# US 4,394,349 A · Apparatus for the fluidized catalytic cracking of hydrocarbon feedstock

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- Number: US 4,394,349 A
- Document ID: US4394349A
- Status: Granted
- Kind: A
- Application number: 06/280,901
- Filed: 1981-07-06
- Granted: 1983-07-19
- Earliest claimed: 1981-07-06
- Assignees: Standard Oil Company (Indiana)
- Inventors: Robert R. Cartmell
- Web page: https://patentgrep.com/patent/US4394349A

## CPC

- B01J 8/0055: {using cyclones}
- C10G 11/18: according to the "fluidised-bed" technique
- B01J: CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- C10G: CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION (cracking to hydrogen or synthesis gas C01B; cracking or pyrolysis of hydrocarbon gases to individual hydrocarbons or mixtures thereof of definite or specified constitution C07C; cracking to cokes C10B); RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES

## Abstract

An apparatus for the fluidized catalytic cracking of a hydrocarbon feedstock comprises a riser reactor and a collar positioned along the same axis as the downstream end of the riser reactor. The collar is further positioned in close proximity to, but not in contact with, the riser reactor such that an annular space is defined between the riser reactor and the collar. The collar has a diameter greater than the diameter of the riser reactor at its downstream end and communicates directly and laterally with the inlets of the cyclone separation system. The riser reactor may or may not include a flow reversal cap to redirect the flow of the hydrocarbons and the catalyst.

## Claims

### Claim 1

An apparatus for the fluidized catalytic cracking of a hydrocarbon feedstock, the apparatus comprising:
(a) a disengaging vessel having a dense catalyst phase and a dilute catalyst phase;
(b) a vertically ascending riser reactor having means at its upstream end for the introduction of the feedstock and the catalyst, the riser reactor further having a downstream end communicating with the interior of the vessel;
(c) a collar having two open ends in communication with the interior of said disengaging vessel and positioned along the same axis as the downstream end of the riser reactor, the collar further being positioned in close proximity to, but not in contact with, the riser reactor such that an annular space is defined between the riser reactor and the collar, the collar having a diameter greater than the diameter of the riser reactor at its downstream end; and
(d) a cyclone separation system located within the vessel and having:
(i) an outlet communicating with the interior of the vessel to discharge catalyst into the dense phase;
(ii) an outlet connected to vent the cracked hydrocarbons outside the vessel; and
(iii) an inlet directly and laterally communicating with the collar;
whereby vapors from the vessel may enter the annular space defined by the collar through one open end thereof and may thereafter enter the cyclone separation system through said inlet.

### Claim 2 (depends on 1)

The apparatus of claim 1 wherein the downstream end of the riser reactor is tapered inwardly.

### Claim 3 (depends on 1)

The apparatus of claim 1 wherein the collar overlaps the riser reactor.

### Claim 4

An apparatus for the fluidized catalytic cracking of a hydrocarbon feedstock, the apparatus comprising:
(a) a disengaging vessel having a dense catalyst phase and a dilute catalyst phase;
(b) a vertically ascending riser reactor having means at its upstream end for the introduction of the feedstock and the catalyst, the riser reactor further having a downstream end communicating with the interior of the vessel;
(c) a collar positioned along the same axis as the downstream end of the riser reactor, the collar further being positioned in close proximity to the riser reactor such that an annular space open at both ends into the vessel is defined between the riser reactor and the collar, the collar having a diameter greater than the diameter of the riser reactor at its downstream end; and
(d) a cyclone separation system located within the vessel and having:
(i) an outlet communicating with the interior of the vessel to discharge catalyst into the dense phase;
(ii) an outlet connected to vent the cracked hydrocarbons outside the vessel; and
(iii) an inlet directly and laterally communicating with the collar;
and said collar being rigidly connected to said cyclone separation system, but not being in contact with said riser reactor, whereby differential thermal expansion between the riser reactor can occur without adverse effect.

### Claim 5

An apparatus for the fluidized catalytic cracking of a hydrocarbon feedstock, the apparatus comprising:
(a) a disengaging vessel having a dense catalyst phase and a dilute catalyst phase;
(b) a vertically ascending riser reactor having means at its upstream end for the introduction of the feedstock and the catalyst, having a downstream end communicating with the interior of the vessel, and including a flow reversal cap to redirect the flow of the hydrocarbons and the catalyst, the flow reversal cap being positioned at the downstream end of the riser reactor and in overlapping coaxial relationship therewith;
(c) a collar having two open ends in communication with the interior of said disengaging vessel and positioned along the same axis as the downstream end of the riser reactor, the collar further being positioned in close proximity to, but not in contact with, the riser reactor such that an annular space is defined between the riser reactor and the collar, the collar having a diameter greater than the diameter of the riser reactor at its downstream end; and
(d) a cyclone separation system located within the vessel and having:
(i) an outlet communicating with the interior of the vessel to discharge catalyst into the dense phase;
(ii) an outlet connected to vent the cracked hydrocarbons outside the vessel; and
(iii) an inlet directly and laterally communicating with the collar.

### Claim 6 (depends on 5)

The apparatus of claim 5 wherein the cross-sectional area of the annular space between the flow reversal cap and the remainder of the riser reactor is approximately equal to the cross-sectional area of the remainder of the riser reactor.