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A rare earth-containing modified Y-type molecular sieve rich in secondary pores and its preparation method

A molecular sieve and secondary pore technology, applied in the field of modified Y-type molecular sieve and its preparation, can solve the problems of difficult and high heavy oil catalytic cracking activity, poor accessibility of active centers, good coke selectivity, etc. Effects of coke selectivity and high heavy oil conversion activity

Active Publication Date: 2020-05-19
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

The ultra-stable molecular sieve prepared by this method has a high silicon-alumina ratio, a small unit cell constant, and contains a certain amount of rare earth, but it does not involve the preparation of a molecular sieve with secondary pores. The high-stable molecular sieve has poor accessibility to the active center , the activity is not high
[0014] The inventors of the present invention found that it is difficult for the ultra-stable Y-type molecular sieve prepared by the prior art to have high heavy oil catalytic cracking activity and good coke selectivity at the same time

Method used

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  • A rare earth-containing modified Y-type molecular sieve rich in secondary pores and its preparation method
  • A rare earth-containing modified Y-type molecular sieve rich in secondary pores and its preparation method
  • A rare earth-containing modified Y-type molecular sieve rich in secondary pores and its preparation method

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Embodiment approach

[0044]In the preparation method of the modified Y-type molecular sieve provided by the present invention, in step (4), the gas-phase ultrastable modified Y-type molecular sieve obtained in step (3) is contacted with an acid solution for reaction (the present invention is called channel cleaning modification, Referred to as channel cleaning, or acid treatment modification). One embodiment, the reaction of the gas-phase ultra-stable modified Y-type molecular sieve obtained in step (3) in contact with the acid solution is to react the gas-phase ultra-stable modified molecular sieve, that is, the gas-phase ultra-stable modified The Y-type molecular sieve is mixed with the acid solution, and reacted for a period of time, then the reacted molecular sieve is separated from the acid solution, for example, separated by filtration, and then optionally washed and optionally dried to obtain the modified Y-type molecular sieve provided by the invention , where the purpose of washing is to ...

Embodiment 1

[0059] 2000Kg (dry basis weight) skeleton SiO 2 / Al 2 o 3 Be 4.6 NaY type zeolite (sodium oxide content 13.5% by weight, Sinopec Catalyst Qilu Branch Company produces) joins and is equipped with 20m 3 In the water exchange tank, stir well at 25°C and then add 600L RECl 3 Solution (RECl 3 The rare earth concentration in the solution is expressed as RE 2 o 3 Calculated as 319g / L), after continuing to stir for 60 minutes, filter, wash, and the filter cake is sent to a flash drying oven for drying; obtain a Y-type molecular sieve with a rare earth-containing conventional unit cell size with reduced sodium oxide content, and its sodium oxide content It is 7.0% by weight, and the unit cell constant is 2.471nm; then, it is sent to a roasting furnace at a temperature of 390°C, and is roasted for 6 hours under 50% water vapor (containing 50% by volume of water vapor in the atmosphere); then, at a temperature of 500°C, it is dried Air atmosphere (water vapor content is lower than ...

Embodiment 2

[0063] 2000Kg (dry basis weight) skeleton SiO 2 / Al 2 o 3 Be 4.6 NaY type zeolite (sodium oxide content 13.5% by weight, Sinopec Catalyst Qilu Branch Company produces) joins and is equipped with 20m 3 In the primary exchange tank of decationized water, stir evenly at 90°C, and then add 800L RECl 3 Solution (RECl 3 The rare earth concentration in the solution is expressed as RE 2 o 3 Calculated as 319g / L), stirred for 60 minutes; filtered, washed, and the filter cake was sent to a flash drying oven for drying to obtain a Y-type molecular sieve with a rare earth-containing conventional unit cell size with a reduced sodium oxide content, and its sodium oxide content was 5.5 % by weight, the unit cell constant is 2.471nm; then, it is sent into a roasting furnace at a temperature (atmosphere temperature) of 450°C and 80% water vapor atmosphere for 5.5 hours; then, the molecular sieve material enters the roasting furnace for roasting and drying treatment, and the roasting tempe...

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Abstract

A rare earth-containing modified Y-type molecular sieve rich in secondary pores and a preparation method thereof. The Y-type molecular sieve has a rare earth content of 5 to 12% by weight, a sodium content of no more than 0.5% by weight, and a total pore volume of 0.36 to 0.48 mL. / g, the secondary pore volume accounts for 20~38% of the total pore volume, the unit cell constant is 2.440~2.455nm, the non-framework aluminum content accounts for less than 10% of the total aluminum content, the lattice collapse temperature is higher than 1060°C, B acid The ratio of the amount to the amount of L acid is not less than 3.50. The preparation method includes: preparing a Y-type molecular sieve with a conventional unit cell size containing rare earths, roasting it for 4.5 to 7 hours in an atmosphere of 350 to 520°C and 30 to 95 volume % water vapor, contacting with silicon tetrachloride gas and treating with acid. A step of. The modified Y-type molecular sieve has higher heavy oil conversion activity and lower coke selectivity, and has higher gasoline yield, liquefied gas yield, light oil yield and total liquid recovery.

Description

technical field [0001] The invention relates to a high-stability modified Y-type molecular sieve and a preparation method thereof, and further relates to a high-stability Y-type molecular sieve for heavy oil catalytic cracking and a preparation method thereof. Background technique [0002] Y-type molecular sieves have been the main active component of catalytic cracking (FCC) catalysts since they were first used in the 1960s. However, with the intensification of heavy crude oil, the content of polycyclic compounds in FCC raw materials increased significantly, but their diffusion capacity in zeolite channels decreased significantly. The pore size of Y-type molecular sieve as the main active component is only 0.74nm, and it is directly used to process heavy fractions such as residual oil. The accessibility of the active center of the catalyst will become the main obstacle to the cracking of polycyclic compounds contained therein. [0003] Molecular sieve pore structure is clo...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01J29/08B01J35/10C10G11/05
CPCC10G11/05B01J29/088C10G2300/70B01J35/651B01J35/633B01J35/647
Inventor 周灵萍张蔚琳许明德陈振宇田辉平朱玉霞
Owner CHINA PETROLEUM & CHEM CORP
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