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Preparation method of hydrogenation catalyst

A hydrogenation catalyst, alumina technology, applied in catalyst activation/preparation, molecular sieve catalysts, chemical instruments and methods, etc., can solve the problems such as the inability to reflect the excellent performance of the composite carrier, the damage to the pore structure of the carrier, and the difficulty of effective combination, etc. Achieve high acidity, avoid agglomeration, avoid uneven effect

Active Publication Date: 2020-04-28
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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  • Preparation method of hydrogenation catalyst
  • Preparation method of hydrogenation catalyst
  • 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 preparation method of a hydrogenation catalyst. The preparation method of the hydrogenation catalyst comprises the following steps: (1) impregnating a molecular sieve with animpregnation solution I containing a VIII group metal compound, drying, and roasting to obtain a modified molecular sieve; (2) uniformly mixing the modified molecular sieve, pseudo-boehmite precursorslurry and organic alcohol to obtain a slurry A; (3) adding a silane coupling agent into the slurry A, uniformly mixing, and then adjusting the pH value of the slurry to 7.5-11 to obtain a slurry B;(4) aging the slurry B obtained in the step (3), filtering to remove water from the material after aging is finished, adding organic amine and a silane coupling agent, kneading into a plastic body, molding, drying, and roasting to obtain a composite carrier; and (5) loading a VIII group metal and a VIB group metal onto the composite carrier to prepare the hydrogenation catalyst. The catalyst has high hydrogenation performance, and is easy for post-hydrogenation desulfurization of sulfides which are difficult to directly remove and hydrogenation saturation of polycyclic aromatic hydrocarbons.

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 Applications(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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