Preparation method of hydrogenation catalyst composition containing molecular sieves 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, improving the performance, and responding well to the environment

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

[0039] Add 125g solid aluminum chloride, sodium 74g tungstenate, and 65g nickel nitrate to 1.5 liter distilled water, while heating and stirring until dissolved, obtaining the solution (A).Add the thick ammonia water to the appropriate amount of distilled water to dilute to about 10WT%of the ammonia water (B), and 19.1g of xylitol dissolve in 500ml water to form a solution (C).Take 10L water glass (industrial grade, the number of molds is 3.0) diluted in 20L to remove ion water and configure the solution (d).4.1 g diaoline is dissolved in 100ml of water, heated to 60 ° C, add 10.6GY molecular sieve Y-1 (SIO (SIO (SIO 2 / Al 2 O 3 The Moore is 11.0, the crystal cells are 24.42?, The relative crystallinity is 95 %), the pulp for 2 hours, and the slurry (e) is obtained.Take the one -dollar rubber tank, add (a) to the tank and stir to heated to 65 ° C, open the valve with (b) container, control the tank system to pH = 4.5 within 10 minutes.(B), open valves with (C) and (E) containers, ...

Embodiment 2

[0042] Add 125g solid sulfate, sodium 88g tungstenate, and 77g nickel nitrate to 1.5 liter distilled water, while heating and stirring until dissolved to obtain the solution (A).Add the thick ammonia water to the appropriate amount of distilled water to dilute to about 10%dilute ammonia (B), and 37.2g of self -dysic acid dissolved in 500ml water to form a solution (C).Take 10L water glass (industrial grade, the number of molds is 3.0) diluted in 20L to remove ion water and configure the solution (d).19.7 g, ethanhanlamine dissolved in 100ml water, heated to 60 ° C, add 98.7GY molecular sieve Y-1 (SIO (SIO (SIO 2 / Al 2 O 3 The Moore is 11.0, the crystal cells are 24.42?, The relative crystallinity is 95 %), the pulp for 2 hours, and the slurry (e) is obtained.Take the one -piece rubber tank, add (a) to the tank and stir it to 65 ° C, open the valve with (b) container, and control the system in the tank to pH = 4.5 within 10 minutes. At this timeAdd to the tank, continue to add (b) ...

Embodiment 3

[0045] Add 125g solid aluminum sulfate, sodium 222g tungstenate, 196g nickel nitrate to 1.5 liter distilled water, heat and stir until dissolved, and obtain the solution (A).Matching sodium aluminate to make a concentration of 20g Al 2 O 3 / l sodium aluminate solution (B).89.4g 1,4-buty-diic acid is dissolved in 1L of water to form a solution (C).76.6g acetramlamine dissolved in 500ml water, heated to 60 ° C, add 766GY molecular sieve Y-1 (SIO (SIO (SIO 2 / Al 2 O 3The Moore is 11.0, the crystal cell constant is 24.42?, The relative crystallization is 95 %), and the slurry (d) is obtained after continuing stirring for 2 hours.Take 10L water glass (industrial grade, the number of molds is 3.0) diluted in 20L to remove ion water and configure the solution (E).Take a 10 % rubber tank, put it in 2L -remove water and stir to 65 ° C. At the same time, open the valves of the container with (a), (b), (c), and (d) at the same time.Drop (a) (c) and (d) within 45 minutes.Keep the temperature ...

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Abstract

The invention discloses a preparation method of a hydrogenation catalyst composition containing molecular sieves and amorphous silica-alumina. The method comprises the following steps: adding a mixture of the 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 hydrothermal treatment, 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, agglomeration and even blockage of the molecular sieves and amorphous silica-alumina can be avoided, simultaneously control the distribution of hydrogenation components on various acidic components effectively and improve 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 present invention involves a preparation method of a hydrogenation catalyst composition, especially for preparation methods for hydrogenation catalyst compositions containing molecular sieves and non -fixed silica aluminum aluminum. Background technique [0002] Hydrogenation technology is one of the important means of secondary processing of crude oil and light oil.Because it has the characteristics of strong raw materials, flexible production operations and product solutions, and good product quality, it has become an important way to produce high -quality lightweight clean oil products and solve the source of chemical raw materials. [0003] The hydrogenation catalyst is generally a dual -function catalyst. The cracking activity and hydrogenation activity are provided by the acidic components and the hydrogenation activity component in the catalyst. [0004] The acid components in the catalyst are generally provided by the molecular sieve contained i...

Claims

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Application Information

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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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