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A kind of preparation method of Y-type molecular sieve with high cracking activity

A technology of cracking activity and molecular sieve, which is applied in the direction of molecular sieve catalysts, chemical instruments and methods, hydrocarbon oil cracking, etc., can solve the problem of not meeting the requirements of high stability and high number of acid centers at the same time, affecting cracking activity or selectivity, B acid Center loss and other issues to achieve the effect of optimized product distribution, moderate product distribution, and high skeleton silicon-aluminum ratio

Active Publication Date: 2019-03-22
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Among them, high-temperature hydrothermal method, coordination chemical method, gas phase and liquid phase extraction of aluminum and silicon replacement method are more researched ultra-stabilization methods. In the process of ultra-stabilization, the skeleton is dealuminated to form hydroxyl holes, and Si-O bonds are replaced. Al-O bonds are inserted into hydroxyl holes to form a more stable Si-O-Si bonded structure, the ratio of silicon to aluminum in the skeleton is increased, and the stability of molecular sieves is enhanced. However, it is inevitable that the hyperstabilization process will affect the acid distribution. Lead to the loss of B acid center, thereby affecting the cracking activity or selectivity
Therefore, the ultra-stabilization process cannot meet the requirements of high stability and high number of acid sites at the same time.

Method used

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  • A kind of preparation method of Y-type molecular sieve with high cracking activity

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Experimental program
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Effect test

Embodiment 1

[0017] With 20g (dry basis) industrial NaY molecular sieve (Na 2 O 12.9%, crystallinity 89%, skeleton silicon-aluminum atomic ratio 2.67, Sinopec Changling Catalyst Factory) mixed with 160g water, added 40g glycerol and treated at 180°C for 4 hours to partially depolymerize the molecular sieve; After the polymerization treatment, the slurry was cooled to room temperature, 32g TPAOH solution (mass fraction 25wt%) was added under stirring, the temperature was raised to 40°C again and 6.4mL water glass solution (SiO 2 content 250g / L, modulus 3.3) into it, continue stirring for a certain period of time and then add 42mL sodium metaaluminate (Al 2 o 3 content of 190g / L), and then heated to 60°C for aging for 2h. Transfer the aged slurry to a crystallization kettle for crystallization at 120°C for 15 hours. After the product is filtered, washed and dried, it is calcined at 550°C for 2 hours to obtain the molecular sieve of the present invention, which is designated as GYC-1. The ...

Embodiment 2

[0019] Mix 20g (dry basis) industrial NaY molecular sieve (same as above) with 200g water, add 130g glycerol and treat at 120°C for 8h; cool the depolymerized slurry to room temperature, add 20g TPAOH solution under stirring, and Add 17mL of water glass solution into it, continue to stir for a certain period of time, and then add 150mL of aluminum sulfate (Al 2 o 3 content 90g / L), the temperature was raised to 70°C and aged for 2h. Transfer the aged slurry to a crystallization kettle for crystallization at 100°C for 20 hours. After filtration, washing and drying, the product is calcined at 650°C for 4 hours to obtain the molecular sieve of the present invention, which is designated as GYC-2. The XRD spectrum shows that it has the structural characteristics of a typical Y-type molecular sieve.

Embodiment 3

[0021] Mix 20g (dry basis) industrial NaY molecular sieve (same as above) with 100g water, add 190g propylene glycol and process at 140°C for 4h; cool the depolymerized slurry to room temperature, add 56g TMAOH solution (mass fraction 25wt% ), heated up to 60°C again and added 25g of tetraethoxy silicon into it, continued to stir for a period of time, then added 84mL of sodium metaaluminate, and continued to age at 60°C for 2h. Transfer the aged slurry to a crystallization kettle for crystallization at 110°C for 10 hours. After the product is filtered, washed and dried, it is calcined at 600°C for 6 hours to obtain the molecular sieve of the present invention, which is designated as GYC-3. The XRD spectrum shows that it has the structural characteristics of a typical Y-type molecular sieve.

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Abstract

A method for preparing Y-type molecular sieves with high cracking activity, which is characterized by including: treating NaY molecular sieves with polyhydric alcohols, depolymerizing and mixing with organic bases, and then adding silicon sources and aluminum sources in sequence and performing aging treatment. Aluminum source press Al 2 O 3 The weight ratio to NaY molecular sieve is 0.1~1:1, and the aluminum source is Al 2 O 3 The silicon source is calculated as SiO 2 The weight ratio is 2 to 10:1. After aging, it is transferred to the crystallization kettle for crystallization again and the product is recovered. This method can not only effectively increase the silicon-aluminum atomic ratio of the molecular sieve skeleton, but also further improve the heavy oil cracking capacity of the molecular sieve and optimize product distribution.

Description

technical field [0001] The invention relates to a preparation method of Y-type molecular sieve with high cracking activity. Background technique [0002] As an important class of microporous catalytic materials, Y-type molecular sieves have been widely used in modern industry since they were synthesized in the 1960s. Y-type molecular sieve is a kind of aluminosilicate with faujasite structure (FAU), which has uniform pore structure, high thermal and hydrothermal stability, strong acidity and high catalytic activity. It is used in petroleum refining and processing such as catalytic cracking In the process of hydrocracking and hydrocracking, Y-type molecular sieve is an extremely important cracking active component. The NaY molecular sieve synthesized by the hydrothermal crystallization method has a high content of sodium oxide. Under high temperature hydrothermal conditions, Na ions will interact with the skeleton aluminum to destroy the structure of the molecular sieve. The...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01J29/08B01J35/02C10G47/20B01J35/00
CPCC10G47/20B01J29/084B01J2229/16B01J2029/081B01J35/00B01J35/30
Inventor 郑金玉罗丁王成强罗一斌
Owner CHINA PETROLEUM & CHEM CORP