Catalytic cracking catalyst preparation method

Patent metadata

Field	Value
Publication number	US-9895681-B2
Application number	US-201314438558-A
Country	US
Kind code	B2
Filing date	Oct 25, 2013
Priority date	Oct 26, 2012
Publication date	Feb 20, 2018
Grant date	Feb 20, 2018

Abstract

A process for preparing a catalytic cracking catalyst, which process comprises: a molecular sieve is introduced into a gas-phase ultra-stabilization reactor, the molecular sieve is moved without the conveying of carrier gas from a molecular sieve inlet of the gas-phase ultra-stabilization reactor to a molecular sieve outlet of the gas-phase ultra-stabilization reactor, and the molecular sieve is contacted and reacted with a gaseous SiCl 4 in the gas-phase ultra-stabilization reactor, the molecular sieve resulting from the contacting and the reacting is optionally washed, then mixed with a matrix and water into slurry, and shaped into particles.

First claim

The invention claimed is:

1. A process for preparing a catalytic cracking catalyst, comprising:
introducing a molecular sieve into a first inlet of a gas-phase ultra-stabilization reactor;
introducing a gaseous SiCl 4 into the first inlet or an optional second inlet of the gas-phase ultra-stabilization reactor;
reacting the molecular sieve and the gaseous SiCl 4 in the gas-phase ultra-stabilization reactor to obtain a ultra-stabilized molecular sieve;
withdrawing the ultra-stabilized molecular sieve from a first outlet of the gas-phase ultra-stabilization reactor;
withdrawing a gas stream from the gas-phase ultra-stabilization reactor, wherein the gas stream comprises residual SiCl 4 ;
optionally washing the ultra-stabilized molecular sieve;
mixing the ultra-stabilized molecular sieve with a matrix and water to form a slurry; and
shaping the slurry into particles, and

wherein the first inlet is at a same or a higher elevation than the first outlet.

2. The process according to claim 1 , wherein a weight ratio of SiCl 4 introduced into the second inlet to the molecular sieve introduced into the first inlet is 0.01-1.

3. The process according to claim 2 , wherein the weight ratio of SiCl 4 introduced into the second inlet to the molecular sieve introduced into the first inlet is 0.05-0.60.

4. The process according to claim 2 , wherein the weight ratio of SiCl 4 introduced into the second inlet to the molecular sieve introduced into the first inlet is 0.05-0.30.

5. The process according to claim 1 , wherein the ultra-stabilized molecular sieve has a relative crystallinity of greater than 50%.

6. The process according to claim 1 , wherein a temperature in the gas-phase ultra-stabilization reactor is 250-700° C., and a reaction time between the molecular sieve and the gaseous SiCl 4 in the gas-phase ultra-stabilization reactor is from 10 seconds to 100 minutes.

7. The process according to claim 1 , wherein the gas-phase ultra-stabilization reactor comprises an upper end, a lower end, and a tubular body disposed between the upper end and the lower end, wherein the upper end is at a higher elevation that the lower end, and
wherein the first inlet and the optional second inlet are disposed about the upper end of the gas-phase ultra-stabilization reactor and the first outlet is disposed about the lower end of gas-phase ultra-stabilization the reactor so that the molecular sieve flow in a downward direction in the gas-phase ultra-stabilization reactor.

8. The process according to claim 7 , wherein at least a section of the tubular body is rotatably mounted.

9. The process according to claim 8 , further comprising rotating the rotatable tubular section at 0.05-40 rpm.

10. The process according to claim 8 , wherein a length of the rotatable tubular section is 20% or more of a total length of the tubular body.

11. The process according to claim 7 , wherein an acute angle between an axis in a longitudinal direction of the tubular body and an imaginary horizontal plane is between 5° to 90°.

12. The process according to claim 11 , wherein the acute angle between the axis in a longitudinal direction of the tubular body and the imaginary horizontal plane is between 30° to 55°.

13. The process according to claim 7 , wherein the first inlet and the optional second inlet are disposed at the upper end of the gas-phase ultra-stabilization reactor.

14. The process according to claim 7 , wherein the tubular body comprises at least one seizing plate, at least one dam plate, or both installed on the inner wall of the tubular body.

15. The process according to claim 7 , wherein the tubular body has a length of 5-200 meters, an inner diameter of 0.01-6 meters, and a ratio of the length of the tubular body to the inner diameter of the tubular body is not less than 1, 3-100:1.

16. The process according to claim 7 , wherein the gas-phase ultra-stabilization reactor further comprises an inner tube disposed coaxially with the tubular body, forming an annular space between the inner tube and the tubular body, wherein the first inlet, the optional second inlet, and the first outlet are fluidly connected to the annular space.

17. The process according to claim 7 , wherein, among any two imaginary points along the axis of the tubular body, the point closer to the upper end has a same or a higher elevation than that of the point farther from the upper end.

18. The process according to claim 7 , wherein an imaginary tangent line at any point on the axis of the tubular body that points away from the upper end is horizontal or points in a downward direction.

19. The process according to claim 1 , wherein the gas-phase ultra-stabilization reactor comprises a conveying device to move the molecular sieve from the first inlet to the first outlet.

20. The process according to claim 19 , wherein the conveying device is a gravity conveying device and/or a mechanical conveying device selected from the group consisting of a reciprocating piston conveyor, a tube chain conveyor, a screw conveyor, a tube belt conveyor, a tube gravity conveyor, a belt conveyor, and a combination thereof.

21. The process according to claim 1 , wherein the gas stream is withdrawn from a second outlet of the gas-phase ultra-stabilizer reactor.

Assignees

• China Petroleum & Chem Corp
• Sinopec Res Inst Petroleum

Inventors

• Xu Mingde
• Zhang Jiexiao
• Zhou Lingping
• Zhang Weilin
• Tian Huiping
• Zhu Yuxia

Classifications

• B01J37/04

  Mixing {(B01J37/0009, B01J37/0018 take precedence)} · CPC title

• B01J2229/16

  to increase the Si/Al ratio; Dealumination · CPC title

• B01J37/0072

  Preparation of particles, e.g. dispersion of droplets in an oil bath · CPC title

• B01J37/06

  Washing {(B01J37/0009, B01J37/0018 take precedence)} · CPC title

• B01J29/088 Primary

  Y-type faujasite · CPC title