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Hydrogenation catalysts containing molecular sieves and alumina

A technology of hydrogenation catalyst and molecular sieve, applied in molecular sieve catalysts, physical/chemical process catalysts, chemical instruments and methods, etc., can solve the problems affecting the distribution of amorphous silicon and aluminum, agglomeration of amorphous silicon and aluminum, and the reduction of catalyst specific surface area and pore volume and other problems, to avoid agglomeration or even blockage of pores, avoid direct contact, and improve performance

Active Publication Date: 2016-01-20
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] Add 555g of solid aluminum chloride and 153g of nickel nitrate hexahydrate into 2 liters 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 42.5g of 1,5-pentanediol in 2L of water to form a solution (c). 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 174g sodium tungstate for saturated impregnation, after impregnation, dry at 120°C for 180 minutes, and bake at 500°C for 4 hours; 10g B Dissolve diamine in 300ml of absolute ethanol, heat to 60°C, stir for half an hour, add metal-modified Y-type molecular sieve, continue stirring for 2 hours, obtain modified molecular sieve (d) that pre-adsorbs organic amine after filtration. Take a plastic tank, add (a) into the...

Embodiment 2

[0044] Add 555g of solid aluminum sulfate and 148g of nickel nitrate into 10 liters of distilled water while heating and stirring until dissolved to obtain solution (a). Dilute the concentrated ammonia water into about 10wt% dilute ammonia water (b) by adding an appropriate amount of distilled water, and dissolve 80g of 1,4-butanediol in 1L of water to obtain a solution (c). 165gY-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 168g sodium tungstate for saturated impregnation. After impregnation, dry at 120°C for 180 minutes and bake at 500°C for 4 hours; The amine was dissolved in 5 L of water, heated to 60° C., stirred for half an hour, and the metal-modified molecular sieve was added and stirred for 2 hours to obtain a molecular sieve slurry (d). Take a plastic tank, add (a) into the tank, stir and heat to 60°C, open the valve of the contai...

Embodiment 3

[0047] Add 555g of solid aluminum sulfate and 767g of nickel nitrate into 10 liters 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), 198g of propylene glycol was dissolved in 1L of water to form a solution (c). 1543gY 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%) is saturated impregnated with an impregnation solution containing 870g sodium tungstate, dried at 120°C for 180 minutes after impregnation, and roasted at 500°C for 4 hours; 155g diethanolamine Dissolve in 10L of water, heat to 60°C, add the metal-modified molecular sieve under stirring, continue stirring at the temperature for 2 hours, and filter to obtain the treated molecular sieve (d). Take a glue tank, put 2l of deionized water into it, stir and heat to 60°C, then add (d), op...

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Abstract

The invention discloses a hydrogenation catalyst containing molecular sieve and aluminum oxide. The composition of the hydrogenation catalyst includes: hydrogenation active metal components, molecular sieves and amorphous alumina, wherein the hydrogenation active metals are Group VIII metals and Group VIB metals, wherein the Group VIII metal components are mainly supported on molecular sieves , Group VIB metal components are mainly supported on amorphous alumina, and amorphous alumina wraps molecular sieves, Group VIII metals account for 1% to 12% of the molecular sieve weight in terms of oxides, and Group VIB metals are calculated in terms of oxides Accounting for 2%~40% of the weight of amorphous alumina, the weight ratio of molecular sieve to amorphous alumina is 1:19~19:1. The hydrogenation catalyst of the present invention fully isolates the main hydrogenation active metal from the acidic center of the molecular sieve, regulates the hydrogenation function and the acidic function, and the acidic cracking component of the molecular sieve fully exerts its effect, so that the reactants can be as fast as possible before contacting the hydrogenation active center. A cleavage reaction may occur. The catalyst is especially suitable for the hydro-upgrading process of hydrocarbons which requires moderate acidity and moderate hydrogenation function.

Description

technical field [0001] The invention relates to a hydrogenation catalyst and a preparation method thereof, in particular to a hydrogenation catalyst containing molecular sieve and alumina and a preparation method thereof. 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 ...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01J29/16B01J29/78C10G47/20
Inventor 蒋广安张晔郑庆华刘雪玲李宝忠王继锋
Owner CHINA PETROLEUM & CHEM CORP
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