Fixed bed or moving bed reactors with a radial flow of process stream to be treated, comprising improved internals

Patent metadata

Field	Value
Publication number	US-10702840-B2
Application number	US-201816012905-A
Country	US
Kind code	B2
Filing date	Jun 20, 2018
Priority date	Jun 21, 2017
Publication date	Jul 7, 2020
Grant date	Jul 7, 2020

Abstract

The present invention concerns reactors with a radial flow of process stream to be treated comprising improved internals which can be used to minimize the catalytic zones which do not receive any of the process stream which is to be treated. The invention also concerns the use of these radial flow reactors in refining or petrochemical processes.

First claim

The invention claimed is:

1. A reactor with a radial flow of process stream to be treated, comprising a shell ( 5 ), means for introducing process stream to be treated ( 4 ) and for effluents ( 11 ) to be removed, a zone for distributing said process stream ( 9 ), optional diplegs ( 6 ) for introducing catalyst, outer screens ( 3 ) and inner screens ( 2 ) to enable the process stream which is to be treated to move from an outer screen ( 3 ) to an inner screen ( 2 ) located substantially at the centre of the reactor, or conversely from the inner screen ( 2 ) to the outer screen ( 3 ), wherein said reactor further comprises at least one supplemental outer screen ( 13 , 18 ) having a shape which is adapted to that of the bottom of the reactor or the head of the reactor, said supplemental screen ( 13 , 18 ) being located in the extension of the outer screen ( 3 ).

2. The reactor as claimed in claim 1 , wherein the lower portion of the outer screen ( 3 ) rests on a support.

3. The reactor as claimed in claim 2 , wherein said support is perforated in order to allow the process stream to be treated to pass through.

4. The reactor according to claim 2 , wherein the lower portion of the outer screen ( 3 ) rests on a support ring ( 8 a ).

5. The reactor as claimed in claim 1 , wherein the lower portion of the surface of the inner screen ( 2 ) comprises one or more pieces ( 7 ) of solid plate, and a perforated plate comprising a zone with specific perforations ( 14 ) which differ from those of the remainder of the inner screen ( 2 ).

6. The reactor as claimed in claim 1 , wherein the upper portion of the surface of the inner screen ( 2 ) comprises one or more pieces ( 7 ) of solid plate, and a perforated plate comprising a zone with specific perforations ( 14 ) which differ from those of the remainder of the inner screen ( 2 ).

7. The reactor as claimed in claim 1 , wherein the outer screen ( 3 ) is composed of contiguous modules resting on a support ring or being suspended, each of the modules being extended into the bottom of the reactor in a manner forming a screen which is adapted to the bottom of the reactor.

8. The reactor as claimed in claim 7 , wherein said contiguous modules are composed of a plurality of assembled pieces.

9. The reactor as claimed in claim 1 , wherein said reactor is a moving bed reactor.

10. The moving bed reactor as claimed in claim 9 , wherein the series of pipes for introducing catalyst ( 6 ) discharges into an annular zone with a trapezoidal section (BSm) in which the catalyst is brought into partial contact with the process stream to be treated, the geometry of said trapezoidal section being such that the outer screen ( 3 ) is extended upwards and does not comprise a solid plate portion.

11. The moving bed reactor as claimed in claim 9 , wherein a solid plate inclined at an angle θ with respect to the horizontal, the angle θ being greater than the angle of repose, delimits the annular catalytic zone above the inner screen ( 2 ).

12. The reactor as claimed in claim 1 , wherein said reactor is a fixed bed reactor in which the catalyst is disposed between an outer screen ( 3 ) located at the periphery of the reactor and an inner screen ( 2 ) located substantially at the centre of the reactor.

13. The fixed bed reactor as claimed in claim 12 , wherein the bed of catalyst is located between a substantially horizontal solid plate ( 17 ) which isolates the upper portion of the catalytic bed of the head of the reactor, and a bed of inert beads which fills the bottom of the reactor.

14. The fixed bed reactor as claimed in claim 12 , wherein a second supplemental outer screen ( 18 ) is added above the outer screen ( 3 ) and in its extension.

15. A refining or petrochemical process consisting comprising continuous reforming of gasolines, skeletal isomerization of gasolines, olefin metathesis, oligocracking, dehydrogenation of paraffins or aromatics, or ammonia production, comprising subjecting a feed to reaction conditions in a reactor according to claim 1 .

Assignees

• Axens

Inventors

• Lambert Fabian

Classifications

• C10G45/66

  with moving solid particles · CPC title

• C10G45/58

  to change the structural skeleton of some of the hydrocarbon content without cracking the other hydrocarbons present, e.g. lowering pour point; Selective hydrocracking of normal paraffins (C10G32/00 takes precedence; improving or increasing the octane number or aromatic content of naphtha C10G35/00) · CPC title

• C10G35/12

  according to the "moving-bed" method · CPC title

• C10G35/04

  Catalytic reforming · CPC title

• C01C1/0429

  Fluidized or moving bed reactors · CPC title