Process for fluid catalytic cracking

Patent metadata

Field	Value
Publication number	US-10273417-B2
Application number	US-201815988909-A
Country	US
Kind code	B2
Filing date	May 24, 2018
Priority date	Mar 27, 2012
Publication date	Apr 30, 2019
Grant date	Apr 30, 2019

Abstract

An apparatus which is an integral hardware consisting of an annular downer reactor and a concentric upflow riser regenerator for catalytic cracking of hydrocarbon feed to is disclosed. The annular downer reactor terminates in annular stripper which is also concentric with the regenerator. The regenerator, reactor and stripper are in fluid connection with each other. The apparatus is highly compact and provides efficient contact between circulating catalyst and hydrocarbon feed. The proposed hardware includes a novel radial distributor for providing improved control and radial distribution of catalyst inside the downflow reactor. The radial distributor has equal numbers of stationary and movable parts placed one after another to cover the entire annular opening at the bottom of the regenerated catalyst vessel. The radial distributor is concentric with regenerator and located between the catalyst holding vessel and the reactor. A process for catalytic cracking using the invented apparatus is also disclosed.

First claim

We claim:

1. A process for catalytic cracking of hydrocarbon, comprising:
collecting regenerated fluid catalytic cracking (FCC) catalyst from an up-flow regenerator in a catalyst holding vessel of an apparatus adapted for catalytic cracking of hydrocarbon;
controlling a uniform circumferential catalyst flow into an annular downer reactor of the apparatus by a radial distributor, the annular downer reactor being concentric with an up-flow regenerator of circular cross section;
allowing the uniform circumferential catalyst flow to fall on an angular deflector plate to form a curtain flow of catalyst in to the annular downer reactor;
injecting a hydrocarbon feed along with a diluent into the curtain flow of catalyst just below the deflector plate using feed injectors and allowing the catalyst, diluent and the feed to move down through the annular downer reactor;
recovering hydrocarbon vapors entrapped in catalyst pores by the use of steam in a stripper of the apparatus;
separating the hydrocarbon vapors and diluent from spent catalyst in the stripper using a separation device; and
returning the spent catalyst to the regenerator using one or more conduits equipped with individual slide valves.

2. The process as claimed in claim 1 , wherein the catalyst has a residence time between 5 to 60 seconds in the up-flow regenerator.

3. The process as claimed in claim 1 , wherein the catalyst and the feed have a residence time between 0.1 to 2 second in the annular downer reactor.

4. A process for catalytic cracking of hydrocarbon, comprising:
using an apparatus for fluid catalytic cracking (FCC) of hydrocarbon feed, the apparatus including:
(a) an annular downer reactor, concentric with an up-flow regenerator of circular cross section, which terminates in annular stripper, the stripper being concentric with the regenerator and the regenerator, reactor and stripper being in fluid connection with each other;
(b) a plurality of conduits equipped with individual slide valves positioned between the stripper and the regenerator;
(c) a catalyst holding vessel positioned at the top of the reactor containing a regenerator termination device;
(d) a radial catalyst distributor positioned concentric with the up-flow regenerator and located between the regenerated catalyst holding vessel and the annular downer reactor; and
(e) an angular deflector plate with an angle of inclination varying between 30° to 80° with horizontal and located below the catalyst distributor and along the outer circumference of the up flow regenerator, to generate a curtain flow of catalyst into the annular downer reactor; collecting the regenerated FCC catalyst from the up-flow regenerator in the catalyst holding vessel;

controlling a uniform circumferential catalyst flow into the annular downer reactor by the radial catalyst distributor;
allowing a uniform circumferential catalyst flow to fall on the angular deflector plate to form a curtain flow of catalyst in to the annular downer reactor;
injecting the hydrocarbon feed along with a diluent steam into the curtain flow of catalyst just below the deflector plate using feed injectors and allowing the catalyst, diluent and the feed to move down through the annular downer reactor;
recovering hydrocarbon vapors entrapped in catalyst pores by use of stream in the stripper;
separating the hydrocarbon vapors and diluent from the spent catalyst in the stripper using a separation device; and
returning the spent catalyst to the regenerator using one or more conduits equipped with individual slide valves.

5. The process as claimed in claim 4 , wherein the catalyst has a residence time between 5 to 60 seconds in the up-flow regenerator.

6. The process as claimed in claim 4 , wherein the catalyst and the feed have a residence time between 0.1 to 2 second in the annular downer reactor.

7. The process as claimed in claim 4 , wherein the radial catalyst distributor controls the uniform circumferential catalyst flow into the reactor.

8. The process as claimed in claim 4 , wherein the radial catalyst distributor comprises a plurality of stationary parts and a plurality of moving parts.

9. The process as claimed in claim 8 , wherein the number of moving parts is equal to the number of stationary parts.

10. The process as claimed in claim 8 , wherein each stationary part has a shape of a circular sector of a particular vertex angle calculated based on the number of stationary parts required.

11. The process as claimed in claim 8 , wherein each moving part is a section of annulus with two sides parallel and moving parallel to edges of two adjacent stationary parts.

12. The process as claimed in claim 4 , wherein the up-flow regenerator is used as a lift line and the catalyst holding vessel is used as the regenerator, operated either under partial or full combustion mode.

13. The process as claimed in claim 4 , wherein the process is used for performing simultaneous pyrolysis and gasification reactions.

14. The process as claimed in claim 13 , wherein the pyrolysis is done in the down-flow reactor and gasification of resulting char from the pyrolysis is done in the up-flow regenerator.

15. The process as claimed in claim 4 , wherein the up-flow regenerator can be used for cracking reaction, the catalyst holding vessel can be used as the stripper, the down-flow reactor can be used as the regenerator and the stripper can be used as the regenerator.

16. The process as claimed in claim 4 , wherein the process provides an annular downer reactor without compromising a central tubular area which is used for regeneration of the spent catalyst.

Assignees

• Indian Oil Corp Ltd

Inventors

• Sadhullah Mukthiyar
• Kumaran Satheesh Vetterkunnel
• Bhattacharyya Debasis
• Saidulu Gadari
• Kukade Somnath
• Kumar Brijesh
• Rajagopal Santanam

Classifications

• C10G11/18 Primary

  according to the "fluidised-bed" technique · CPC title

• B01J8/386

  internally, i.e. the particles rotate within the vessel · CPC title

• B01J2208/0084

  inside the bed, e.g. baffles · CPC title

• B01J8/26

  with two or more fluidised beds, e.g. reactor and regeneration installations · CPC title

• C10G11/10

  with stationary catalyst bed · CPC title