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Method for preparing 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 enhancing the binding force, responding well to the environment and 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 218g of solid aluminum chloride, 11g of sodium tungstate, and 9g of nickel nitrate into 1 liter of distilled water while heating and stirring until dissolved to obtain solution (a). The concentrated ammonia water was diluted with an appropriate amount of distilled water to form about 10wt% dilute ammonia water (b), and 33.3 g of xylitol was dissolved in 500 ml of water 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). Dissolve 7.2g of diethanolamine in 100ml of water, heat to 60°C, add 18.5g of Y-type molecular sieve Y-1 (SiO 2 / Al 2 o 3 =11.0, unit cell constant is 24.42 Å, relative crystallinity is 95%) beating for 2 hours to obtain slurry (e). Take a stainless steel reaction 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, and continue to drop (b)...

Embodiment 2

[0040] Add 330g of solid aluminum sulfate, 74g of sodium tungstate, and 65g of nickel nitrate into 1 liter 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 98.3g of 1,4-butanediol in 500ml of water 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). Dissolve 52.1g of ethanolamine in 100ml of water, heat to 60°C, add 260.6g of Y-type molecular sieve Y-1 (SiO 2 / Al 2 o 3 =11.0, unit cell constant is 24.42 Å, relative crystallinity is 95%) beating for 2 hours to obtain slurry (e). Take a stainless steel reaction tank, add (a) into the tank, stir and heat to 65°C, open the valve of the container containing (b), and control the system in the tank to drop to pH=4.5 within 10 minutes, at this time, add Add...

Embodiment 3

[0043] Add 211g of solid aluminum sulfate, 901.9g of sodium tungstate, and 795.1g of nickel nitrate into 1 liter of distilled water while heating and stirring until dissolved to obtain solution (a). Prepare the solid sodium metaaluminate to a concentration of 20g Al 2 o 3 / l sodium aluminate solution (b). 150.8 g of 1,4-butanedioic acid was dissolved in 1 L of water to form solution (c). 178.3g of ethylenediamine was dissolved in 500ml of water, heated to 60°C, and 1783g of Y-type molecular sieve Y-1 (SiO 2 / Al 2 o 3 =11.0, the unit cell constant is 24.42 Å, and the relative crystallinity is 95%), and the slurry (d) is obtained after stirring for 2 hours. Take 10L water glass (industrial grade, modulus 3.0) and dilute it in 20L deionized water to prepare solution (e). Take a steel reaction tank, put 2l of deionized water into it, stir and heat it to 65°C, open the valves of the containers containing (a), (b), (c) and (d) at the same time, and control the pH of the system...

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PUM

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Abstract

The invention discloses a method for preparing a hydrogenation catalyst composition. The method comprises the following steps: adding a mixture of molecular sieves and organic amines as well as organic alcohols and / or organic acids before or in the process of preparing an amorphous silica-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 amorphous silica-alumina together with good combination degree and dispersion degree, thereby avoiding agglomeration and even blockage of the molecular sieves and amorphous silica-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, especially 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 refrac...

Claims

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Application Information

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IPC IPC(8): B01J29/16B01J29/78C10G47/20
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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