Carrier, residual oil hydrogenation catalyst based on carrier, and preparation method of carrier

A residue hydrogenation and catalyst technology, which is applied in catalyst activation/preparation, chemical instruments and methods, metal/metal oxide/metal hydroxide catalysts, etc., can solve the problem of low metal removal rate and desulfurization activity, heavy oil or residue The problems of low oil conversion rate and low catalytic activity can improve the metal removal rate and desulfurization activity, improve the catalytic activity, and facilitate the diffusion and mass transfer.

Active Publication Date: 2014-09-03
福建三聚福大化肥催化剂国家工程研究中心有限公司 +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0005] The technical problem to be solved by the present invention is that the residual oil hydrogenation catalyst in the prior art has the problem of easy coking and low catalytic activity when it is used in reactions such as hydrodemetallization, hydrodesulfurization, and hydroconversion of heavy oi

Method used

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  • Carrier, residual oil hydrogenation catalyst based on carrier, and preparation method of carrier
  • Carrier, residual oil hydrogenation catalyst based on carrier, and preparation method of carrier

Examples

Experimental program
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Example Embodiment

[0032] Example 1

[0033] This embodiment provides a residue hydrogenation catalyst, and the raw materials used to prepare the residue hydrogenation catalyst include:

[0034] Modified kaolin carrier, 70 parts by weight;

[0035] Active metal Mo, 3 parts by weight (as Mo 2 O 3 meter);

[0036] Activated carbon, 19 parts by weight, the specific surface area of ​​the activated carbon is 500m 2 / g, the pores with a radius of 80-120nm on the activated carbon account for 55% of the total pores;

[0037] Wherein, the carrier is prepared by the following method:

[0038] (1) Weigh the kaolin raw soil and the pore expander sodium carbonate and mix them uniformly, control the mass ratio of the kaolin raw soil to the pore expander to 1:6, and carry out the process under nitrogen at a temperature of 600°C Reaming treatment 3h;

[0039] (2) Use 15% hydrochloric acid to pickle the product of step (1) twice, and then wash it with water after the pickling is completed; after the water washing is comple...

Example Embodiment

[0043] Example 2

[0044] This embodiment provides a residue hydrogenation catalyst, and the raw materials used to prepare the residue hydrogenation catalyst include:

[0045] Modified kaolin carrier, 55 parts by weight;

[0046] Active metal W, 9 parts by weight (in WO 3 meter);

[0047] Activated coal-made activated carbon, 40 parts by weight;

[0048] Rare earth metal La, 2 parts by weight (as La 2 O 3 meter);

[0049] Wherein, the carrier is prepared by the following method:

[0050] (1) Weigh the kaolin raw soil and the pore expander potassium carbonate and mix them uniformly, and control the mass ratio of the kaolin raw soil to the pore expander to be 1:4. In a mixed gas atmosphere of nitrogen and carbon dioxide, 500 Perform hole expansion treatment for 8 hours at a temperature of ℃;

[0051] (2) Use 20% hydrochloric acid to pickle the product of step (1) once, and then wash it with water after the pickling is completed; after completing the water washing, separate the solid product...

Example Embodiment

[0058] Example 3

[0059] This embodiment provides a residue hydrogenation catalyst, and the raw materials used to prepare the residue hydrogenation catalyst include:

[0060] Modified kaolin carrier, 80 parts by weight;

[0061] Active metal Mo (with Mo 2 O 3 Count), 4 parts by weight;

[0062] Blue charcoal activated carbon after activation treatment, 15 parts by weight;

[0063] Rare earth metal Pr (as Pr 2 O 3 ), 6 parts by weight.

[0064] Wherein, the carrier is prepared by the following method:

[0065] (1) Weigh the kaolin raw soil and the pore expander sodium carbonate and mix them uniformly, and control the mass ratio of the kaolin raw soil to the pore expander to be 1:8. In a mixed gas atmosphere of oxygen and carbon dioxide, 800 Perform hole expansion treatment for 1h at a temperature of ℃;

[0066] (2) Use 25% hydrochloric acid to pickle the product of step (1) once, and then wash it with water after the pickling is completed; after completing the water washing, separate the ...

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Abstract

The invention provides a carrier for a residual oil hydrogenation catalyst and the catalyst based on the carrier. The carrier is prepared by the following steps of (1) respectively weighing kaolin original soil and a pore-enlarging agent according to the mass ratio of 1:4 to 1:8, uniformly mixing, and performing pore-enlarging processing for 1 to 8 hours in a gas atmosphere of one or two of nitrogen, oxygen, air and carbon dioxide in a temperature condition of 500 to 800 DEG C; (2) pickling a pore-enlarged product from the step (1), water-washing, and then drying at 100 to 150 DEG C, so as to obtain the carrier of the residual oil hydrogenation catalyst. The carrier prepared by adopting the preparation method has a large pore diameter, pores with the radius of 50 to 80nm accounts for more than 70% of the total number of the pores, the specific surface area can reach 120 to 220m<2>/g, and when hydrogenation reaction is performed on heavy oil or residual oil, the carrier is favorable for rapid diffusion and mass transfer of asphaltene.

Description

technical field [0001] The invention relates to a carrier, a residue oil hydrogenation catalyst based on the carrier and a preparation method thereof, belonging to the field of residue oil hydrogenation catalysis. Background technique [0002] With the development of heavy and inferior crude oil in the world, and the increasing scarcity of crude oil resources, it is particularly important to effectively process heavy oil and crude oil residues, among which hydrogenation technology is to process heavy and residues to make them lighter. One of the most effective programs. However, due to the heavy and residual oil containing a large amount of impurities such as metals, sulfur, and nitrogen, as well as a large amount of residual carbon that is easy to coke, these impurities will pollute the corresponding catalyst in the subsequent processing, and even lead to the poisoning of the corresponding catalyst. , which will have a great impact on the stability of heavy and residual oi...

Claims

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Application Information

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IPC IPC(8): B01J23/28B01J23/30B01J37/02C10G45/08
Inventor 江莉龙曹彦宁林科马永德魏可镁魏颖
Owner 福建三聚福大化肥催化剂国家工程研究中心有限公司
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