Vessel comprising a bottom of decreasing cross section and variable angle of inclination, with lateral injections of liquid to limit fouling

Patent metadata

Field	Value
Publication number	US-11266963-B2
Application number	US-202016782197-A
Country	US
Kind code	B2
Filing date	Feb 5, 2020
Priority date	Feb 6, 2019
Publication date	Mar 8, 2022
Grant date	Mar 8, 2022

Abstract

A vessel for the downflow of a preferably hydrocarbon liquid, containing solid particles: a bottom comprising a cylindrical upper part (11), a lower part (12) with a decreasing cross section and a varying angle of inclination α with respect to the vertical axis (Z), and an outlet pipe (9); injections (5) and (6) of recirculated and/or of makeup liquid into the lower and upper parts respectively; injections (5) inclined with respect to the tangent to the wall of the lower part at the injection point by an angle β1 in the vertical plane (xz) and by an angle β2 in the horizontal plane (xy); injections (6) are inclined with respect to the wall of the upper part by an angle θ1 in the vertical plane (xz) and by an angle θ2 in the horizontal plane (xy).

First claim

The invention claimed is:

1. A method comprising injecting recirculated and/or makeup liquid into a bottom of a vessel ( 1 , 100 , 200 , 300 ) in which vessel there is
downflow of a liquid containing solid particles,
a bottom comprising a vertical cylindrical upper part ( 11 ) of diameter D 1 , a lower part ( 112 , 212 , 312 ) of decreasing cross section and variable angle of inclination α with respect to the vertical axis of revolution (Z) of the vertical cylindrical upper part, and an outlet pipe ( 9 ) of diameter D 2 , said method comprising
injecting of at least one injection ( 5 ) of said recirculated and/or makeup liquid into the said lower part ( 112 , 212 , 312 ) of decreasing cross section and variable angle of inclination;
injecting of at least one injection ( 6 ) of said recirculated and/or makeup liquid into the vertical cylindrical upper part ( 11 );
the said injection(s) ( 5 ) situated in the said lower part ( 112 , 212 , 312 ) being inclined with respect to the tangent (T in ) to the wall of the lower part at the injection point by an angle β 1 in the vertical plane (xz) and by an angle β 2 in the horizontal plane (xy); the said injection(s) ( 6 ) situated in the said vertical cylindrical upper part being inclined with respect to the wall of the vertical cylindrical upper part by an angle θ 1 in the vertical plane (xz) and by an angle θ 2 in the horizontal plane (xy), the angles β 1 and θ 1 being comprised between 5° and 175°, the angles β 2 and θ 2 being comprised between 0° and 180°.

2. The method according to claim 1 , wherein in the vessel the lower part ( 112 , 212 , 312 ) with decreasing cross section and variable angle of inclination comprises a convex portion ( 112 , 312 ).

3. The method according to claim 2 , wherein in the vessel the lower part ( 112 , 212 , 312 ) with decreasing cross section and variable angle of inclination is a convex portion of height L 1 with a ratio L 1 /D 1 comprised between 0.01 and 20.

4. The method according to claim 2 , wherein in the vessel the said lower part ( 112 , 212 , 312 ) with decreasing cross section and variable angle of inclination further comprises at least one frustoconical portion (s 1 ).

5. The method according to claim 4 , wherein in the vessel the ratio D 1 /D 3 is comprised between 0.05 and 0.9, D 3 being the smallest diameter of the said frustoconical portion (S 1 ) surmounting the said convex portion (b), and wherein the ratio L 3 /D 3 is comprised between 0.01 and 10, L 3 being the height of the said convex portion (b).

6. The method according to claim 2 , wherein in the vessel the convex portion comprises a solid insert forming a frustoconical internal surface of angle of inclination α′, comprised between 5° and 85°, the said insert at least partially incorporating the injections ( 5 ) situated in the said convex portion of the said lower part.

7. The method according to claim 2 , wherein the convex portion ( 112 , 312 ) has an elliptical cross section.

8. The method according to claim 1 , wherein in the vessel the said lower part ( 212 ) with decreasing cross section and variable angle of inclination comprises a succession of frustoconical portions (s 1 , s 2 , s 3 ).

9. The method according to claim 1 , wherein in the vessel, the center of the outlet pipe ( 9 ) is situated at a distance L 4 away from the wall of the vertical cylindrical upper part ( 11 ), L 4 being comprised between D 2 / 2 and D 1 / 2 .

10. The method according to claim 1 , comprising in the vessel a recirculation pipe ( 4 ) receiving part of the liquid leaving the said outlet pipe ( 9 ), the said recirculation pipe ( 4 ) supplying at least one of the said injections ( 5 ) or ( 6 ) with recirculated liquid.

11. The method according to claim 1 , comprising in the vessel a makeup pipe ( 10 ) supplying at least one of the said injections ( 5 ) or ( 6 ) with makeup liquid.

12. The method according to claim 1 , wherein in the vessel the injections are distributed in horizontal layers ( 7 ) in the lower part ( 112 , 212 , 312 ) and in horizontal layers ( 8 ) in the vertical cylindrical upper part ( 11 ), respectively.

13. The method according to claim 12 , wherein in the vessel the height H between two horizontal layers is comprised between 0.01 m and 10 m.

14. The method according to claim 12 , wherein the number of injections N per layer is comprised between 1 and 30.

15. The method according to claim 14 , wherein the injections into one and the same layer are spaced by an angle δ equal to 360/N.

16. The method according to claim 1 , wherein in the vessel the ratio D 1 /D 2 is comprised between 1.1 and 1000.

17. The method according to claim 1 , wherein in the vessel the diameter D 1 is comprised between 0.1 m and 30 m.

18. The method according to claim 1 , wherein in the vessel the angles β 1 and θ 1 are comprised between 10° and 150°.

19. The method according to claim 1 , wherein in the vessel the angles β 2 and θ 2 are comprised between 0° and 90°.

20. The method according to claim 1 , which is a gas/liquid separation processing hydrocarbon feedstocks.

21. The method according to claim 1 , that is an ebullated-bed hydroconversion of feedstocks containing hydrocarbon fractions of which at least 50 wt % have a boiling point above 300° C.

22. The method according to claim 21 , wherein the velocity V of the liquid injected in the said injections is comprised between 0.05 m·s −1 and 40 m·s −1 .

23. The method according to claim 21 , wherein the level of recirculated and/or of makeup liquid injected with respect to the hydrocarbon liquid circulating through the vessel is comprised between 1% and 400%.

Assignees

• Ifp Energies Now

Inventors

• Amblard Benjamin
• Marques Joao
• Le Coz Jean-Francois

Classifications

• B01J19/26

  Nozzle-type reactors, i.e. the distribution of the initial reactants within the reactor is effected by their introduction or injection through nozzles · CPC title

• C10G47/26

  suspended in the oil, e.g. slurries · CPC title

• B01J2219/194

  round · CPC title

• B01J4/001 Primary

  Feed or outlet devices as such, e.g. feeding tubes · CPC title

• B01J10/002

  carried out in foam, aerosol or bubbles · CPC title