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Alkaline silica sol composition and application thereof in preparation of cracking catalyst

A technology of silica sol and composition, which is applied in the field of alkaline silica sol composition, can solve the problems of poor stability of acidic silica sol, discomfort of acidic silica sol, and low catalyst pore volume, and achieve high recovery cost, low cost, and favorable The effect of the cyclone

Active Publication Date: 2011-11-02
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

However, the pore volume of the catalyst prepared by acidic silica sol is low, which is not conducive to the cracking of macromolecules, and the stability of acidic silica sol is relatively poor. It needs to be stable at a lower pH value and temperature (usually below 30 ° C), and requires all The pH value of the prepared catalyst slurry should be low enough, otherwise the formed slurry is easy to gel, which requires that when using molecular sieves, alumina substrates and other component slurries to prepare catalysts, the various slurries should have a lower pH value, and usually It is necessary to adjust the pH value of the molecular sieve slurry to be acidic; however, active components such as zeolite commonly used in cracking catalysts are easily destroyed when the pH value is too low, and the activity is reduced. Therefore, acidic silica sol is not suitable for the method of directly using NaY molecular sieves to prepare catalysts.

Method used

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preparation example Construction

[0017] In the preparation method of the cracking catalyst provided by the present invention, the step of introducing clay may also be included. When the clay is introduced, the clay can be made into a slurry and then mixed with the silica sol composition and molecular sieve, or the solid clay and the alkaline silica sol composition can be beaten and then mixed with the molecular sieve. The clay is selected from one or more of kaolin, halloysite, montmorillonite, diatomite, halloysite, saponite, retortite, sepiolite, attapulgite, hydrotalcite and bentonite. Based on the weight of the catalyst, the amount of clay introduced is such that the content of clay in the catalyst does not exceed 70% by weight.

[0018] In the preparation method of the cracking catalyst provided by the present invention, it may also include the step of introducing an alumina matrix, and the alumina matrix is ​​one or more of hydrated alumina, such as hydrated alumina with a pseudo-boehmite structure, On...

Embodiment 1

[0029] Under the room temperature of 35 ℃, 4.6kg sodium water glass (produced by Sinopec Catalyst Qilu Branch, SiO 2 Content 20% by weight, modulus 3.2) mixes with 10.1kg decationized water, then under agitation, adding concentration thereinto is 0.9kg of sulfuric acid solution of 25% by weight, obtains SiO 2 A silica sol composition with a concentration of 6.0% by weight and a pH value of 10.2.

[0030] Add 3.3 kg of kaolin (produced by China Kaolin Company, solid content: 84% by weight) to 4.7 kg of decationized water, and beat to obtain a kaolin slurry.

[0031] Add 1.2kg NaY molecular sieve (manufactured by Catalyst Qilu Branch, solid content 78.2%, sodium oxide content 13.7%) into 1.9kg decationized water, beating to obtain molecular sieve slurry.

[0032] The above-mentioned silica sol composition, kaolin slurry and molecular sieve slurry are mixed and stirred to obtain a catalyst slurry, and then the slurry is spray-dried to obtain microspherical catalyst particles.

...

Embodiment 2

[0036] At room temperature of 35°C, 7.1kg of sodium water glass (produced by Sinopec Catalyst Qilu Branch, SiO 2 Content 20% by weight, modulus 3.2) is mixed with 9.1kg decationized water, then under stirring, adding therein concentration is 1.2kg of sulfuric acid solution of 20% by weight, obtains SiO 2 A silica sol composition with a concentration of 8.2% by weight and a pH value of 10.78.

[0037] Add 3.1 kg of kaolin (produced by China Kaolin Company, solid content 84% by weight) to 4.3 kg of decationized water, and beat to obtain a kaolin slurry.

[0038] Add 2.2kg NaY molecular sieve (produced by Catalyst Qilu Branch Company, solid content 78.2%, sodium oxide content 13.7%) into 3.5kg decationized water, beat to obtain molecular sieve slurry.

[0039] The above-mentioned silica sol composition, kaolin slurry and molecular sieve slurry are mixed and stirred to obtain a catalyst slurry, and then the slurry is spray-dried to obtain microspherical catalyst particles.

[00...

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Abstract

The invention relates to an alkaline silica sol composition and an application thereof in the preparation of a cracking catalyst, and the alkaline silica sol composition contains 0.9-7% by weight of alkali metal oxide, 3-20% by weight of SiO2, 0.5-7% by weight of acid radical and the balance of water, the pH value of the alkaline silica sol composition is 10-11.5; and the silica sol composition is used for preparing the cracking catalyst, and the preparation comprises the steps of mixing the silica sol composition with a NaY molecular sieve, beating, then spray drying, carrying out ion exchange and drying. The cracking catalyst prepared by the preparation method of the cracking catalyst has the advantages of high pore volume, strong heavy oil conversion capacity and high yield of gasoline.

Description

technical field [0001] The invention relates to an alkaline silica sol composition and its application in the preparation of catalytic cracking catalysts. Background technique [0002] Silica sol is widely used in the fields of casting, textile, papermaking, metallurgy and catalyst preparation, including acidic silica sol and alkaline silica sol. The commonly used methods for preparing silica sol include ion exchange, elemental silicon dissolution, electrodialysis and neutralization peace law. [0003] At present, the ion exchange method is mainly used to prepare alkaline silica sol. In this method, acidic silica sol is prepared by reacting water glass with strong acid ion exchange resin, and then adjusting the pH value with ammonia water, etc., and then evaporating and concentrating to obtain the required silica sol. This method has high energy consumption, and the regeneration of the ion exchange resin produces a large amount of waste water, resulting in high cost. [00...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01J29/08C10G11/05
Inventor 杨丽静田辉平龙军严加松
Owner CHINA PETROLEUM & CHEM CORP
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