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Heavy oil catalytic cracking catalyst, preparation method of heavy oil catalytic cracking catalyst and heavy oil catalytic cracking method

A technology for cracking catalyst and heavy oil catalysis, applied in catalytic cracking, physical/chemical process catalyst, molecular sieve catalyst, etc., can solve the problems of low gasoline octane number, decreased gasoline yield, poor coke selectivity, etc.

Active Publication Date: 2017-01-04
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0016] The purpose of the present invention is to solve the problems of poor stability of existing heavy oil catalytic cracking catalysts, poor selectivity of coke in heavy oil catalytic cracking reactions and low gasoline octane product (being the product of octane number and gasoline yield) of gasoline products , providing heavy oil catalytic cracking catalyst and its preparation method and heavy oil 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

Method used

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preparation example Construction

[0047] The present invention also provides a method for preparing a catalyst, the method comprising: (A) performing gas-phase superstable treatment, washing and rare earth ion exchange on small-grain Y-type zeolite in sequence to prepare small-grain gas-phase superstable high-silicon rare earth Y Type zeolite; (B) the small crystal 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, activated alumina, inorganic oxide The compound binder and water are mixed and beaten, spray-dried, roasted, washed, filtered and dried to obtain a catalytic cracking catalyst; the inorganic oxide binder contains at least one active alumina.

[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 accord...

Embodiment 1

[0066] This example is used to illustrate the preparation of the heavy oil 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 zeolite, and filter;

[0070] (3) Rare earth ion exchange: After the...

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 a heavy oil catalytic cracking catalyst and its preparation method and a heavy oil catalytic cracking method. The heavy oil catalytic cracking catalyst comprises 10-40% by dry base weight of small crystal grain gas phase ultrastable high-silica rare earth Y-type zeolite, 10-60% by dry base weight of clay and 13-60% of by oxide weight of an inorganic oxide, the inorganic oxide contains at least one active alumina, the average diameter of the alumina crystal grains is in a range of 0.1-0.8 micrometers, a lattice constant is in a range of 24.5-24.6 angstroms and a silica-alumina ratio is in a range of 7-10. The small crystal grain gas phase ultrastable high-silica rare earth Y-type zeolite comprises, by weight, 6-16% of a rare earth oxide and less than 2% of sodium oxide. The Y-type zeolite is prepared from small crystal grain Y-type zeolite through gas phase ultrastable treatment, washing and rare earth ion exchange. The average aperture of the active alumina is in a range of 5-25nm. The catalytic cracking catalyst has good stability and good catalytic cracking coke selectivity and can produce a gasoline product with a high gasoline octane number and good quality.

Description

technical field [0001] The invention relates to a catalyst for catalytic cracking of heavy oil, a preparation method thereof, and a method for catalytic cracking of heavy oil with the 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 necessary to further improve the performance of catalytic cracking catalysts and convert h...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01J29/08C10G11/05
Inventor 田辉平严加松龙军周灵萍朱玉霞张杰潇李家兴刘博
Owner CHINA PETROLEUM & CHEM CORP
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