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Modification method for Y-type molecular sieve

A molecular sieve and modification technology, applied in molecular sieve catalysts, chemical instruments and methods, physical/chemical process catalysts, etc., can solve the problems of non-framework aluminum crystallinity loss, molecular sieve reduction, acid content reduction, etc., to achieve stability and heavy oil Improvement of conversion ability, improvement of acid distribution, and improvement of silicon-aluminum ratio

Active Publication Date: 2017-03-01
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Since Al-O bonds with longer bond lengths are replaced by Si-O bonds with shorter bond lengths, the unit cell of the molecular sieve decreases, and the silicon-aluminum ratio of the skeleton increases to a certain extent, but at the same time, the acid centers of the molecular sieve will be affected, and the acid content will decrease. , has a certain influence on cracking activity and selectivity
In addition, except for the hydrothermal method, other methods are mostly at the cost of loss of molecular sieve yield. Even with the addition of active silicon source, the overall molecular sieve yield is reduced, so it causes waste of aluminum source and may cause Pollution to the environment; while the hydrothermal method has no yield loss, the presence of non-framework aluminum and the loss of crystallinity are also unfavorable factors

Method used

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  • Modification method for Y-type molecular sieve

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0017] With 20g (dry base) industrial NaY molecular sieve (Na 2 O 13.1%, crystallinity 85%, skeletal silicon-aluminum atomic ratio 2.62, Sinopec Changling Catalyst Factory) mixed with 160g glycerin and 200g deionized water, stirred evenly and heated to 150°C for depolymerization for 4h; then depolymerized After the final slurry was allowed to stand and cooled to room temperature, 24g of TPAOH solution (mass fraction 25wt%) was added under vigorous stirring, and after stirring for 30 minutes, 20mL of sodium metaaluminate (Al 2 o 3 Content 190g / L) was added thereinto, continued to stir for 30 minutes and then added 3mL water glass solution (SiO 2 The content is 250g / L, the modulus is 3.3), and the temperature is raised to 70°C under stirring for 2 hours. Subsequently, the above slurry was transferred to a stainless steel crystallization kettle for crystallization at 110°C for 10 h, and the obtained product was filtered, washed, and dried, and then calcined at 550°C for 2 h, an...

Embodiment 2

[0019] Mix 20g (dry basis) industrial NaY molecular sieve (same as above) with 60g glycerol and 160g deionized water, stir evenly and heat up to 180°C for depolymerization for 2 hours; Add 32g TEAOH solution (mass fraction 25wt%) under stirring, stir 80mL aluminum sulfate (Al 2 o 3 Content 90g / L) was added thereinto, and after stirring for 30 minutes, 8.5mL of water glass solution was added, and the temperature was raised to 60°C for aging for 2h while stirring. Subsequently, the above slurry was transferred to a stainless steel crystallization kettle for crystallization at 100°C for 20 hours, and the obtained product was filtered, washed, and dried, and then calcined at 600°C for 2 hours, and the obtained molecular sieve was designated as GYSA-2. The powder diffraction XRD pattern shows that it has the characteristics of a typical Y-type molecular sieve.

Embodiment 3

[0021] Mix 20g (dry basis) industrial NaY molecular sieve (same as above) with 110g glycerin and 200g deionized water, stir evenly and heat up to 100°C for depolymerization for 8 hours; Add 30g of TPAOH solution and 18g of TEAOH solution under stirring, after stirring for 30 minutes, add 80mL of sodium metaaluminate into it at room temperature, continue stirring for 30 minutes, then add 5.5g of tetraethoxy silicon, heat up to 80°C and age for 2h under stirring . Subsequently, the above slurry was transferred to a stainless steel crystallization kettle for crystallization at 100°C for 8 hours, and the obtained product was filtered, washed, and dried, then calcined at 700°C for 2 hours, and the obtained molecular sieve was designated as GYSA-3. The powder diffraction XRD pattern shows that it has the characteristics of a typical Y-type molecular sieve.

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Abstract

A modification method for a Y-type molecular sieve includes the steps of: a) adding water to NaY molecular sieve to pulp the molecular sieve, and adding polyhydroxy alcohol to the molecular sieve according to the alcohol-to-sieve ratio of 1-20:1, and treating the mixture at 80-200 DEG C to prepare slurry A; b) mixing the slurry A with organic alkali to prepare slurry B according to the alkali-to-sieve ratio of 0.1-1:1, and successively adding an aluminum source and a silicon source and aging the mixture to obtain slurry C, wherein the mass ratio of the aluminum source, on the basis of Al2O3, to the NaY molecular sieve is 0.1-1:1, the mass ratio of the silicon source, on the basis of SiO2, to the aluminum source, on the basis of Al2O3, is 0.1-0.5:1, and the silicon source is added after the aluminum source is fully and uniformly mixed with the slurry B; and c) performing hydrothermal crystallization to the slurry C in a sealed reaction kettle and collecting a product. The method can increase the silicon-aluminum ratio of framework of the molecular sieve and improve distribution of acidity, and meanwhile, ensures that the molecular sieve has better hydrothermal structural stability and excellent heavy oil conversion performance.

Description

technical field [0001] The invention relates to a method for modifying a Y-type molecular sieve. Background technique [0002] Since the Y-type molecular sieve was synthesized in the 1960s, it has been widely used in modern industry because of its uniform pore structure, excellent thermal and hydrothermal stability, strong acidity and high catalytic activity. As an important class of microporous catalytic materials, Y-type molecular sieves are also widely used in petroleum refining and processing, such as catalytic cracking, hydrocracking and other reaction processes, Y-type molecular sieves are the most important cracking active group in catalysts Yuan. [0003] The directly synthesized NaY molecular sieve has a high content of sodium oxide. Under high temperature hydrothermal conditions, Na ions will interact with the skeleton aluminum to destroy the molecular sieve structure. Therefore, the synthesized NaY molecular sieve cannot be directly used in refining processes suc...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01J29/08
Inventor 郑金玉王成强罗一斌
Owner CHINA PETROLEUM & CHEM CORP
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