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Beta molecular sieve, preparation method, and application thereof

A technology of molecular sieve and alumina, which is applied in molecular sieve catalysts, chemical instruments and methods, physical/chemical process catalysts, etc., can solve the problems of molecular sieves such as weakened acidity, reduced interaction, and lack of mesopore structure, so as to achieve low pour point, Good heterogeneous pour point depressing ability and high yield

Active Publication Date: 2019-05-03
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

[0005] CN104353484A discloses a preparation method of cheap strongly acidic hierarchically porous Beta zeolite, relates to a preparation method of hierarchically porous Beta zeolite, which solves the problem of weakening the acidity of the existing desiliconization post-treatment hierarchically porous Beta zeolite molecular sieve
The seed crystal selected in this invention is a microporous molecular sieve, which is added to the preparation system after silanization, and its hydrophobicity is used to increase its effect on the hydrophobic end of the surfactant micelle, thereby reducing the interaction between the two directing agents. However, the formed mesopores still do not have a regular structure, and whether the addition of seed crystals reduces the amount of templating agent has not been reported.

Method used

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  • Beta molecular sieve, preparation method, and application thereof
  • Beta molecular sieve, preparation method, and application thereof
  • Beta molecular sieve, preparation method, and application thereof

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preparation example Construction

[0034] The invention also provides a preparation method of the Beta molecular sieve. Generally, the preparation of aluminum-containing molecular sieves can be divided into steps such as gelation, crystallization, and post-treatment. In order to obtain the Beta molecular sieve of the present invention, the post-treatment step in the synthesis process of the aluminum-containing molecular sieve needs to be specially treated, and the specific steps are as follows:

[0035] (1) filtering the crystallized mother liquor to form a filter cake with a dry basis content of 5-30%;

[0036] (2) directly roasting the filter cake to obtain a molecular sieve precursor;

[0037] (3) subjecting the molecular sieve precursor to hydrothermal treatment;

[0038] (4) Filtrating, washing and drying the hydrothermally treated product.

[0039] In step (1), the purpose of filtering the crystallized mother liquor is to remove the synthesis mother liquor. The present invention specifically limits th...

Embodiment 1

[0057] (1) Preparation of mother liquor after crystallization

[0058] Take 6.05 mL of white carbon black, 0.51 g of analytically pure aluminum sec-butoxide, and 18.4 mL of tetraethylammonium hydroxide (40% by weight) for use. Mix 15 grams of deionized water with tetraethylammonium hydroxide, aluminum sec-butoxide and 37 grams of deionized water, then add white carbon black, stir for 1 hour, then transfer to a reaction kettle, and crystallize at 140°C for 120 hours.

[0059] (2) Preparation of filter cake

[0060] Filter the mother liquor after crystallization prepared in the operation (1), and continue suction filtration for 5 minutes when there is no filtrate on the filter cake, and obtain the filter cake F-1, which has a dry basis content of 11.2 %, the silica / alumina molar ratio is 30.2.

[0061] (3) Preparation of molecular sieve precursor

[0062] The filter cake F-1 was raised from room temperature to 450° C. at a heating rate of 25° C. / min, and kept at a constant te...

Embodiment 2

[0069] Beta molecular sieves were prepared according to the method of Example 1, except that in step (3), the filter cake F-1 was raised from room temperature to 350° C. at a heating rate of 5° C. / min, and kept at a constant temperature for 14 hours. During the heating process, the roasting furnace is a closed roasting furnace to obtain the molecular sieve precursor C-2. Beta molecular sieve finished product H-2 was obtained.

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Abstract

The invention relates to the field of molecular sieve materials and particularly relates to a beta molecular sieve, a preparation method, and an application thereof. The molar ratio of silicon oxide to aluminum oxide of the molecular sieve is 120-300. The molecular sieve has a mesoporous structure; a closed hysteresis loop exists at the position P / P0 = 0.4-0.99 on a low temperature nitrogen adsorption-desorption curve, the start position of the closed hysteresis loop being at the position P / P0 = 0.4-0.7. A catalyst with the beta molecular sieve being a solid acid has excellent isomerizing pourpoint depression effect. A target product in products is high in yield and low in pour point.

Description

technical field [0001] The invention relates to the field of molecular sieve materials, in particular to a Beta molecular sieve and its preparation method and application. Background technique [0002] Molecular sieve material has high acidity and high specific surface area, and is an excellent acidic catalyst. At the same time, molecular sieve materials have strong chemical stability and hydrothermal stability, and are difficult to be destroyed by corrosion and dissolution of reactants. Compared with commonly used homogeneous catalysts, molecular sieve material catalysts can be directly reused without separation, and will not pollute the environment and products. The specific surface area and other pore structure parameters of molecular sieve materials have an important influence on the catalytic performance of molecular sieves. Therefore, the preparation of molecular sieves with special channels is an important research direction in the chemical industry. [0003] CN1350...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C01B39/04B01J29/74
Inventor 毕云飞夏国富杨清河黄卫国郭庆洲方文秀
Owner CHINA PETROLEUM & CHEM CORP