A kind of anti-heavy metal type catalytic cracking catalyst and preparation method thereof

A catalytic cracking and anti-heavy metal technology, applied in catalytic cracking, physical/chemical process catalysts, molecular sieve catalysts, etc., can solve problems such as insufficient selectivity of coke, lack of acidity of catalyst matrix, optimization of pore structure, etc.

Active Publication Date: 2021-06-01
PETROCHINA CO LTD
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

However, the introduction of these active components does not passivate heavy metals, but lacks further optimization of catalyst matrix acidity and pore structure, resulting in insufficient catalyst performance in heavy oil conversion and coke selectivity.

Method used

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  • A kind of anti-heavy metal type catalytic cracking catalyst and preparation method thereof
  • A kind of anti-heavy metal type catalytic cracking catalyst and preparation method thereof
  • A kind of anti-heavy metal type catalytic cracking catalyst and preparation method thereof

Examples

Experimental program
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Effect test

Embodiment 1

[0042] Preparation of Rare Earth-Containing Medium and Macroporous Si-Al Materials

[0043] Take 26.8ml NaY zeolite directing agent and mix with 51.2ml 250g / l water glass evenly, add water to dilute to Si0 2 The concentration is 40g / L (as Si0 2 , the same below), after stirring evenly, neutralize with 6mol / L sulfuric acid solution at 60°C to form a gel for aging, the pH value of the gel is 8, after adding the acid, continue to age at a constant temperature for 1.5h under stirring conditions; after the aging is completed, add 6mol / L sulfuric acid to pH=4, then slowly add 9.9ml 90g / L aluminum chloride solution (A1 2 0 3 After the addition, continue to stir for 2 hours; add 10wt% sodium hydroxide solution to adjust the pH value to 7, and age at a constant temperature for 1.5 hours under stirring at 90°C. After the obtained product is filtered and washed, the resulting solid precipitate is ion-exchanged according to ammonium nitrate: solid precipitate (dry basis): water = 1:0.5...

Embodiment 2

[0050] Preparation of Rare Earth-Containing Medium and Macroporous Si-Al Materials

[0051] Take 22.23ml of NaY zeolite directing agent and 40.89ml of tetraethyl orthosilicate, mix evenly, add water to dilute to Si0 2 The concentration is 50g / L, after stirring evenly, neutralize with 5mol / L nitric acid solution at 80°C to form a gel for aging, the pH value of the gel is 9, after adding acid, continue aging at constant temperature for 1h under stirring conditions; after aging, add 5mol dropwise / L nitric acid until the pH value = 6, then slowly add 4.76ml 90g / L aluminum nitrate solution under stirring conditions, and continue stirring for 1.5h after the addition; add 10wt% potassium hydroxide solution to adjust the pH value = 9, and stir at 95°C Aging at constant temperature for 2h. After the resulting product is filtered and washed, the resulting solid precipitate is ion-exchanged to remove sodium ions according to ammonium nitrate:solid precipitate (dry basis):water=1:0.7:9,...

Embodiment 3

[0058] Preparation of Rare Earth-Containing Medium and Macroporous Si-Al Materials

[0059] Take 13.4ml NaY zeolite directing agent and mix with 46ml 200g / L sodium silicate aqueous solution, add water to dilute to Si0 2 The concentration is 45g / L, after stirring evenly, it is neutralized with 5.5mol / L hydrochloric acid solution at 90°C to form a gel for aging, and the pH value of the gel is 10. After adding the acid, continue to age at a constant temperature for 2.5 hours under the condition of stirring; after aging, drop Add 5.5mol / L sulfuric acid to pH=5.5, then slowly add 12.41ml 90g / L aluminum sulfate solution under stirring condition, continue to stir for 1.0h after adding; add ammonia water to adjust pH=10, and age at constant temperature under stirring at 70°C 2.5h. After the obtained product is filtered and washed, the resulting solid precipitate is ion-exchanged to remove sodium ions according to ammonium sulfate: solid precipitate (dry basis): water=1:0.8:10, and th...

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Abstract

The invention provides an anti-heavy metal catalytic cracking catalyst and a preparation method thereof. The anti-heavy metal catalytic cracking catalyst has 80-50 parts of matrix, preferably 75-60 parts, containing 1-20 parts, preferably 2-12 parts, of rare earth medium and macroporous silicon-alumina materials; 0.5-15 parts, preferably 1-12 parts, of large-grain alumina materials; 20-50 parts, preferably 25-40 parts, of molecular sieves. The catalytic cracking catalyst prepared by the method has the characteristics of strong heavy metal resistance, low oil slurry yield and high total liquid product yield.

Description

technical field [0001] The invention relates to a preparation method of a catalytic cracking catalyst, in particular to a preparation method of an anti-heavy metal catalytic cracking catalyst. Background technique [0002] Since the 1980s, as the world's crude oil has become increasingly heavy and inferior, refineries in various countries have vigorously developed fluid catalytic cracking (FCC) technology for blending or fully refining heavy oil and residual oil, in order to broaden the source of FCC raw oil, To meet the demand for light oil products in the global market and maximize economic benefits. Compared with conventional FCC raw oils (such as AGO and VGO), the content of Ni, V, Fe, Cu and other metals in residual oil or heavy oil is obviously higher, which seriously pollutes FCC catalysts, and the most influential ones are nickel and vanadium, which deposit On the catalyst, the cracking activity of the catalyst is reduced, the product selectivity is poor, and when t...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01J29/08C10G11/05
CPCB01J29/088B01J2229/16B01J2229/20B01J2229/24C10G11/05
Inventor 熊晓云高雄厚王久江胡清勋张忠东赵红娟刘宏海张莉赵晓争王宝杰田爱珍
Owner PETROCHINA CO LTD
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