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A kind of preparation method of beta molecular sieve

A molecular sieve and hydrothermal treatment technology, applied in the field of molecular sieve materials, can solve the problems of mesopores without structure, reduce interaction, and weaken the acidity of molecular sieves, and achieve the effects of high yield, low pour point, and good heterogeneous pour point depressing ability

Active Publication Date: 2021-01-15
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 acid weakening problem 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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  • A kind of preparation method of beta molecular sieve
  • A kind of preparation method of beta molecular sieve
  • A kind of preparation method of beta molecular sieve

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preparation example Construction

[0028]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-processing step in the synthesis process of the aluminum-containing molecular sieve needs to be specially treated. The specific steps are as follows:

[0029](1) Filter the mother liquor after crystallization to form a filter cake with a dry basis content of 5-30%;

[0030](2) Roasting the filter cake directly to obtain a molecular sieve precursor;

[0031](3) subjecting the molecular sieve precursor to hydrothermal treatment;

[0032](4) Filter, wash, and dry the hydrothermal treatment product.

[0033]In step (1), the purpose of filtering the mother liquor after crystallization is to remove the synthetic mother liquor. The present invention specifically limits the dry content of the filter ...

Embodiment 1

[0051](1) Preparation of mother liquor after crystallization

[0052]Take 6.05 mL of white carbon black, 0.51 g of analytically pure aluminum sec-butoxide, and 18.4 mL of tetraethylammonium hydroxide (content 40% by weight) for use. 15 g of deionized water was mixed with tetraethylammonium hydroxide, aluminum sec-butoxide and 37 g of deionized water, and then white carbon black was added, stirred for 1 hour and then transferred to the reactor, and crystallized at 140°C for 120 hours.

[0053](2) Preparation of filter cake

[0054]Filter the crystallization mother liquor prepared in step (1), count the time when there is no filtrate on the filter cake, and continue the suction filtration for 5 minutes to obtain a filter cake F-1. The dry basis content of the filter cake F-1 is 11.2 %, the silicon oxide / alumina molar ratio is 30.2.

[0055](3) Preparation of molecular sieve precursor

[0056]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 co...

Embodiment 2

[0062]The Beta molecular sieve was 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, and molecular sieve precursor C-2 is obtained. Prepared Beta molecular sieve product H-2.

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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 a preparation method and application thereof.Background technique[0002]Molecular sieve material has high acidity and high specific surface area, and is an excellent acid catalyst. At the same time, the molecular sieve material has strong chemical and hydrothermal stability, and it is difficult to be damaged by the corrosion and dissolution of the 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 pore structure parameters such as the specific surface area of ​​the molecular sieve material have an important influence on the catalytic performance of the molecular sieve, so the preparation of molecular sieves with special pores is an important research direction in the chemical industry.[0003]CN1350981A discloses a m...

Claims

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Application Information

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Patent Type & Authority Patents(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