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Preparation method of hydrogenation catalyst composition containing molecular sieve and amorphous silica-alumina

A hydrogenation catalyst, amorphous silica-alumina technology, applied in the direction of molecular sieve catalysts, chemical instruments and methods, physical/chemical process catalysts, etc., can solve the problem of amorphous silica-alumina agglomeration, catalyst specific surface area and pore volume reduction, affecting catalyst performance and other issues to achieve the effect of enhancing the binding force and improving the performance

Active Publication Date: 2016-02-10
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 129g of solid aluminum chloride, 86.5g of sodium tungstate, and 76.3g of nickel nitrate into 2 liters of distilled water while heating and stirring until dissolved to obtain solution (a). Add an appropriate amount of distilled water to the concentrated ammonia water and dilute it into about 10wt% dilute ammonia water (b), dissolve 4.3g of hexadecylamine in 200ml of absolute ethanol, add 11g of 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%) to form a solution (c). Take 10L of water glass (industrial grade, modulus 3.0) and dilute it in 20L of deionized water to prepare solution (d). Take a plastic tank, add (a) into the tank, stir and heat to 65°C, open the valve of the container containing (b), and add the system in the tank dropwise to pH=4.5 within 10 minutes. Add 250ml of solution (c) into the tank, continue to add (b) dropwise, and control the dropwise addition of t...

Embodiment 2

[0040] Add 129g of solid aluminum sulfate, 93g of sodium tungstate, and 82g of nickel nitrate into 2 liters of distilled water while heating and stirring until dissolved to obtain solution (a). Add an appropriate amount of distilled water to the concentrated ammonia water and dilute it into about 10wt% dilute ammonia water (b), dissolve 23g of cetylamine in 200ml of absolute ethanol, add 115.3g of 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%) beating to form a slurry (c). Take 10L of water glass (industrial grade, modulus 3.0) and dilute it in 20L of deionized water to prepare solution (d). Take a plastic tank, add (a) into the tank, stir and heat to 65°C, open the valve of the container containing (b), control the system in the tank to drop to pH=4.5 within 10 minutes, open the storage The valve of the container of (c), continue to drop (b), control the dropwise addition of the...

Embodiment 3

[0043] Add 129g of solid aluminum sulfate, 551g of sodium tungstate, and 486g of nickel nitrate into 2 liters of distilled water while heating and stirring until dissolved to obtain solution (a). Prepare the solid sodium metaaluminate to a concentration of 20gAl 2 o 3 / l sodium aluminate solution (b), 109g dodecylamine is dissolved in 2.5L absolute ethanol, adds 1090gY 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%) beating to prepare the slurry (c). Take 10L of water glass (industrial grade, modulus 3.0) and dilute it in 20L of deionized water to prepare solution (d). Take a glue tank, put 2l of deionized water into it, stir and heat it to 65°C, open the valves of the containers (a), (b) and (c) at the same time, control the pH of the system to 8.0, and control the pH of the system within 45 minutes (a) (c) and (d) drop off. Keep the temperature at 65°C, pH=8.0, and after stayin...

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PUM

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Abstract

The invention discloses a preparation method of a hydrogenation catalyst composition containing molecular sieve and amorphous silicon aluminum. The method comprises: adding a mixture of molecular sieves and organic amines before or during the preparation of amorphous silica-alumina and hydrogenation active metal oxide composite oxides by co-precipitation, aging after gel formation, and then performing hydrothermal treatment, and filtering , washing, drying, shaping, drying and roasting to obtain a hydrogenation catalyst composition. The catalyst prepared by this method can organically combine the molecular sieve and the amorphous silica-alumina, has a good degree of combination and dispersion, can avoid agglomeration or even blockage between the molecular sieve and the amorphous silica-alumina, and effectively controls hydrogenation The distribution of components on each acidic component improves the performance of the catalyst. The hydrogenation catalyst composition prepared by the method of the invention is particularly suitable for hydrogenation catalysts with relatively high requirements on acidity and relatively low requirements on hydrogenation performance.

Description

technical field [0001] The invention relates to a method for preparing a hydrogenation catalyst composition, in particular to a method for preparing a hydrogenation catalyst composition containing molecular sieves and amorphous silicon-alumina. 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 con...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01J29/16B01J29/78C10G47/20
Inventor 蒋广安刘雪玲李宝忠张晔郑庆华王继锋
Owner CHINA PETROLEUM & CHEM CORP
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