Mixing and distribution device with mixing and exchange zones

Patent metadata

Field	Value
Publication number	US-9764299-B2
Application number	US-201615085466-A
Country	US
Kind code	B2
Filing date	Mar 30, 2016
Priority date	Apr 1, 2015
Publication date	Sep 19, 2017
Grant date	Sep 19, 2017

Abstract

Device for the mixing and distribution of fluids for a catalytic reactor with a downward flow, said device comprising at least one collection zone (A), at least one mixing zone (B) comprising at least one enclosure ( 15 ) for the mixing of the fluids, at least one distribution zone (C), characterized in that said mixing zone (B) is situated at the same level as the distribution zone (C) and also comprises at least one enclosure ( 16 ) for the exchange of the fluids, connected to, and communicating with, said mixing enclosure ( 15 ), said exchange enclosure ( 16 ) comprising at least one lateral passage section ( 17 a, 17 b ) suitable for the passage of the fluids from said exchange enclosure ( 16 ) to said distribution zone (C).

First claim

The invention claimed is:

1. Device for the mixing and distribution of fluids for a catalytic reactor with a downward flow, said device comprising:
at least one collection zone (A) comprising at least one collection means ( 5 );
at least one substantially vertical collection line ( 7 ) suitable for receiving a reaction fluid collected by said collection means ( 5 ) and at least one injection means ( 8 ) opening into said collection line ( 7 ) for injecting a quench fluid;
at least one mixing zone (B), situated downstream of said collection line ( 7 ) in the direction of circulation of the fluids and communicating with said collection line ( 7 ), said mixing zone (B) comprising at least one enclosure for mixing the fluids ( 15 );
at least one distribution zone (C), situated downstream of said mixing zone (B) in the direction of circulation of the fluids, comprising a distribution plate ( 12 ) supporting a plurality of chimneys ( 13 );

characterized in that said mixing zone (B) is situated at the same level as the distribution zone (C) and also comprises at least one enclosure ( 16 ) for the exchange of the fluids, connected to, and communicating with, said mixing enclosure ( 15 ), said exchange enclosure ( 16 ) comprising at least one lateral passage section ( 17 a , 17 b ) suitable for the passage of the fluids from said exchange enclosure ( 16 ) to said distribution zone (C).

2. Device according to claim 1 , characterized in that said mixing enclosure ( 15 ) is situated above said exchange enclosure ( 16 ).

3. Device according to claim 1 , characterized in that the cumulative total height H′ 2 of said mixing enclosure ( 15 ) and of said exchange enclosure ( 16 ) is comprised between 200 and 800 mm.

4. Device according to claim 1 , characterized in that the width W of said exchange enclosure ( 16 ) is comprised between 200 and 800 mm.

5. Device according to claim 1 , characterized in that the section of said mixing enclosure ( 15 ) and/or of said exchange enclosure ( 16 ) is a parallelogram.

6. Device according to claim 1 , characterized in that the volume ratio between said exchange enclosure ( 16 ) and said mixing enclosure ( 15 ) is comprised between 5 and 60%.

7. Device according to claim 1 , characterized in that the lateral passage sections ( 17 a , 17 b ) are distributed over at least two levels.

8. Device according to claim 1 , characterized in that said mixing enclosure ( 15 ) and said exchange enclosure ( 16 ) form a single piece.

9. Device according to claim 1 , characterized in that it comprises a dispersal system of the fluids, arranged below said distribution plate ( 12 ), said dispersal system comprising at least one dispersal means ( 19 ) of the fluids.

10. Device according to claim 9 , characterized in that said dispersal means ( 19 ) is a grid, the axis of said grid being perpendicular to the longitudinal axis of the enclosure of the reactor.

11. Device according to claim 1 , characterized in that said mixing enclosure ( 15 ) is positioned between two exchange enclosures ( 16 ).

12. Device according to claim 1 , characterized in that said mixing enclosure ( 15 ) comprises at least one deflecting means on at least one or more internal wall(s) of said mixing enclosure ( 15 ).

13. Device according to claim 1 , characterized in that said exchange enclosure ( 16 ) comprises a plurality of horizontal passage sections suitable for the passage of the fluids from said exchange zone ( 16 ) to the distribution plate ( 12 ).

14. Device according to claim 1 , characterized in that the enclosure or enclosures ( 15 ) and/or ( 16 ) closest to the distribution plate ( 12 ) is (are) situated at a distance “d” from said distribution plate ( 12 ) comprised between 20 and 150 mm.

15. Catalytic reactor with a downward flow comprising an enclosure ( 1 ) containing at least two fixed catalyst beds ( 2 , 14 ) separated by an intermediate zone comprising a device for the mixing and distribution of fluids according to claim 1 .

Assignees

• Ifp Energies Now

Inventors

• Beard Philippe
• Bazer-Bachi Frederic
• Plais Cecile
• Augier Frederic
• Haroun Yacine
• Delteil Jauffray

Classifications

• C10G65/10

  including only cracking steps · CPC title

• C10G47/00

  Cracking of hydrocarbon oils, in the presence of hydrogen or hydrogen- generating compounds, to obtain lower boiling fractions (C10G15/00 takes precedence; destructive hydrogenation of non-melting solid carbonaceous or similar materials C10G1/06) · CPC title

• C10G45/44

  Hydrogenation of the aromatic hydrocarbons · CPC title

• C10G45/02

  to eliminate hetero atoms without changing the skeleton of the hydrocarbon involved and without cracking into lower boiling hydrocarbons; Hydrofinishing · CPC title

• B01J2219/00765

  Baffles attached to the reactor wall · CPC title