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Hydrogenation catalysts containing molecular sieves and amorphous silica-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 of amorphous silicon-aluminum agglomeration, reduction of catalyst specific surface area and pore volume, and influence on catalyst performance, etc. Achieve the effects of enhancing binding force, avoiding agglomeration and improving performance

Active Publication Date: 2016-08-03
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

[0040] Add 243 g of solid aluminum chloride and 13 g of nickel nitrate to 1 liter of distilled water, while heating and stirring to dissolve, to obtain solution (a). Dilute concentrated ammonia water with an appropriate amount of distilled water to form about 10wt% dilute ammonia water (b), and dissolve 37g xylitol in 500ml water to form solution (c). Take 10L water glass (industrial grade, modulus 3.0) and dilute it in 20L deionized water to prepare solution (d). 62gY 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%) Saturated impregnation with an impregnating solution containing 14g of sodium tungstate, drying at 120°C for 180 minutes after impregnation, and baking at 500°C for 4 hours; 24g of diethanolamine Dissolve in 100ml of water, heat to 60°C, add metal-modified Y molecular sieve under stirring, and beat for 2 hours to obtain slurry (e). Take a glue tank, add (a) to the tank, stir...

Embodiment 2

[0043] Add 293g of solid aluminum sulfate and 104g of nickel nitrate to 1 liter of distilled water, while heating and stirring to dissolve, to obtain solution (a). Concentrated ammonia water is added to an appropriate amount of distilled water to dilute to about 10wt% dilute ammonia water (b), 86g adipic acid is dissolved in 500ml water to form solution (c). Take 10L water glass (industrial grade, modulus 3.0) and dilute it in 20L deionized water to prepare solution (d). 44gY 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 117g sodium tungstate immersion solution for saturated immersion, dry at 120°C for 180 minutes, and calcinate at 500°C for 4 hours; 9g ethanolamine solution In 100 ml of water, heat to 60° C., add the metal-modified Y molecular sieve under stirring, and beat for 2 hours to obtain slurry (e). Take a glue tank, add (a) to the tank, stir and heat to 65℃, open the va...

Embodiment 3

[0046] 343 g of solid aluminum sulfate and 361 g of nickel nitrate were added to 1 liter of distilled water, while heating and stirring to dissolve to obtain solution (a). Prepare solid sodium metaaluminate to a concentration of 20gAl 2 O 3 / l Sodium aluminate solution (b). 245g of 1,4-succinic acid was dissolved in 1L of water to form solution (c). 999gY 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 410g sodium tungstate impregnation solution for saturated impregnation. After impregnation, the molecular sieve is dried at 120°C for 180 minutes, and 500°C is calcined for 4 hours; 100g ethylenedi The amine was dissolved in 500 ml of water, heated to 60°C, and the metal-modified Y molecular sieve was added under stirring. After stirring for 2 hours, a slurry (d) was obtained. Take 10L water glass (industrial grade, modulus 3.0) and dilute it in 20L deionized water to prepare solutio...

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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 a method thereof, in particular to a hydrogenation catalyst containing molecular sieve and amorphous silicon aluminum 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 raw material adaptability, flexible production operations and product schemes, and good product quality, it has become an important way to produce high-quality, light and clean oils and to solve the source of chemical raw materials. [0003] The hydrocracking catalyst is generally a dual-function catalyst, and its cracking activity and hydrogenation activity are provided by the acidic component and the hydrogenation active component in the catalyst. [0004] The acidic component in the catalyst is generally provided by the molecular sieve contained in the catalyst and / or the refr...

Claims

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Application Information

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