Catalytic cracking method for treating a fraction having a low amount of conradson carbon

Patent metadata

Field	Value
Publication number	US-11060038-B2
Application number	US-202016751030-A
Country	US
Kind code	B2
Filing date	Jan 23, 2020
Priority date	Jun 30, 2011
Publication date	Jul 13, 2021
Grant date	Jul 13, 2021

Abstract

The present invention discloses a process for the catalytic cracking of a weakly coking feedstock having a Conradson carbon residue of 0.1% by weight and a hydrogen content of greater than 12.7% by weight, comprising at least a feedstock cracking zone, a zone for separating/stripping the effluents from the coked catalyst particles and a zone for regenerating said particles, characterized in that at least a solid carbon material in the fluidized state, having a carbon content equal to or greater than 80% by weight, is injected upstream of and/or during the catalyst regeneration step into a dense bed of coked catalyst.

First claim

The invention claimed is:

1. A plant for implementing a process for the catalytic cracking of a weakly coking feedstock having a Conradson carbon residue equal to or less than 0.1% by weight and a hydrogen content equal to or greater than 12.7% by weight, the plant comprising:
at least a main reactor comprising at least a feedstock cracking zone,
a disengager and a stripper for separating/stripping effluents from coked catalyst particles,
a single-stage or multistage regenerator for regenerating the coked catalyst particles,
a first and a second homogeneously dispersing means for homogeneously dispersing a solid carbon material in a divided state to form dispersed carbon material over the coked catalyst particles coming from the disengager and the stripper,
wherein the first homogeneously dispersing means is located upstream of the regenerator and the second homogenously dispersing means is located in the regenerator, wherein a grinding vessel adapted to grind carbon material is coupled to the first homogenously dispersing means, and
wherein the regenerator comprises a regeneration zone and is equipped with at least one structured packing placed downstream of the first and the second homogeneously dispersing means relative to an envisaged circulation of the catalyst in said regenerator, wherein the regeneration zone is capable of burning all of a mixture of coke on the coked catalyst particles and all of the dispersed solid carbon material to produce a regenerated catalyst having a reduced content of carbon material.

2. The plant according to claim 1 , characterized in that the first homogeneously dispersing means is placed in a line connecting the stripper to the regenerator and conveying stripped coked catalyst to said regenerator.

3. The plant according to claim 1 , characterized in that the second homogeneously dispersing means is placed in a dense part of a dense fluidized bed in the regenerator.

4. The plant according to claim 1 , characterized in that the second homogeneously dispersing means is capable of dispersing gas/solid mixtures in the dense fluidized bed, and comprises open tubes and/or rakes formed from several parallel tubes opening into the dense fluidized bed, wherein the tubes are connected to a manifold tube.

5. The plant according to claim 1 , wherein the at least one structured packing is formed by interlacing plates, strips or fins constituting a screen, and wherein the at least one structured packings occupies less than 10% of the flow cross section area of the regenerator.

6. The plant according to claim 1 , wherein the second homogeneously dispersing means includes an air blower.

7. The plant according to claim 1 , wherein the second homogenously dispersing means includes a carbon injection line and a DeSox or DeNox injector.

8. The plant according to claim 1 , wherein the disengager includes a cyclone.

Assignees

• Total Raffinage France
• Total Raffinage Chimie

Inventors

• Bories Marc
• Leroy Patrick
• Gbordzoe Eusebius

Classifications

• C10G2300/1014

  of vegetal origin · CPC title

• C10G2300/301

  Boiling range · CPC title

• B01J38/30

  in gaseous suspension, e.g. fluidised bed · CPC title

• C10G2300/708

  Coking aspect, coke content and composition of deposits · CPC title

• C07C2523/755

  Nickel · CPC title