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Preparation method of hydrogenation catalyst composition containing molecular sieve

A technology of hydrogenation catalyst and molecular sieve, 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. Achieve the effects of improving performance, avoiding agglomeration, and enhancing binding force

Active Publication Date: 2015-12-16
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 493g of solid aluminum chloride, 11.7g of sodium tungstate, and 10.3g of nickel nitrate into 2.5 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), dissolve 8.2g decylamine in 300ml of absolute ethanol, heat to 60°C, and add 21g 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 Å, and the relative crystallinity is 95%), stirred for 2 hours, filtered, and dried at 100°C for 4 hours to obtain (c). 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 (c) into the tank, continue to add (b) dropwise, and control the dropwise addition of the tank system to pH=8.0 within 30 minutes. Keep the ...

Embodiment 2

[0040] Add 593g of solid aluminum sulfate, 219g of sodium tungstate, and 192g of nickel nitrate into 2.5 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), dissolve 46.8g of hexadecylamine in 300ml of absolute ethanol, heat to 60°C, and add 234.2g 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%), stir for 2 hours, filter, and dry the filter cake at 110°C for 12 hours to obtain (c). 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 = 4.5 within 10 minutes. Add (d) into the tank, continue to add (b) dropwise, and control the dropwise addition of the tank system to pH=8.0 within 30 minutes. Keep ...

Embodiment 3

[0043] Add 234g of solid aluminum sulfate, 233g of sodium tungstate, and 205g 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 20gAl 2 o 3 / l sodium aluminate solution (b), 83.6g of octadecylamine was dissolved in 300ml of absolute ethanol, heated to 60°C, and under stirring, 836.4g 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 Å, and the relative crystallinity is 95%), and stirred for 2 hours to obtain the slurry (c). 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 (c) at the same time, control the pH of the system to 8.0, and control it within 45 minutes Finish (a) and (c) dropwise. Keep the temperature at 60°C, PH=8.0, age for 1 hour, filter the material in the tank to a dry basis content of 15wt%,...

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Abstract

The invention discloses a preparation method of a hydrogenation catalyst composition containing molecular sieves. The method comprises: adding a mixture of molecular sieves and organic amines before or during the preparation of the composite oxide of amorphous alumina and hydrogenation active metal oxides by the co-precipitation method, aging after gel formation, 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 alumina, has a good degree of combination and dispersion, can avoid agglomeration or even blockage between the molecular sieve and amorphous alumina, and effectively control the hydrogenation component The distribution 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. 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): B01J29/16B01J29/78C10G47/20
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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