 0~150μm, and the microspheres are calcined at 600℃ for 5h, Roasted microspheres;

[0026](2) Put 300g of calcined microspheres, 100mL of lye, 270mL of sodium silicate, 82mL of directing agent, 75mL of water obtained in step (1) into a crystallization reactor, hydrothermally crystallize at 95℃ for 36h, and filter to remove the mother liquor Afterwards, the filter material is washed with water, filtered, and dried to obtain a molecular sieve composite material;

[0027](3) Add 200 g of molecular sieve composite material obtained in step (2), 100 g of ammonium chloride, and 600 mL of water, add 5% hydrochloric acid, adjust the pH of the system to 3.0, exchange for 10 minutes at room temperature, filter, wash and filter, the exchange product is in Roast with steam at 550°C for 3 hours t...

Embodiment 2

[0032](1) Mix 166g of catalyst filter residue, 594g of kaolin, 45g of titanium sulfate, 24g of tetrabutyl titanate, 20g of corn flour with 4000mL of water, mix and make a slurry, spray dry into microspheres, the microsphere particles are 0~150μm, and the microspheres are at 700℃ Roasted for 3h to obtain roasted microspheres;

[0033](2) Put 200g of calcined microspheres, 40mL of lye, 350mL of sodium silicate, 60mL of directing agent, and 50mL of water obtained in step (1) into a crystallization reactor, hydrothermally crystallize at 110°C for 12h, and filter to remove the mother liquor Afterwards, the filter material is washed with water, filtered, and dried to obtain a molecular sieve composite material;

[0034](3) 150g of molecular sieve composite material obtained in step (2), 60g of ammonium chloride, and 450mL of water were added to 5% hydrochloric acid, the system pH=3.1, exchanged at room temperature for 40min, after filtering, washing and filtering, the exchange product Roasting ...

Embodiment 3

[0039](1) Mix 300g filter residue of the catalyst, 660g kaolin, 30g titanium oxide, 10g sodium hydroxide, 4000mL ionized water, and spray dry into microspheres. The microsphere particles are 0~150μm, and the microspheres are calcined at 800℃ for 2h to obtain Roasted microspheres;

[0040](2) Put 300g of calcined microspheres, 400mL of lye, 193mL of sodium silicate, 60mL of directing agent, and 130mL of water obtained in step (1) into a crystallization reactor, hydrothermally crystallize at 98°C for 22h, and filter to remove the mother liquor Afterwards, the filter material is washed with water, filtered, and dried to obtain a molecular sieve composite material;

[0041](3) Add 200 g of molecular sieve composite material obtained in step (2), 60 g of ammonium chloride, and 600 mL of water, add 5% hydrochloric acid, adjust the pH of the system to 3.3, exchange for 15 minutes at room temperature, filter, wash and filter, and repeat the above Exchange twice, calcining the exchange product at ...

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Abstract

The invention belongs to the technical field of catalytic cracking auxiliary agent preparation, and discloses a sulfur-reducing catalytic cracking auxiliary agent preparation method, which comprises:(1) adding water to catalyst filtration residue, kaolin and an auxiliary agent, carrying out mixing beating, carrying out spray drying to form microspheres, and calcining to obtain calcined microspheres; (2) mixing the calcined microspheres, alkali liquor, sodium silicate, a guiding agent and water, carrying out hydrothermal crystallization, filtering, and drying to obtain a molecular sieve composite material; (3) performing acid exchange and ammonium salt exchange on the molecular sieve composite material, filtering, and roasting the exchange product to obtain an HY molecular sieve; (4) carrying out exchange modification with rare earth and vanadium elements on the HY molecular sieve, and carrying out drying and roasting to obtain an REV modified molecular sieve; and (5) dipping the REV modified molecular sieve into a metal solution, drying, and roasting to obtain the sulfur-reducing catalytic cracking aid. The sulfur-reducing auxiliary agent prepared by the invention is used in a catalytic cracking process, can effectively reduce the sulfur content, creates favorable conditions for cyclic utilization of filter residues generated in a catalyst production process, and can reduce environmental pollution and production cost by utilizing the filter residues.

Description

Technical field[0001]The invention belongs to the technical field of preparation of catalytic cracking aids, and relates to a preparation method of a sulfur reduction catalytic cracking aid.Background technique[0002]With the continuous economic development and the continuous improvement of people's living standards, the role of automobiles in people's daily life will become more and more important, and the contradiction between the continuous increase in the number of automobiles and the improvement of environmental quality will become increasingly prominent. The sulfur in gasoline not only directly affects SOx emissions, pollutes the environment, and leads to the formation of acid rain, but also has harmful effects on the low-temperature activity of automobile catalysts, thereby affecting volatile organic compounds, CO, NOx, PM (particulate matter) and total Emissions of poisons. About 80% of gasoline in my country comes from the catalytic cracking process, and 85%-95% of the sulfu...

Claims

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Application Information

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IPC IPC(8): B01J29/16B01J35/10B01J37/10B01J37/30B01J37/02B01J37/08C10G11/05
CPCB01J29/166B01J37/10B01J37/30B01J37/0201B01J37/088C10G11/05C10G2300/202B01J2229/183B01J2229/186B01J35/615B01J35/633
Inventor 谈立成郑淑琴
Owner HUNAN JULI CATALYST