Preparation method of hydrogenation catalyst containing molecular sieves

A hydrogenation catalyst, molecular sieve technology, applied in molecular sieve catalysts, chemical instruments and methods, physical/chemical process catalysts, etc. Blocking of molecular sieves and other problems to achieve the effect of enhancing binding force and improving 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

[0041] 1164 g of solid aluminum chloride was added to 3 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 and dilute it into about 10wt% dilute ammonia water (b), and dissolve 89g of mannitol in 300ml of water to form a solution (c). 78.6g 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%). Use an impregnation solution containing 36g sodium tungstate and 32g nickel nitrate hexahydrate for saturated impregnation, dry at 120°C for 180 minutes after impregnation, and bake at 500°C 4 hours; 30.6g of ethylenediamine was dissolved in 300ml of absolute ethanol, heated to 60°C, stirred for half an hour, added metal-containing Y molecular sieve, continued to stir for 2 hours, and filtered to obtain a modified molecular sieve (d ). Take a plastic tank, add...

Embodiment 2

[0044] 1074g of solid aluminum sulfate was added to 3 liters of distilled water while heating and stirring until dissolved to obtain aluminum sulfate solution (a). Dilute the concentrated ammonia water into about 10wt% dilute ammonia water (b) by adding an appropriate amount of distilled water, and dissolve 160g of 1,4-butanediol in 1L of water to obtain a solution (c). 391g 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%) use an impregnation solution containing 405g sodium tungstate and 357.3g nickel nitrate hexahydrate for saturated impregnation, after impregnation, dry at 120°C for 180 minutes, 500°C Roast for 4 hours; dissolve 78g of 1,4-butanediamine in 1L of water, heat to 60°C, stir for half an hour, add metal-containing molecular sieves, and stir for 2 hours to obtain molecular sieve slurry (d). Take a plastic tank, add (a) into the tank, stir and heat to 60°C, open the valv...

Embodiment 3

[0047] 187g of solid aluminum sulfate was added to 7L 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), 66.8g of 1,3-propanediol was dissolved in 300ml of water to form solution (c). 39.3g Y-type molecular sieve Y-1 (SiO 2 / Al 2 o 3The molar ratio is 11.0, the unit cell constant is 24.42?, and the relative crystallinity is 95%) use an impregnation solution containing 54.7g sodium tungstate and 48.2g nickel nitrate hexahydrate for saturated impregnation, and dry at 120°C for 180 minutes after impregnation, 500 Roast at ℃ for 4 hours; dissolve 3.93g of diethanolamine in 6L of water, heat to 60℃, add metal-containing molecular sieve under stirring, continue stirring at the temperature for 2 hours, and filter to obtain treated molecular sieve (d). Take a glue tank, put 2l of deionized water into it, stir and heat to 6...

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Abstract

The invention discloses a preparation method of a hydrogenation catalyst containing molecular sieves. The method comprises the following steps: adding a mixture of the molecular sieves containing hydrogenation active metal components and organic amines as well as organic alcohols and / or organic acids in the amorphous alumina gel forming process; carrying out aging after amorphous alumina 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. By adopting the method, the molecular sieves and alumina can be organically combined together with good combination degree and dispersion degree, agglomeration and even blockage of the molecular sieves and amorphous alumina can be avoided, and meanwhile, the hydrogenation and cracking functions of the catalyst can be effectively adjusted and the usability of the catalyst can be improved. The catalyst prepared by the method is suitable for the shallow cracking and deep hydrogenation processes.

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. 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 refractory inorganic oxi...

Claims

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Application Information

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IPC IPC(8): B01J29/16B01J29/78C10G47/20
Inventor 张晔蒋广安郑庆华刘雪玲李宝忠王继锋
Owner CHINA PETROLEUM & CHEM CORP
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