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A kind of hydrocracking catalyst for producing heavy naphtha and jet fuel and its preparation method and application

A technology for hydrocracking and heavy naphtha, applied in the direction of organic compound/hydride/coordination complex catalyst, physical/chemical process catalyst, molecular sieve catalyst, etc., can solve the problem of increasing auxiliary equipment, large loss of specific surface area and pore volume , the skeleton structure is easy to collapse and other problems, to achieve the effect of improving the dispersion and improving the reactivity

Active Publication Date: 2021-06-01
PETROCHINA CO LTD
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  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0017] The preparation methods of micro-mesoporous composite materials mentioned in the above documents or patents are either complicated in process or take a long time in the synthesis process
CN102000604A introduces a microwave treatment process in the process of synthesizing Y / MCM-41 composite molecular sieve, increases auxiliary equipment, and greatly increases the cost of synthesizing composite molecular sieve
In addition, the mesoporous part in the micro-mesoporous composite material mentioned in the above documents or patents is irregular pores
In the above patents, heteropolyacids are generally loaded or mixed with macroporous amorphous structure materials such as alumina and silica-alumina, but these materials have relatively low specific surface area compared with regular and ordered mesoporous materials, which reduces the specific surface area of ​​heteropolyacids. Catalytic activity
Due to the small pore size of microporous molecular sieves and relatively large heteropolyacid molecules, the loss of specific surface area and pore volume after loading is large, and it is difficult to exert catalytic activity.
The mesoporous molecular sieves developed in recent years have greatly improved the specific surface area, pore volume and pore size of molecular sieves. However, mesoporous molecular sieves such as SBA-15 and MCM-41 have poor thermal stability. Collapse, prone to permanent loss of catalytic activity

Method used

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  • A kind of hydrocracking catalyst for producing heavy naphtha and jet fuel and its preparation method and application
  • A kind of hydrocracking catalyst for producing heavy naphtha and jet fuel and its preparation method and application
  • A kind of hydrocracking catalyst for producing heavy naphtha and jet fuel and its preparation method and application

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preparation example Construction

[0033] The present invention provides a kind of preparation method of the hydrocracking catalyst of prolific heavy naphtha and jet fuel, at first synthesizing directing agent, adopting hydrothermal crystallization method to synthesize Y / TS-1 / APO-5 composite molecular sieve, then in Y / Add surfactant, basic aluminum source and / or basic silicon source solution to the slurry of TS-1 / APO-5 molecular sieve, and the product is washed, dried and calcined to obtain mesoporous Y / TS-1 / APO-5 / ASA composite. then H 3 PMo 12-x PR x o 40 ·nH 2 The O heteropolyacid aqueous solution is mixed with the mesoporous Y / TS-1 / APO-5 / ASA composite material, then alumina and nitric acid are added, and the hydrocracking catalyst is obtained after kneading, rolling, extruding, drying and roasting. The catalyst can process heavy raw oil, and can produce more heavy naphtha and jet fuel.

[0034] The preparation method of the prolific heavy naphtha and jet fuel hydrocracking catalyst specifically compr...

Embodiment 1

[0054] Embodiment 1: the synthesis of Y / TS-1 / APO-5 / ASA composite material

[0055] (1) Preparation of guiding agent: Take 24.7g of sodium hydroxide (Beijing Chemical Plant, analytically pure) and add it to 45.9 g of water, stir until the sodium hydroxide is completely dissolved, then add 6.5g of sodium metaaluminate (researched by Shandong Aluminum Industry Co., Ltd. Institute, Industrial Products, Al 2 o 3 Content 49.1wt%), stir until sodium metaaluminate completely dissolves, get sodium metaaluminate solution A, in solution A, Al 2 o 3 The content is 3.8wt%, Na 2 The O content is 20 wt%. With 70g solution A and 100g water glass (Beijing Red Star Soda Soda Factory, SiO 2 Content 27.81wt%, Na 2 O content 8.74wt%) was poured into 65.5g of deionized water successively, stirred evenly, and aged at 30° C. for 22 hours to obtain the directing agent. The molar ratio of each component of the directing agent is: 16Na 2 O: Al 2 o 3 :16SiO2 2 :330H 2 O.

[0056] (2) Prepara...

Embodiment 2

[0060] Unless otherwise specified, the sources of each raw material are the same as in Example 1.

[0061] (1) Preparation of guiding agent: Take 11.4g of sodium hydroxide and add it to 45.9g of water, stir until the sodium hydroxide is completely dissolved, then add 4g of sodium metaaluminate, and stir until the sodium metaaluminate is completely dissolved to obtain sodium metaaluminate Solution A, Al in solution A 2 o 3 The content is 2.5wt%, Na 2 The O content is 9 wt%. Pour 70g of solution A and 90g of water glass into 65.5g of deionized water in sequence, stir well, and then statically age at 30°C for 22 hours to obtain the directing agent. The molar ratio of each component of the directing agent is: 14Na 2 O: Al 2 o 3 :16SiO2 2 :330H 2 O.

[0062] (2) Preparation of TS-1 and APO-5 molecular sieve slurry: according to the ratio of TS-1 molecular sieve: APO-5 molecular sieve: aqueous solution is 1:2:7, 1g of TS-1 molecular sieve and 2g of APO-5 molecular sieve are...

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Abstract

The invention provides a hydrocracking catalyst capable of producing heavy naphtha and jet fuel and its preparation method and application. The method comprises: synthesizing a directing agent first, and then synthesizing Y / TS‑1 / APO‑1 by hydrothermal crystallization 5 composite molecular sieve, then add surfactant, alkaline aluminum source and / or alkaline silicon source solution to the slurry of Y / TS‑1 / APO‑5 molecular sieve, and the product is washed, dried and roasted to obtain mesoporous Y / TS‑1 / APO‑5 / ASA composite. then H 3 PMo 12‑ x PR x o 40 ·nH 2 The O heteropoly acid aqueous solution is mixed with the mesoporous Y / TS-1 / APO-5 / ASA composite material, then alumina and nitric acid are added, and the hydrocracking catalyst is obtained after kneading, rolling, extruding, drying and roasting. The catalyst can process heavy raw oil, and can produce more heavy naphtha and jet fuel.

Description

technical field [0001] The invention relates to a preparation method of a hydrocracking catalyst capable of producing heavy naphtha and jet fuel. Background technique [0002] Molecular sieve complex refers to a composite material that combines molecular sieves and other substances through the interaction between molecules, atoms or ions. Regular materials with mesoporous structures such as MCM-41 mesoporous molecular sieves are suitable for the transformation of organic macromolecules due to their large pore structure, but their poor thermal stability, hydrothermal stability and weak acidity limit their Applications of this type of material in the field of catalysis. The research on microporous-mesoporous composite materials based on high stability and strong acidic microporous molecular sieves has important industrial application value. [0003] With the continuous development of catalytic applications of molecular sieves, single-channel molecular sieves can no longer me...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01J31/38B01J29/89C10G47/20
CPCB01J29/005B01J29/08B01J29/83B01J29/89B01J2229/20C10G47/20
Inventor 李海岩谢方明孙发民姜维曲云龙张全国丛丽茹赵檀关旭董春明王亮秦丽红马守涛吴显军张文成郭金涛王刚焦庆雨孙宏磊李军吕倩王甫村
Owner PETROCHINA CO LTD
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