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Silicon-containing hydrodemetallization catalyst and its preparation method and application

A hydrodemetallization and catalyst technology, applied in the direction of metal/metal oxide/metal hydroxide catalysts, chemical instruments and methods, physical/chemical process catalysts, etc., can solve the adverse effects and interactions of the mechanical strength of the carrier and the catalyst It needs to be further improved, such as the increase of macropore content, so as to achieve the effect of facilitating mass transfer and diffusion, improving anti-sintering ability, and improving anti-carbon deposition

Active Publication Date: 2021-07-27
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0006] In summary, in the process of preparing macroporous alumina supports and / or hydrodemetallization catalysts in the prior art, physical pore-enlarging agents are usually used to increase the pore diameter of the supports, and the addition of physical pore-enlarging agents can indeed make the alumina The content increases, but it will have adverse effects on the mechanical strength of the carrier and catalyst
In addition, in the process of preparing catalysts at this stage, the interaction between active components and supports needs to be further improved.

Method used

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  • Silicon-containing hydrodemetallization catalyst and its preparation method and application

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preparation example Construction

[0032] The preparation method of silicon-containing hydrodemetallization catalyst of the present invention, the method comprises the following steps,

[0033] (1) performing a first contact with the first silicon-containing solution and a first physical pore-enlarging agent, and performing a second contact with the second silicon-containing solution and a second physical pore-enlarging agent;

[0034] (2) The contacted first physical pore-enlarging agent obtained in step (1), the contacted second physical pore-enlarging agent and pseudo-boehmite are mixed, formed, first dried, and first roasted to obtain a silicon-containing Alumina carrier;

[0035] (3) The hydrogenation active component impregnating solution is contacted with the silicon-containing alumina carrier obtained in step (2) for the third time, and the contacted silicon-containing alumina carrier is subjected to second drying and second roasting to obtain a silicon-containing alumina carrier Hydrodemetallization c...

Embodiment 1

[0071] 1) Weigh 15 grams of the first carbon black powder with a particle diameter of 400 meshes and place it in a spray boiling pan, and use a nozzle atomization method to impregnate the first carbon black powder with unsaturated Method: Spray 7.5 mL of ethanol solution of ethyl orthosilicate (amount is 50% of the saturated water absorption of the first carbon black powder, which is equivalent to containing 4 grams of silicon dioxide).

[0072] 2) Weigh 5 grams of the second carbon black powder with a particle diameter of 1300 mesh and place it in a spray boiling pot, and spray the second carbon black powder in a saturated impregnated manner in an atomized manner under the rotating state of 90 rpm. Soak in 5 mL of ethanol solution of ethyl orthosilicate (the amount used is the saturated water absorption of the second carbon black powder, which is equivalent to containing 0.5 g of silicon dioxide).

[0073] 3) the first carbon black powder after the impregnation obtained in th...

Embodiment 2

[0077] Prepare the silicon-containing hydrodemetallization catalyst in the same manner as in Example 1, except that:

[0078] In step 1), the particle diameter of the first carbon black powder is 325 orders, and the addition is 12.5 grams, using the ethanol solution of 3.8mL orthosilicate methyl ester (consumption is 30% of the saturated water absorption of the first carbon black powder, wherein Equivalent to containing 2 grams of silicon dioxide) spraying the first carbon black powder.

[0079] Step 2) in, the particle diameter of the second carbon black powder is 1100 orders, and the addition is 7.5 grams, uses the ethanol solution of 7.5mL orthosilicate methyl ester (consumption is the saturated water absorption of the second carbon black powder, wherein is equivalent to containing Silica 1 gram) sprays and soaks the second carbon black powder.

[0080] In step 3), the calcination temperature under nitrogen atmosphere is 500°C, and the calcination temperature under air atm...

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Abstract

The invention relates to the field of catalyst preparation, and discloses a method for preparing a silicon-containing hydrodemetallization catalyst. The method includes the following steps: (1) first contacting a first silicon-containing solution with a first physical pore-enlarging agent, and The second silicon-containing solution is contacted with the second physical pore-enlarging agent for the second time; (2) the contacted first physical pore-enlarging agent obtained in step (1), the contacted second physical pore-enlarging agent and the pseudo thin water The bauxite is mixed, shaped, first dried, and first calcined to obtain a silicon-containing alumina carrier; (3) the hydrogenation active component impregnating solution is contacted with the silicon-containing alumina carrier obtained in step (2) for the third time, and The contacted silicon-containing alumina carrier is subjected to second drying and second calcining to obtain a silicon-containing hydrodemetallization catalyst. The catalyst prepared by the method has high mechanical strength, suitable pore structure, moderate interaction between active components and supports, and high hydrodemetallization activity and activity stability.

Description

technical field [0001] The invention relates to the field of catalyst preparation, in particular to a method for preparing a silicon-containing hydrodemetallization catalyst. Background technique [0002] With the increasing requirements for deep processing of raw materials worldwide, the main energy structure is gradually developing in the direction of macromolecules and high carbon, especially for my country where crude oil is generally heavy. In order to effectively solve the problems of excessive diffusion resistance of heavy oil components in the catalyst pores, heavy metal impurity deposition and coking caused by catalyst activity decline or deactivation, it is urgently required that the alumina carrier widely used in the petrochemical industry has a large pore volume and The characteristic of large aperture. The large pore size is conducive to the diffusion of macromolecular compounds into the catalyst particles, and the large pore volume is conducive to improving th...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01J27/19B01J35/10C10G45/08
CPCB01J23/002B01J27/19B01J35/1019B01J35/1042B01J35/1061C10G45/08C10G2300/202
Inventor 任靖张勇李顺新宋春利姜艳
Owner CHINA PETROLEUM & CHEM CORP
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