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A kind of preparation method of hydrogenation catalyst

A technology of hydrogenation catalyst and alumina, which is applied in the direction of catalyst activation/preparation, molecular sieve catalyst, chemical instruments and methods, etc. It can solve problems such as failure to reflect the excellent performance of the composite carrier, damage to the pore structure of the carrier, and difficulty in effective combination. Achieve the effects of easy molding, improved hydrogenation capacity, and improved carrier strength

Active Publication Date: 2022-03-04
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

This method also does not avoid the addition of acid during the molding process, which will still lead to partial destruction of the carrier pore structure
At the same time, this method uses organic substances containing hydroxyl or carboxyl groups to enhance the binding ability of alumina and molecular sieves. There is no chemical reaction between alumina and molecular sieves, so it is difficult to effectively combine them. During the drying and roasting process, with the decomposition of organic substances, the product catalyst The alumina and molecular sieve components will agglomerate
[0004] At the same time, for the composite molecular sieve-alumina carrier, due to the difference in the adsorption properties of different material components, the catalyst synthesized by the conventional impregnation method cannot reflect the excellent performance of the composite carrier.

Method used

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  • A kind of preparation method of hydrogenation catalyst
  • A kind of preparation method of hydrogenation catalyst
  • A kind of preparation method of hydrogenation catalyst

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0038] Put 1 L of aluminum sulfate solution (concentration of 0.2 mol / L) and 1 L of sodium metaaluminate solution (concentration of 0.3 mol / L) in the raw material tank respectively, and place 1 L of pure water in the reaction tank as the bottom liquid, pass The temperature of the reaction tank is controlled to 60° C. by water circulation, and a small amount of sodium hydroxide is added to make the pH value of the solution 8.5. Inject the aluminum sulfate solution into the reaction tank at a rate of 10 mL / min, and at the same time inject the sodium metaaluminate solution and adjust the rate so that the pH value of the reaction tank solution is constant at 8.8. After 60 min, the neutralization is completed, and the Na is fully washed to remove + ions and SO 4 2- After ionization, a certain amount of deionized water was added to obtain pseudo-boehmite slurry A with a solid-to-liquid ratio of 8% (calculated as alumina).

Embodiment 2

[0040] 50g ZSM-5 molecular sieve (SiO 2 / Al 2 o 3 The molar ratio is 30.0, the unit cell constant is 20Å, and the relative crystallinity is 85%) is placed in a rolling pot, and under the condition of rotation, 70ml of ZSM-5 molecular sieves in the rolling pot are sprayed into 70ml containing 14.0g of hexahydrate Aqueous solution of nickel nitrate, after the solution is sprayed, continue to rotate in the rolling pot for 30 minutes, then place it for 3 hours, dry it at 110°C for 3 hours, put it into a muffle furnace and roast it for 2 hours at a roasting temperature of 500°C to obtain the modified ZSM-5 molecular sieve.

[0041] Put the modified ZSM-5 molecular sieve obtained above into the 625g pseudoboehmite slurry A obtained in Example 1, add 200g ethanol after stirring evenly, and then add 50g tetraethoxysilane after continuous stirring. After stirring evenly, a small amount of tetramethylammonium hydroxide was added to adjust the pH value of the slurry to 8.5. Put it i...

Embodiment 3

[0044] 20g SBA-15 mesoporous molecular sieve (SiO 2 / Al 2 o 3 The molar ratio is 35.0) placed in a rolling pot, and under the condition of rotation, spray 70ml of an aqueous solution containing 4.9g of nickel nitrate hexahydrate into the SBA-15 mesoporous molecular sieve in the rolling pot in an atomized manner. After the solution is sprayed, the Continue to rotate in the rolling pot for 30 minutes, then place it for 3 hours, dry it at 110°C for 3 hours, put it into a muffle furnace and roast it for 2 hours at a roasting temperature of 500°C to obtain a modified SBA-15 mesoporous molecular sieve.

[0045] Put the above-mentioned modified SBA-15 mesoporous molecular sieve into the 1000g pseudoboehmite slurry A obtained in Example 1, and then add 800g of isopropanol after stirring evenly, and then add 120g of dimethylvinyl Ethoxysilane, after stirring continuously, add a small amount of triethanolamine to adjust the pH value of the slurry to 9.0. Put it in a closed autoclave...

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Abstract

The invention discloses a method for preparing a hydrogenation catalyst. The preparation method of the hydrogenation catalyst of the present invention comprises: (1) impregnating molecular sieves with impregnation solution I containing Group VIII metal compounds, then drying and roasting to obtain modified molecular sieves; (2) preparing modified molecular sieves, pseudothin water Mix the bauxite precursor slurry and organic alcohol evenly to obtain slurry A; (3) add the silane coupling agent to slurry A and mix evenly, then adjust the pH value of the slurry to 7.5~11 to obtain slurry B; (4) combine the steps (3) The obtained slurry B is aged. After aging, the material is filtered to remove moisture, and organic amine and silane coupling agent are added to knead into a plastic body. After molding, drying and roasting, a composite carrier is obtained; (5) The hydrogenation catalyst is prepared by loading the group VIII metal and the group VIB metal on the composite carrier. The catalyst has very high hydrogenation performance, and is easy to desulfurize after hydrogenation and hydrogenation saturation of polycyclic aromatic hydrocarbons which are difficult to directly remove sulfides.

Description

technical field [0001] The invention relates to a method for preparing a hydrogenation catalyst. Background technique [0002] In today's petroleum refining process, catalysts play a very important role, and the physical and chemical properties of catalyst supports have a great influence on the activity of catalysts. Usually the carrier of the hydrogenation catalyst is porous acidic alumina, and there are also literature patent reports to adopt porous low-acidity molecular sieve or composite alumina (CN103349995A, CN102631934A, CN105251527A, J.Catal.317(2014) 303-317, J.Catal.317( 2010) 273-286) as a carrier to prepare a highly active hydrogenation catalyst. Compared with porous acidic alumina carrier catalyst, this catalyst has stronger hydrogen adsorption capacity, so its hydrogenation activity is higher and it is easy to 4,6-dimethyl Hydrodesulfurization of dibenzothiophene (4, 6-DMDBT) which is difficult to directly remove sulfide. However, this type of molecular sieve...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01J29/46B01J29/03B01J29/76B01J37/02C10G45/12
CPCB01J29/46B01J29/0333B01J29/7615B01J37/0205C10G45/12C10G2300/202B01J2229/18
Inventor 孙进郭蓉周勇杨成敏姚运海
Owner CHINA PETROLEUM & CHEM CORP
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