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Preparation method of hydrogenation catalyst

A hydrogenation catalyst, hydrogenation activity technology, applied in molecular sieve catalysts, chemical instruments and methods, physical/chemical process catalysts, etc. Problems such as incompatibility with the cracking function to achieve the effect of improving the performance

Active Publication Date: 2014-05-21
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Among them, the carrier material is prepared by directly adding molecular sieves in the process of forming amorphous silica-alumina. In this way, amorphous silica-alumina is prone to agglomeration, and it is also easy to enter the pores of the other party or block the pores of molecular sieves, which affects the amorphous silica-alumina. The distribution on the molecular sieve, the poor connectivity between the molecular sieve and the amorphous silica-alumina channel, reduces the specific surface area and pore volume of the catalyst, and the distribution of active metals is not easy to control, which makes the hydrogenation function of the catalyst mismatch with the cracking function, affecting the catalyst performance

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0037] Add 800 g of solid aluminum chloride into 3.5 liters of distilled water while heating and stirring until dissolved to obtain solution (a). Concentrated ammonia water is added appropriate amount of distilled water and is diluted into about 10wt% dilute ammonia water (b), 42g Y type molecular sieve Y-1 (SiO 2 / Al 2 o 3 The molar ratio is 11.0, the unit cell constant is 24.42?, and the relative crystallinity is 95%). Use an impregnation solution containing 18g sodium tungstate and 16g nickel nitrate hexahydrate for saturated impregnation, dry at 120°C for 180 minutes after impregnation, and bake at 500°C 4 hours; 16g of octadecylamine was dissolved in 350ml of absolute ethanol to form a solution (c). While stirring, add metal-containing Y molecular sieve to (c) and stir for 1 hour, filter, and dry the filter cake at 100° C. for 4 hours to obtain (d). Take a plastic tank, add (a) into the tank, stir and heat to 60°C, open the valve of the container containing (b), and ad...

Embodiment 2

[0040] 800g of solid aluminum sulfate was added to 3.5 liters of distilled water while heating and stirring until dissolved to obtain aluminum sulfate solution (a). Concentrated ammonia water is added appropriate amount of distilled water and is diluted into about 10wt% dilute ammonia water (b), 195gY type molecular sieve Y-1 (SiO 2 / Al 2 o 3 The molar ratio is 11.0, the unit cell constant is 24.42?, and the relative crystallinity is 95%) use an impregnation solution containing 233g sodium tungstate and 205g nickel nitrate hexahydrate for saturated impregnation, dry at 120°C for 180 minutes after impregnation, and bake at 500°C 4 hours; 39 g of hexadecylamine was dissolved in 1 L of ethanol to form solution (c). Under stirring, add metal-containing molecular sieves to (c), stir for 1 hour, filter, and dry the filter cake at 110°C for 12 hours to obtain (d). Take a plastic tank, add (a) into the tank, stir and heat to 60°C, open the valve of the container containing (b), and...

Embodiment 3

[0043] 730g of solid aluminum sulfate was added to 1.5 liters of distilled water while heating and stirring until dissolved to obtain aluminum sulfate solution (a). Prepare the solid sodium metaaluminate to a concentration of 20g Al 2 o 3 / l sodium aluminate solution (b), 1848g Y-type molecular sieve Y-1 (SiO 2 / Al 2 o 3 The molar ratio is 11.0, the unit cell constant is 24.42?, and the relative crystallinity is 95%) use an impregnation solution containing 636g sodium tungstate and 560g nickel nitrate hexahydrate for saturated impregnation, dry at 120°C for 180 minutes after impregnation, and bake at 500°C 4 hours; 185 g of decylamine was dissolved in 2.5 L of ethanol to form solution (c). In the state of stirring, add the metal-modified molecular sieve into (c), and stir for 1 hour to obtain (d). Take a glue tank, put 1L of deionized water into it, stir and heat it to 60°C, open the valves of the containers containing (a), (b) and (d) at the same time, control the pH of ...

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Abstract

The invention discloses a preparation method of a hydrogenation catalyst. The method comprises the following steps: adding a mixture of molecular sieves containing hydrogenation active metal components and organic amines in the amorphous alumina gel forming process; aging after amorphous alumina gel forming is completed and then carrying out filtration, washing and drying; then carrying out forming, drying and roasting, thus obtaining the hydrogenation catalyst. By adopting the method, the molecular sieves and alumina can be organically combined together with good combination degree and dispersion degree, agglomeration and even blockage of the molecular sieves and amorphous alumina can be avoided, and meanwhile, the hydrogenation and cracking functions of the catalyst can be effectively adjusted and the usability of the catalyst can be improved. The catalyst prepared by the method is suitable for the shallow cracking and deep hydrogenation processes.

Description

technical field [0001] The invention relates to a method for preparing a hydrogenation catalyst, in particular to a method for preparing a hydrogenation catalyst containing molecular sieves. Background technique [0002] Hydrocracking technology is one of the important means for the secondary processing of crude oil and the lightening of heavy oil. Because of its strong adaptability to raw materials, flexible production operations and product solutions, and good product quality, it has become an important way to produce high-quality light clean oil products and solve the source of chemical raw materials. [0003] Hydrocracking catalysts are generally dual-functional catalysts, and their cracking activity and hydrogenation activity are respectively provided by the acidic component and hydrogenation active component in the catalyst. [0004] The acidic component of the catalyst is generally provided by molecular sieves contained in the catalyst and / or refractory inorganic oxi...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01J29/076B01J29/16B01J29/78C10G47/20
Inventor 蒋广安张晔郑庆华刘雪玲李宝忠王继锋
Owner CHINA PETROLEUM & CHEM CORP
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