A kind of hydrocracking catalyst and its preparation method and application

A hydrocracking and catalyst technology, applied in the direction of catalyst activation/preparation, physical/chemical process catalyst, molecular sieve catalyst, etc., can solve the problem of inability to achieve catalyst, differential matching of hydrogenation activity and cracking activity, and inability to achieve differential matching of catalyst And other issues

Active Publication Date: 2022-07-08
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Regardless of whether the catalyst is prepared by the kneading method or the impregnation method, the hydrogenation activity and cracking activity of different parts inside and outside the catalyst are evenly distributed. The current preparation method cannot realize the differential matching of the hydrogenation activity and cracking activity inside and outside the catalyst.
[0004] U.S. Patent No. 5,229,347 provides a method for preparing a moderate hydrocracking catalyst. The prepared catalyst uses a combination of VIB and VIII as the active metal component, and introduces the metal component by impregnation. Realize the differential matching of catalyst internal and external hydrogenation activity and cracking activity

Method used

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  • A kind of hydrocracking catalyst and its preparation method and application
  • A kind of hydrocracking catalyst and its preparation method and application
  • A kind of hydrocracking catalyst and its preparation method and application

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0040] Molecular sieve preparation method:

[0041] (1) Take the original NaY molecular sieve powder prepared in the laboratory, mix it with ammonium nitrate with a concentration of 1.7 mol / L according to the liquid-solid ratio of 10:1, and exchange it at 80 °C for 1 hour. Repeat this process twice. Na content in Na 2 O is calculated as 2.6%;

[0042] (2) The Y molecular sieve obtained in step (1) was hydrothermally treated at 620°C and 0.1Mpa for 2 hours, and the process was repeated twice;

[0043] (3) The molecular sieve obtained in step (2) is mixed with dilute nitric acid according to a liquid-solid ratio of 10:1 (the concentration of dilute nitric acid in the solution is controlled by H+ ion concentration to 1 mol / L), and then the temperature is raised to 90 °C for constant temperature reaction for 3 hours.

[0044] (4) Take the Y molecular sieve treated with the dilute nitric acid solution in step (3), mix it with sodium nitrate with a concentration of 1.2 mol / L accor...

Embodiment 2

[0051] Molecular sieve preparation method:

[0052] (1) Take the original NaY molecular sieve powder prepared in the laboratory, mix it with ammonium nitrate with a concentration of 2 mol / L according to a liquid-solid ratio of 10:1, exchange it at 60 °C for 1 hour, and repeat this process twice. Content as Na 2 O counts as 2.5%;

[0053] (2) The Y molecular sieve obtained in step (1) was hydrothermally treated at 640°C and 0.1Mpa for 2 hours, and the process was repeated twice;

[0054] (3) The molecular sieve obtained in step (2) is mixed with dilute nitric acid according to a liquid-solid ratio of 10:1 (the concentration of dilute nitric acid in the solution is controlled to be 1.4 mol / L by H+ ion concentration), and then the temperature is raised to 90 °C for constant temperature reaction for 2 hours.

[0055] (4) Take the Y molecular sieve treated with the dilute nitric acid solution in step (3), mix it with sodium nitrate with a concentration of 1.5mol / L according to a ...

Embodiment 3

[0062] Molecular sieve preparation method:

[0063] (1) Take the original powder of NaY molecular sieve prepared in the laboratory, mix it with ammonium nitrate with a concentration of 2 mol / L according to the liquid-solid ratio of 10:1, exchange it at 80 °C for 1 hour, and repeat this process once. Content as Na 2 O is calculated as 2.9%;

[0064] (2) The Y molecular sieve obtained in step (1) was hydrothermally treated at 660°C and 0.1Mpa for 3 hours, and the process was repeated once;

[0065] (3) The molecular sieve obtained in step (2) is mixed with dilute nitric acid according to a liquid-solid ratio of 10:1 (the concentration of dilute nitric acid in the solution is controlled to be 1.6 mol / L by H+ ion concentration), and then the temperature is raised to 70 °C for constant temperature reaction for 2 hours.

[0066] (4) Take the Y molecular sieve treated with the dilute nitric acid solution in step (3), mix it with sodium nitrate with a concentration of 1.5mol / L accor...

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Abstract

The invention discloses a hydrocracking catalyst and a preparation method and application thereof. The method includes the following steps: (1) forming modified Y molecular sieve, amorphous silica-alumina and / or alumina, drying and calcining to obtain the catalyst carrier; the sodium content in the modified Y molecular sieve is 1 to 8 wt%; (2) the catalyst carrier prepared in step (1) by saturated impregnation with a non-polar organic solvent, and then dried to the non-polar catalyst carrier in the catalyst carrier The content of the organic solvent is 20-90% of the saturated adsorption capacity of the catalyst carrier. (3) The material obtained in step (2) is subjected to ammonium salt ion exchange, drying and calcination treatment; (4) active metal is introduced into the material obtained in step (3), and the final catalyst is obtained by drying and calcining. The catalyst prepared by the method can reduce the cracking of high value-added lubricating oil base oil to generate other low-value products, especially the excessive cracking of straight-chain paraffin high viscosity index components in the lubricating base oil.

Description

technical field [0001] The invention relates to a hydrocracking catalyst and its preparation method and application, in particular to a hydrocracking catalyst for high-quality lubricating oil base oil with high yield and its preparation method and application. Background technique [0002] The hydrocracking process includes two processes: cracking and hydrogenation. On the one hand, heavy feedstock oil is cracked and converted into light distillate components, and on the other hand, hydrogenation is carried out while cracking to improve product quality. For the hydrocracking catalyst, the hydrogenation activity and the cracking activity deployment method determine the reaction characteristics and performance of the catalyst. [0003] At present, the preparation methods of hydrocracking catalysts are mainly divided into two categories: kneading method and impregnation method. The kneading method is to mix the active metal components with molecular sieve, alumina, and amorpho...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01J29/16B01J35/10B01J37/02B01J37/10B01J37/30C10G67/02
CPCB01J29/166B01J35/1019B01J35/1038B01J37/0201B01J37/10B01J37/30C10G67/02B01J2229/18Y02P20/52
Inventor 郭蓉柳伟杜艳泽秦波高杭张晓萍
Owner CHINA PETROLEUM & CHEM CORP
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