Gas/liquid oligomerization reactor comprising transverse internals

Patent metadata

Field	Value
Publication number	US-12312288-B2
Application number	US-202017785525-A
Country	US
Kind code	B2
Filing date	Dec 8, 2020
Priority date	Dec 18, 2019
Publication date	May 27, 2025
Grant date	May 27, 2025

Abstract

The present invention relates to the field of gas/liquid reactors making possible the oligomerization of ethylene to give linear olefins by homogeneous catalysis with a reaction chamber comprising transverse internals capable of slowing down the ascent of the gaseous ethylene in the said reactor.

First claim

The invention claimed is:

1. A process for the oligomerization of gaseous ethylene employing a reactor comprising:
a reaction chamber ( 1 ) of elongated shape along the vertical axis;
a means for introduction of gaseous ethylene ( 2 ), located in a lower part of the reaction chamber;
a means for withdrawal ( 5 ) of a liquid fraction, located in the lower part of the reaction chamber;
a means for introducing a portion of the liquid fraction into a heat exchanger which is in fluid communication with said means for withdrawal ( 5 ) of the liquid fraction, and
a means for removing said portion of the liquid fraction from said heat exchanger and introducing said portion of the liquid fraction into a top part of the reaction chamber ( 1 ),
a means for bleeding off ( 4 ) a gaseous fraction, located at a top part of said reaction chamber;
wherein:
said chamber ( 1 ) comprises two or more transverse internals ( 11 ) wherein each transverse internal ( 11 ) is positioned over at least a part of a cross section of the reaction chamber ( 1 ) so as to increase residence time of gaseous ethylene in a liquid phase;
each of said internals exhibiting one or more openings ( 12 ) with a hydraulic diameter between 21 and 500 mm; and
said one or more openings ( 12 ) occupying between 20% and 80% of the total surface area of the cross section of the reaction chamber at which said internal is located, and
wherein said process comprises:
introducing a metal catalyst and an activating agent into the reaction chamber,
bringing said metal catalyst and the activating agent into contact with gaseous ethylene by the introduction of said gaseous ethylene into the lower part of the reaction chamber,
withdrawing the liquid fraction,
cooling the withdrawn liquid fraction by passing said liquid fraction through the heat exchanger,
introducing the cooled withdrawn liquid fraction into a top part of the reaction chamber,
recycling the gaseous fraction, withdrawn at a gas headspace positioned at an upper part of the top part of the reaction chamber by the means for bleeding off, and introducing the gaseous fraction at the lower part of the reaction chamber, into the liquid phase, and
wherein said process is carried out at a pressure between 0.1 and 10.0 MPa and at a temperature between 30 and 200° C.

2. The process of claim 1 , in which the transverse internals exhibit at least one opening ( 12 ) with a hydraulic diameter between 25 and 450 mm.

3. The process of claim 1 , in which the transverse internals ( 11 ) exhibit a plurality of openings with a hydraulic diameter between 21 and 500 mm.

4. The process of claim 1 , wherein said one or more openings ( 12 ) occupy/occupies between 25% and 75% of the total surface area of the cross section of the chamber on which said internal is located.

5. The process of claim 1 , in which the transverse internals ( 11 ) extend radially across a width of the chamber ( 1 ) of said reactor, and are suitable to slow down the ascent of the gaseous ethylene in the liquid phase.

6. The process of claim 1 , in which the transverse internals ( 11 ) are chosen from a perforated plate, a slit tray, a tray having valves, discs, and rings.

7. The process of claim 1 , in which the transverse internals ( 11 ) extend radially across only a portion of a width of the chamber ( 1 ) of said reactor, so as to be able to slow down the ascent of the gaseous ethylene in the liquid phase.

8. The process of claim 1 , in which the transverse internals ( 11 ) are selected from the group consisting of flat, curved, and pyramidal lateral plates.

9. The process of claim 1 , comprising at least two transverse internals ( 11 ), wherein the at least two transverse internals ( 11 ) are positioned alternately on the walls of the chamber ( 1 ).

10. The process of claim 1 , in which the chamber comprises a number of transverse internals between 2 and 30.

11. The process of claim 1 , wherein the transverse internals exhibit at least one opening ( 12 ) with a hydraulic diameter between 30 and 400 mm.

12. The process of claim 1 , wherein the transverse internals ( 11 ) exhibit a plurality of openings with a hydraulic diameter between 25 and 450 mm.

13. The process of claim 1 , wherein the transverse internals ( 11 ) exhibit a plurality of openings with a hydraulic diameter between 30 and 400 mm.

14. The process of claim 1 , wherein said one or more openings ( 12 ) occupy/occupies between 40% and 70% of the total surface area of the cross section of the chamber on which the said internal is located.

15. The process of claim 1 , wherein the chamber comprises a number of transverse internals between 2 and 20.

16. The process of claim 1 , wherein the chamber comprises a number of transverse internals between 2 and 15.

Assignees

• Ifp Energies Now

Inventors

• Augier Frederic
• Vonner Alexandre
• Maximiano Raimundo Pedro

Classifications

• B01J2219/00166

  controlling the residence time inside the reactor vessel · CPC title

• B01J19/24 Primary

  Stationary reactors without moving elements inside (B01J19/08, B01J19/26 take precedence; with stationary particles B01J8/02) · CPC title

• C07C2/24

  with metals · CPC title

• B01J2219/00765

  Baffles attached to the reactor wall · CPC title

• B01J19/006

  Baffles · CPC title