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Preparation method of silicon-based catalytic cracking catalyst

A catalytic cracking and catalyst technology, applied in the direction of physical/chemical process catalysts, molecular sieve catalysts, chemical instruments and methods, etc., can solve the problems of poor stability of acid silica sol, difficulty in storage, easy loss of fluidity, etc., to achieve rapid diffusion, The effect of increasing solid content and reducing production cost

Active Publication Date: 2019-01-18
PETROCHINA CO LTD
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0013] The invention discloses a preparation method of a silicon-based catalytic cracking catalyst, which solves the problem that acid silica sol, which is used as a catalytic cracking catalyst matrix, has poor stability and is difficult to store, and that the colloids existing in the alkaline silica sol in the process of preparing a silicon-rich catalytic cracking catalyst are easy to gel, In the process of preparing the catalyst, it is easy to lose fluidity. At the same time, the molecular sieve is modified by precipitation rare earth, and optimized from both the matrix and the active component, so that the prepared catalytic cracking catalyst has better coke selectivity and better resistance to heavy metals. performance

Method used

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  • Preparation method of silicon-based catalytic cracking catalyst
  • Preparation method of silicon-based catalytic cracking catalyst

Examples

Experimental program
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Embodiment 1

[0046] In the reaction tank with water bath heating, add 2.3kg water, 714g aluminum sol (solid content 21% by weight), add 909g activated alumina (solid content 66% by weight) under stirring, then slowly add hydrochloric acid and carry out peptization, Stir for 1h. The initial pH value of sodium-type alkaline silica sol (30% by weight of silicon dioxide content) is 9.60. Weigh 1000 g of alkaline silica sol, add 9 ml of concentrated hydrochloric acid (concentration 37% by mass) under stirring conditions, and stir evenly to obtain the pH value 3.0 hydrochloric acid modified alkaline silica sol; 1.28kg of REHY molecular sieve with a solid content of 82% by weight plus 1.92kg of water for beating and dispersion, adding 3% oxalic acid relative to the dry basis of the molecular sieve and relative to the dry basis of the catalyst RE 2 o 3 1.0% rare earth solution by mass, wherein oxalic acid is pre-dissolved in water, a 1:1 diluted aqueous solution of the rare earth solution and th...

Embodiment 2

[0048] In a reaction tank with water bath heating, add 2.3kg of water, add 1045g of activated alumina (solid content 66% by weight) under stirring, then slowly add hydrochloric acid for peptization, stir for 1h, add 571g of aluminum sol (solid content 21% by weight) weight%). The initial pH value of sodium-type alkaline silica sol (silicon dioxide content 30% by weight) is 9.60. Weigh 1000 g of alkaline silica sol, add 8 ml of concentrated hydrochloric acid (concentration 37 mass %) under stirring conditions, and stir evenly to obtain the pH value 3.5 hydrochloric acid modified alkaline silica sol; 1.28kg of REHY molecular sieve with a solid content of 82% by weight plus 1.92kg of water for beating and dispersion, adding 3% oxalic acid relative to the dry basis of the molecular sieve and relative to the dry basis of the catalyst RE 2 o 3 1.0% rare earth solution by mass, wherein oxalic acid is pre-dissolved in an appropriate amount of water, and a 1:1 diluted aqueous solutio...

Embodiment 3

[0050] In a reaction tank with water bath heating, add 2.3 kg of water, add 1000 g of activated alumina (solid content: 66% by weight) under stirring, then slowly add hydrochloric acid for peptization, and stir for 1 h. The initial pH value of sodium-type alkaline silica sol (30% by weight of silica content) is 9.60. Weigh 1000 g of alkaline silica sol, add 7 ml of concentrated hydrochloric acid (concentration: 37% by mass) under stirring conditions, and stir evenly to obtain the pH value 3.8 hydrochloric acid modified alkaline silica sol; 1.28kg of REHY molecular sieves with a solid content of 82% by weight plus 1.92kg of water for beating and dispersion, adding 3% oxalic acid relative to the dry basis of the molecular sieve and relative to the dry basis of the catalyst RE 2 o 3 1.0% rare earth solution by mass, wherein oxalic acid is pre-dissolved in an appropriate amount of water, and a 1:1 diluted aqueous solution of the rare earth aqueous solution and the precipitant amm...

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Abstract

The invention discloses a preparation method of a silicon-based catalytic cracking catalyst. The preparation method comprises mixing and beating an aluminum-based binder, a modified molecular sieve, clay and silica sol to obtain paste and carrying out spray drying and roasting to obtain the catalyst. The silica sol is alkaline silica sol modified by an acid and a modification method of the alkaline silica sol comprises adding an acid into the alkaline silica sol at a temperature of 0-30 DEG C along with stirring so that the uniform sol has pH of 1-5 and is acid-modified silica sol. A preparation method of the modified molecular sieve comprises adding water into a molecular sieve at a temperature of 0-30 DEG C along with stirring, beating the mixture, then adding an organic acid into the slurry along with stirring for aluminum removal modification, then adding a rare earth ion precipitating agent and a rare earth aqueous solution into the slurry together and carrying out uniform stirring to obtain the modified molecular sieve slurry. The catalyst has good coke selectivity and good anti-heavy metal performances.

Description

technical field [0001] The invention relates to a preparation method of an oil refining catalyst, in particular to a preparation method of a catalytic cracking catalyst. Background technique [0002] Fluid Catalytic Cracking (FCC for short) process is the main process of secondary processing of crude oil, an important means of deep processing of heavy oil, and one of the main sources of economic benefits of various refineries. As the world's petroleum resources continue to become heavy and inferior, blending heavy oil and residual oil in the catalytic cracking process has become a common processing method for refineries in various countries. Heavy oil contains more asphaltenes, colloids and heavy metals, especially vanadium and nickel are high in heavy metals. In the cracking reaction, heavy metals such as vanadium and nickel are deposited on the surface of the catalyst, resulting in a decrease in catalyst activity, especially vanadium, which is highly oxidized and highly m...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01J29/08
Inventor 李雪礼高雄厚谭争国张海涛段宏昌潘志爽张忠东李荻蔡进军黄校亮郑云锋刘超伟袁程远
Owner PETROCHINA CO LTD
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