# US 7,611,678 B2 · Multi-zone moving-bed reaction device with an addition of regenerated or fresh catalyst in each zone

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- Number: US 7,611,678 B2
- Document ID: US7611678B2
- Status: Granted
- Kind: B2
- Application number: 11/269,883
- Filed: 2005-11-09
- Published: 2006-06-08
- Granted: 2009-11-03
- Earliest claimed: 2004-11-09
- Assignees: Institut Francais du Petrole
- Inventors: Sylvain Louret; Patrice Font; Sylvie Lacombe; Eric Sancheż; Laurent Simon
- Web page: https://patentgrep.com/patent/US7611678B2

## CPC

- B01J 8/125: {with multiple sections one above the other separated by distribution aids, e.g. reaction and regeneration sections}
- B01J 8/085: {Feeding reactive fluids (for solid material, see B01J8/0015)}
- B01J 8/087: {Heating or cooling the reactor}
- C10G 50/00: Production of liquid hydrocarbon mixtures from lower carbon number hydrocarbons, e.g. by oligomerisation
- C10G 2300/1088: Olefins
- C10G 2300/4018: Spatial velocity, e.g. LHSV, WHSV
- C10G 2400/04: Diesel oil
- 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

A reaction device includes staged zones making it possible to implement strongly endothermic or exothermic reactions. The device reduces the differences in catalytic activity between these zones using an addition of fresh or regenerated catalyst at the inlet of each reaction zone and provides an integrated heat exchanger. A process of chemical conversion employs the device for gas-phase and/or liquid-phase exothermic or endothermic reactions, and in particular for the oligomerization reaction of C2 to C12 fractions for the purpose of producing a diesel fraction.

## Claims

### Claim 1

A reaction device comprising a catalytic reactor of elongated shape along an essentially vertical axis, said reactor comprising several vertically-staged catalytic reaction zones of similar diameters, said reactor being suitable for the circulation of at least one moving-bed granular catalyst that descends successively into each of the reaction zones and comprises means (100) for introducing and means (101) for evacuating a reaction fluid, means (102) for introducing fresh or regenerated catalyst at the top of the reactor, and means (105) for evacuating spent catalyst from a lower part of the reactor, said reactor comprising:
a) an upper reaction zone (3a), and a reaction zone (3b), located below upper reaction zone (3a), reaction zones are (3a) and (3b) being two successive reaction zones connected directly, on the one hand, by a path for reaction fluid and path for catalyst from zone (3a) to zone (3b).
b) means (2a) for introducing regenerated catalyst and/or fresh catalyst from the top of the reactor into upper reaction zone (3a), and
c) means (4a) within said reactor between reaction zones (3a) and (3b) for collecting spent catalyst obtained from upper reaction zone (3a), connected to:
d) means (7) within said reactor below said means (4a) for collecting spent catalyst and intermediate zone (3a) and (3b) for mixing at least a portion of spent catalyst thus collected with an addition of fresh or regenerated catalyst, connected to:
e) conduit (103) located outside said path for catalyst from zone (3a) to zone (3b) and entering said mixing zone for providing said addition of fresh or regenerated catalyst, and
f) means for passing the catalyst mixture thus produced in said means for mixing to the reaction zone (3b).

### Claim 2 (depends on 1)

A device according to claim 1, comprising means (104) connected to said collecting means (4a) for drawing-off and evacuating a portion of said spent catalyst obtained from upper reaction zone (3a).

### Claim 3 (depends on 2)

A device according to claim 2, in which two successive reaction zones (3a) and (3b) are connected by a circuit for circulation of the reaction fluid that passes through a heat exchange means (8) that is internal or external to said reactor.

### Claim 4 (depends on 3)

A device according to claim 3, in which said heat exchange means (8) is located inside the reactor, in an intermediate zone (22) located between two successive reaction zones (3a) and (3b).

### Claim 5 (depends on 4)

A device according to claim 4, in which said heat exchange means (8) is a heat exchanger located in said intermediate zone at a constriction in the path of a catalyst from zone (3a) to zone (3b).

### Claim 6 (depends on 3)

A device according to claim 3, in which said intermediate zone comprises means (10) for introducing one or more additional reaction fluids (106) and for mixing this fluid or these fluids with the reaction fluid that circulates between successive reaction zones (3a) and (3b).

### Claim 7 (depends on 4)

A device according to claim 4, in which said intermediate zone comprises means (10) for introducing one or more additional reaction fluids (106) and for mixing this fluid or these fluids with the reaction fluid that circulates between successive reaction zones (3a) and (3b).

### Claim 8 (depends on 2)

A device according to claim 2, in which said intermediate zone comprises means (10) for introducing one or more additional reaction fluids (106) and for mixing this fluid or these fluids with the reaction fluid that circulates between successive reaction zones (3a) and (3b).

### Claim 9 (depends on 2)

A reactor system according to claim 2 further comprising a source of fresh and/or regenerated granular catalysts;
conduit means connecting said source with both the top of the reactor and the means (7) for mixing, said conduit means comprising valve means for regulating relative amounts of fresh and/or regenerated catalysts to be transported to the top of the reactor and to the means for mixing, and for replenishing withdrawn spent catalysts.

### Claim 10 (depends on 1)

A device according to claim 1, in which two successive reaction zones (3a) and (3b) are connected by a circuit for circulation of the reaction fluid that passes through a heat exchange means (8) that is internal or external to said reactor.

### Claim 11 (depends on 10)

A device according to claim 10, in which said heat exchange means (8) is located inside the reactor, in an intermediate zone (22) located between two successive reaction zones (3a) and (3b).

### Claim 12 (depends on 11)

A device according to claim 11, in which said heat exchange means (8) is a heat exchanger located in said intermediate zone at a constriction in the path of a catalyst from zone (3a) to zone (3b).

### Claim 13 (depends on 11)

A device according to claim 11, in which said intermediate zone comprises means (10) for introducing one or more additional reaction fluids (106) and for mixing this fluid or these fluids with the reaction fluid that circulates between successive reaction zones (3a) and (3b).

### Claim 14 (depends on 10)

A device according to claim 10, in which said intermediate zone comprises means (10) for introducing one or more additional reaction fluids (106) and for mixing this fluid or these fluids with the reaction fluid that circulates between successive reaction zones (3a) and (3b).

### Claim 15 (depends on 11)

A device according to claim 11, in which said intermediate zone comprises means (10) for introducing one or more additional reaction fluids (106) and for mixing this fluid or these fluids with the reaction fluid that circulates between successive reaction zones (3a) and (3b).

### Claim 16 (depends on 12)

A device according to claim 12, in which said intermediate zone comprises means (10) for introducing one or more additional reaction fluids (106) and for mixing this fluid or these fluids with the reaction fluid that circulates between successive reaction zones (3a) and (3b).

### Claim 17 (depends on 5)

A device according to claim 5, in which said intermediate zone comprises means (10) for introducing one or more additional reaction fluids (106) and for mixing this fluid or these fluids with the reaction fluid that circulates between successive reaction zones (3a) and (3b).

### Claim 18 (depends on 1)

A device according to claim 1, wherein said conduit (103) enters laterally through the reactor into the means (7) for mixing.