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Preparation method of hydrogenation catalyst composition

A technology of hydrogenation catalyst and composition, which is applied in molecular sieve catalysts, chemical instruments and methods, physical/chemical process catalysts, etc. It can solve the problems of amorphous silicon-aluminum agglomeration, reduction of catalyst specific surface area and pore volume, and influence on catalyst performance, etc. , to achieve the effect of avoiding agglomeration, improving performance and enhancing binding force

Active Publication Date: 2015-11-18
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

[0035] Add 1520g of solid aluminum chloride, 34g of sodium tungstate, and 30g of nickel nitrate into 3.5 liters of distilled water while heating and stirring until dissolved to obtain solution (a). Dilute the concentrated ammonia water into about 10wt% dilute ammonia water (b) by adding an appropriate amount of distilled water, and dissolve 25.2 g of octadecylamine in 350 ml of absolute ethanol to form a solution (c). While stirring, add 64.6g 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%), stirred for 1 hour, filtered, and dried 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 add the system in the tank dropwise to pH=4.0 within 10 minutes, at this time, add Add (d) into the tank, continue to add (b) dropwise, and control the dropwise addition of the tank system to pH=8.0 wit...

Embodiment 2

[0038] Add 1450g of solid aluminum sulfate, 151g of sodium tungstate, and 133g of nickel nitrate into 3.5 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), and dissolve 114.5 g of hexadecylamine in 1 L of ethanol to form a solution (c). While stirring, add 572.5g 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%), stirred for 1 h, filtered to obtain a filter cake, and dried at 110°C for 12 h 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 control the system in the tank to drop to pH=4.0 within 10 minutes, at this time Add (d) to the tank, continue to add (b) dropwise, and control the dropwise addition of the tank system to p...

Embodiment 3

[0041] Add 148g of solid aluminum sulfate, 295g of sodium tungstate, and 260g of nickel nitrate into 1.5 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), 62.2g decylamine was dissolved in 2.5L ethanol to form solution (c). While stirring, add 622g 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%), and stirred for 1 h 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 the system to 8.0, and control it within 45 minutes Finish (a) and (d) dripping. Keep the temperature at 60°C, pH=8.0, age for 1 hour, filter the material in the tank, wash until there is no sulfate ion, wash twice with absolut...

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PUM

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Abstract

The invention discloses a preparation method of a hydrogenation catalyst composition. The method comprises the following steps: adding a mixture of molecular sieves and organic amines before or in the process of preparing an alumina-hydrogenation active metal oxide composite oxide by a coprecipitation method; carrying out aging after gel forming is completed and then carrying out filtration, washing and drying; then carrying out forming, drying and roasting, thus obtaining the hydrogenation catalyst composition. A catalyst prepared by the method can organically combine the molecular sieves and alumina together with good combination degree and dispersion degree, thereby avoiding agglomeration and even blockage of the molecular sieves and amorphous alumina, simultaneously controlling the distribution of the hydrogenation components on various acidic components effectively and improving the usability of the catalyst. The hydrogenation catalyst composition prepared by the method is especially suitable for hydrogenation catalysts with relatively high requirements for acidity and relatively low requirements for hydrogenation properties.

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. 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 ...

Claims

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Application Information

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