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

A hydrogenation catalyst and amorphous silica-alumina technology, which is applied in the direction of molecular sieve catalysts, catalyst carriers, chemical instruments and methods, etc., can solve problems such as blockage of molecular sieves, easy access to each other's channels, and amorphous silica-alumina agglomeration, etc., to improve the use of Performance, improved utilization, enhanced bonding effect

Active Publication Date: 2015-01-14
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

In this method, amorphous silicon-alumina is prone to agglomeration, and it is also easy to enter the pores of the other party or block the orifice of the molecular sieve, which affects the distribution of amorphous silicon-alumina on the molecular sieve, and the connectivity between molecular sieve and amorphous silicon-alumina channels is poor. The specific surface area and pore volume of the catalyst are reduced, and the distribution of the active metal of the catalyst is uneven, which affects the performance of the catalyst

Method used

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

Examples

Experimental program
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Embodiment 1

[0034] 255g of solid aluminum chloride was added to 1.5 liters of distilled water while heating and stirring until dissolved to obtain aluminum chloride solution (a). Add an appropriate amount of distilled water to the concentrated ammonia water to dilute it into about 10% dilute ammonia water (b), dissolve 8g of octadecylamine in 120ml of absolute ethanol, and add 20g of modified 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 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 250ml of solution (c) into the tank, continue to add (b) dropwise, and control the dropwis...

Embodiment 2

[0037] 266g of solid aluminum sulfate was added to 1.2 liters of distilled water while heating and stirring until dissolved to obtain aluminum sulfate solution (a). Add an appropriate amount of distilled water to the concentrated ammonia water and dilute it into about 10% dilute ammonia water (b), dissolve 21g hexadecylamine in 200ml absolute ethanol, add 104g modified 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 Å, 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 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, open the storage The valve of the container of (c), continue to drop (b), control the dropwise addition of the system in t...

Embodiment 3

[0040]255g of solid aluminum sulfate was added to 1.2 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), 98g decylamine is dissolved in 2.5L absolute ethanol, adds 979g modified 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 Å, and the relative crystallinity is 95%), and the slurry (c) is obtained. Take 10L of water glass (industrial grade, modulus 3.0) and dilute it in 20L of deionized water to prepare solution (d). Take a stainless steel reaction tank, put in 2l deionized water, stir and heat 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 staying for 20 minutes, ...

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Abstract

The invention discloses a preparation method of a hydrogenation catalyst containing a molecular sieve and amorphous silica-alumina. The preparation method comprises the following steps of preparing a catalyst carrier material and introducing a hydrogenation active component by a dipping method or a coprecipitation method to obtain the hydrogenation catalyst. The preparation process of the catalyst carrier material comprises the followings steps of adding a mixture of a molecular sieve and an organic amine into amorphous silica-alumina in gelling, after gelling of the amorphous silica-alumina, carrying out aging, then carrying out hydrothermal treatment and then carrying out filtration, washing and drying to obtain the catalyst carrier material. The preparation method realizes ordered arrangement and uniform deposition of silica-alumina on the surface of the molecular sieve, improves the binding strength of the molecular sieve and the silica-alumina, avoids agglomeration of the amorphous silica-alumina and the molecular sieve and channel blocking caused by the agglomeration, realizes mutual communication of channels of the silica-alumina and the molecular sieve, fully develops synergism of the silica-alumina and the molecular sieve, and improves catalyst use performances. The hydrogenation catalyst can be used for various hydrogenation technologies.

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 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, and it has been widely used at present. [0003] The acidic component in the catalyst is generally provided by molecular sieves and / or amorphous silica-alumina (hereinafter referred to as amorphous silica-alumina) and amorphous alumina contained in the catalyst. For molecular sieves, amorphous silica-alumina, and amorphous alumina, the order of acidity decreases in order, while the concentration of pore distribution increases in order, which determines the three in the catalyst. Each exhibits different characteristics and advantages. Amorphous alumina has high specific surface area, good sintering r...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01J29/16B01J29/78B01J32/00C10G47/20
Inventor 蒋广安张晔方向晨王继锋
Owner CHINA PETROLEUM & CHEM CORP
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