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A kind of preparation method of silicon-based catalytic cracking catalyst

A catalytic cracking and catalyst technology, applied in the field of preparation of silicon-based catalytic cracking catalysts, can solve the problems of easy gelation of colloids, easy loss of fluidity, poor stability of acid silica sols and difficult storage, etc. Beneficial for rapid diffusion

Active Publication Date: 2018-10-16
PETROCHINA CO LTD
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0013] The invention provides a method for preparing a silicon-based catalytic cracking catalyst, which solves the problem that acid silica sol, which is used as a catalyst matrix for catalytic cracking, has poor stability and is not easy to store. During the catalyst process, it is easy to lose fluidity. At the same time, the molecular sieve is modified with rare earth, and optimized from the two aspects of matrix and active components, so that the prepared catalytic cracking catalyst has better coke selectivity and better resistance to heavy metals.

Method used

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  • A kind of preparation method of silicon-based catalytic cracking catalyst
  • A kind of preparation method of silicon-based catalytic cracking catalyst

Examples

Experimental program
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Effect test

Embodiment 1

[0045] In the reaction tank with water bath heating, add 2.3kg water, 857g 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 A 1.0% rare earth aqueous solution by mass, in which oxalic acid is pre-dissolved in water, is stirred for 40 minutes respectively to obtain a mo...

Embodiment 2

[0047] In a reaction tank with water bath heating, add 2.3kg of water, add 909g of activated alumina (solid content 66% by weight) under stirring, then slowly add hydrochloric acid for peptization, stir for 1h, add 786g 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 A 1.0% rare earth aqueous solution by mass, in which oxalic acid is pre-dissolved in water, is stirred for 40 minutes respectively to obtain a ...

Embodiment 3

[0049] In a reaction tank with water bath heating, add 2.3kg of water, add 864g of activated alumina (solid content: 66% by weight) under stirring, then slowly add hydrochloric acid for peptization, and stir for 1 hour. The initial pH value of sodium-type alkaline silica sol (silica content 30% by weight) is 9.60. Weigh 1000 g of alkaline silica sol, add 7 ml of concentrated hydrochloric acid (concentration 37 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 A 1.0% rare earth aqueous solution by mass, in which oxalic acid is pre-dissolved in an appropriate amount of water, and stirred for 40 minutes respectively to obtain a modified molecular sieve slurry. Ad...

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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 Al-based binder, a modified molecular sieve, clay and silica sol, and carrying out spray drying and roasting to obtain the catalyst. The silica sol is acid-modified alkaline silica sol and under modification conditions of stirring and a temperature of 0-30 DEG C, an acid is added into the alkaline silica sol and the mixture is uniformly mixed until sol pH is in a range of 1-5 so that the acid-modified alkaline silica sol is obtained. Under modification conditions of stirring and a temperature of 0-30 DEG C, water is added into a molecular sieve, the mixture is beat to form slurry, an organic acid is added into the slurry for Al removal modification, a rare earch solution is added into the slurry and the mixture is uniformly mixed to form the modified molecular sieve slurry. The catalyst has the advantages of coke selectivity and heavy metal resistance.

Description

technical field [0001] The invention relates to a preparation method of a catalytic cracking catalyst, in particular to a preparation method of a silicon-based 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 ox...

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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