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Hydrogenation catalyst containing molecular sieves and amorphous silica-alumina

A technology of amorphous silica-alumina and hydrogenation catalyst, applied in molecular sieve catalysts, physical/chemical process catalysts, chemical instruments and methods, etc., can solve the problem of amorphous silica-alumina agglomeration, reduction of catalyst specific surface area and pore volume, and influence on catalyst performance and other problems, to achieve the effect of improving performance, avoiding agglomeration, and enhancing binding force

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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

[0040] Add 243g of solid aluminum chloride and 13g of nickel nitrate into 1 liter of distilled water while heating and stirring until dissolved to obtain solution (a). Dilute the concentrated ammonia water with an appropriate amount of distilled water to form about 10wt% dilute ammonia water (b), and dissolve 37g of xylitol 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). 62g 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 impregnation solution containing 14g sodium tungstate for saturated impregnation, after impregnation, dry at 120°C for 180 minutes, and bake at 500°C for 4 hours; 24g diethanolamine Dissolve in 100ml of water, heat to 60°C, add metal-modified Y molecular sieve under stirring, beat for 2 hours to obtain slurry (e). Take a plastic tank, add (a) int...

Embodiment 2

[0043] Add 293g of solid aluminum sulfate and 104g 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 86g of adipic acid 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). 44g 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 impregnation solution containing 117g sodium tungstate for saturated impregnation, after impregnation, dry at 120°C for 180 minutes, and bake at 500°C for 4 hours; 9g ethanolamine dissolves In 100ml of water, heated to 60°C, added metal-modified Y molecular sieve under stirring state, beating for 2 hours to obtain slurry (e). Take a pla...

Embodiment 3

[0046] Add 343g of solid aluminum sulfate and 361g 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 o3 / l sodium aluminate solution (b). 245 g of 1,4-butanedioic acid was dissolved in 1 L of water to form solution (c). 999g 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 impregnation solution containing 410g sodium tungstate for saturated impregnation, after impregnation, dry the molecular sieve at 120°C for 180 minutes, and roast at 500°C for 4 hours; The amine was dissolved in 500ml of water, heated to 60°C, metal-modified Y molecular sieve was added under stirring, and the slurry (d) was 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). ...

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Abstract

The invention discloses a hydrogenation catalyst containing molecular sieves and amorphous silica-alumina. The hydrogenation catalyst comprises hydrogenation active metal components, the molecular sieves and amorphous silica-alumina, wherein the hydrogenation active metals are group VIII metals and group VIB metals; the group VIII metal components are mainly loaded on the molecular sieves; the group VIB metal components are mainly loaded on amorphous silica-alumina; the molecular sieves are coated with amorphous silica-alumina; the group VIII metals account for 1-12% of the molecular sieves by weight in terms of oxide; the group VIB metals account for 2-40% of amorphous silica-alumina by weight in terms of oxide; the weight ratio of the molecular sieves to amorphous silica-alumina is (1:19)-(19:1). The hydrogenation catalyst has the beneficial effects that the hydrogenation catalyst fully isolates the main hydrogenation active metals from the acid centers of the molecular sieves and adjusts the hydrogenation and acid functions; the acid cracking components of the molecular sieves give full play so that reactants carry out cracking reaction as much as possible before coming into contact with the hydrogenation active centers; the catalyst is especially suitable for the hydrocarbon hydro-upgrading process with moderate requirements for acidity and the hydrogenation function.

Description

technical field [0001] The invention relates to a hydrogenation catalyst and its method, in particular to a hydrogenation catalyst containing molecular sieve and amorphous silicon aluminum and its preparation method. 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 / o...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01J29/16B01J29/78C10G47/20
Inventor 蒋广安刘雪玲张晔李宝忠郑庆华王继锋
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