High-silicon rare earth Y type zeolite of small crystal grains with gas phase ultra-stabilization, catalytic cracking catalyst as well as preparation method thereof and catalytic cracking method

A gas phase ultra-stable, small-grain technology, applied in catalytic cracking, crystalline aluminosilicate zeolite, octahedral crystalline aluminum silicate zeolite, etc., can solve the problem of gasoline octane number decline, poor coke selectivity, gasoline octane number Problems such as low accumulation

Active Publication Date: 2017-01-04
CHINA PETROLEUM & CHEM CORP +1
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  • Abstract
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Problems solved by technology

[0016] The purpose of the present invention is in order to solve the problem that existing catalytic cracking catalyst stability is poor, carries out catalytic cracking reaction coke selectivity difference and the gasoline octane number product (being the product of octane number and gasoline yield) of the gasoline product that obtains is low, provides Disclosed are small-grain gas-phase ultra-stable high-silicon rare earth Y-type zeolite, catalytic cracking catalyst, preparation method thereof, and catalytic cracking method
Among them, the octane number of catalytic cracking gasoline is directly related to the quality and price of gasoline. Generally, the increase of gasoline production by catalytic cracking faces the problem of a decrease in gasoline octane number, and the problem of gasoline yield decline when increasing the gasoline octane number

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  • High-silicon rare earth Y type zeolite of small crystal grains with gas phase ultra-stabilization, catalytic cracking catalyst as well as preparation method thereof and catalytic cracking method
  • High-silicon rare earth Y type zeolite of small crystal grains with gas phase ultra-stabilization, catalytic cracking catalyst as well as preparation method thereof and catalytic cracking method

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preparation example Construction

[0047] The present invention also provides a method for preparing the catalyst provided by the present invention, the method comprising: (A) performing gas-phase superstable treatment, washing and rare earth ion exchange on the small-grain Y-type zeolite in sequence to prepare small-grain gas-phase superstable High-silicon rare earth Y-type zeolite; (B) the small-grain gas-phase ultra-stable high-silicon rare-earth Y-type zeolite obtained in step (A), and optional hydrothermal ultra-stable high-silicon rare-earth Y-type zeolite, and clay, inorganic oxide The material binder and water are mixed and beaten, spray-dried, calcined, washed, filtered and dried to obtain a catalytic cracking catalyst.

[0048] The preparation steps of the small-crystal gas-phase ultrastable high-silicon rare earth Y-type zeolite can be described above, and will not be repeated here.

[0049] Step (B) in the present invention can be carried out according to the preparation method of the existing crack...

Embodiment 1

[0066] This example is used to illustrate the preparation of the small-grain gas-phase ultrastable high-silicon rare earth Y-type zeolite and catalytic cracking catalyst provided by the present invention.

[0067] (A) Preparation of small-grain gas-phase ultrastable high-silicon rare earth Y-type zeolite

[0068] (1) Gas phase ultra-stable treatment: dry 750 grams (dry basis, the same below) of small grain RENaY zeolite (average particle diameter is 0.2 micron, unit cell constant is 24.68 angstroms, rare earth oxide content is 13.0% by weight, The content of sodium oxide is 3.8% by weight, and the solid content is 96% by weight, produced by Sinopec Catalyst Qilu Branch) into the reactor, according to zeolite: SiCl 4 (weight ratio, the same below) = 1:0.1, feed SiCl 4 Carry out contact, the temperature of contact is 200 ℃, the time of contact is 3 minutes; Then, blow with dry air for 60 minutes;

[0069] (2) Washing: wash once with deionized water 5 times the weight of the ze...

Embodiment 2

[0074] This example is used to illustrate the preparation of the small-grain gas-phase ultrastable high-silicon rare earth Y-type zeolite and catalytic cracking catalyst provided by the present invention.

[0075] (A) Preparation of small-grain gas-phase ultrastable high-silicon rare earth Y-type zeolite

[0076] (1) Gas-phase ultra-stable treatment: get dry 750 grams of small-grain RENaY zeolite (the average particle diameter is 0.50 microns, the unit cell constant is 24.66 angstroms, the rare earth oxide content is 10.2% by weight, and the sodium oxide content is 4.0% by weight, The solid content is 97% by weight, produced by Sinopec Catalyst Qilu Branch) into the reactor, according to zeolite: SiCl 4 =1:0.3, feed SiCl 4 Carry out contact, the temperature of contact is 400 ℃, the time of contact is 15 minutes; Then, blow with dry air for 60 minutes;

[0077] (2) Washing: wash once with deionized water 10 times the weight of the zeolite, and filter;

[0078] (3) Rare earth...

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Abstract

The invention relates to high-silicon rare earth Y type zeolite of small crystal grains with gas phase ultra-stabilization, a catalytic cracking catalyst as well as a preparation method and a catalytic cracking method. The crystal grain average diameter of the high-silicon rare earth Y type zeolite of small crystal grains with gas phase ultra-stabilization is 0.1-0.8 micrometer, lattice constant is 24.5-24.6 angstrom, and silica-alumina ratio is 7-10; the total weight of the zeolite is used as a reference, wherein the content of rare earth oxide is 6-16 wt.%, and the content of sodium oxide is lower than 2 wt.%; the zeolite is prepared by gas phase ultra-stabilization treatment, washing and rare earth ion exchange in order from Y type zeolite of small crystal grains. The catalytic cracking catalyst containing the zeolite has good stability, coke after catalytic cracking has good selectivity, and obtained gasoline product has extremely high gasoline octane number and good quality.

Description

technical field [0001] The invention relates to a small-grain gas-phase high-silicon rare earth Y-type zeolite, a catalytic cracking catalyst containing the zeolite and a preparation method thereof, and a method for catalytic cracking of heavy oil by the catalytic cracking catalyst. 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 to convert them into high value-added products such as liquefied gas, gasoline, and diesel. The performance of the catalyst in the catalytic cracking process determines the distribution of catalytic cracking products and the economic benefit of the catalytic unit. Due to the depletion of petroleum resources and the large demand for light oil products in the market, it is very ...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C01B39/24B01J29/08C10G11/05
Inventor 龙军严加松周灵萍田辉平朱玉霞张杰潇李家兴刘博
Owner CHINA PETROLEUM & CHEM CORP
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