Apparatus for fluid catalytic cracking

Patent metadata

Field	Value
Publication number	US-10130929-B2
Application number	US-201214388217-A
Country	US
Kind code	B2
Filing date	Dec 24, 2012
Priority date	Mar 27, 2012
Publication date	Nov 20, 2018
Grant date	Nov 20, 2018

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. An apparatus for fluid catalytic cracking of hydrocarbon feed comprising:
(a) a regenerated catalyst holding vessel, an annular downer reactor concentric with an up-flow regenerator of circular cross section, an annular stripper concentric with the up-flow regenerator, wherein the up-flow regenerator, the regenerated catalyst holding vessel, the annular downer reactor, and the annular stripper being in fluid connection with each other;
(b) a radial catalyst distributor is positioned concentric with the upflow regenerator and located between the regenerated catalyst holding vessel and the annular downer reactor, the radial catalyst distributor comprising a plurality of stationary parts and a plurality of moving parts; each stationary part is a section of annulus having a shape of a circular sector with a predetermined vertex angle and the moving part is a section of an annulus having two parallel sides; each moving part being configured to move between edges of two stationary parts and to regulate catalyst flow from the regenerated catalyst holding vessel to the annular downer reactor and to create a variable flow area for the catalyst; the number of the moving parts being equal to the number of the stationary parts in the radial catalyst distributor; and
(c) 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 from the regenerated catalyst holding vessel into the annular downer reactor;
(d) feed injectors located circumferentially at equidistant locations at the outer circumference of the angular deflector plate to inject a hydrocarbon feed along with a diluent into the curtain flow of the catalyst just below the angular deflector plate;
(e) a plurality of conduits equipped with individual slide valves positioned between the stripper and the regenerator; and
wherein:
the regenerated catalyst holding vessel is positioned at top of the annular downer reactor and includes a regenerator termination device; and
the annular downer reactor terminates in the annular stripper placed at the bottom to separate products from the catalyst.

2. The apparatus as claimed in claim 1 , wherein the radial catalyst distributor controls generates a uniform circumferential flow of the catalyst from the regenerated catalyst holding vessel into the annular downer reactor.

3. The apparatus as claimed in claim 1 , wherein the particular vertex angle is calculated based on the number of stationary parts present in the radial catalyst distributor.

4. The apparatus as claimed in claim 1 , wherein the moving parts have parallel sides that move parallel to the edges of two adjacent stationary parts present in the radial catalyst distributor.

5. The apparatus of claim 1 , wherein said diluent is steam.

Assignees

• Indian Oil Corp Ltd
• 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

• B01J8/26

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

• B01J2208/0084

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

• C10G11/10

  with stationary catalyst bed · CPC title