Method for oligomerization in a reactor comprising a gas/liquid double distributor

Patent metadata

Field	Value
Publication number	US-12364960-B2
Application number	US-202118269044-A
Country	US
Kind code	B2
Filing date	Dec 14, 2021
Priority date	Dec 23, 2020
Publication date	Jul 22, 2025
Grant date	Jul 22, 2025

Abstract

The present invention relates to a gas/liquid reactor for the oligomerization of gaseous ethylene, comprising a gaseous ethylene injection device and a liquid injection device, said injection devices advantageously being arranged so that the injection of the liquid can bring about a reduction, by shear, of the size of the ethylene bubbles, during the injection of the gaseous ethylene. The gas/liquid reactor according to the present invention may be used for any gaseous olefinic feedstock injected into a liquid phase.

First claim

The invention claimed is:

1. A process for the oligomerization of a gaseous olefinic feedstock, comprising:
the contact of a liquid comprising a catalytic system comprising a metal catalyst, at least one activator and at least one additive, and optionally a solvent; and the gaseous olefinic feedstock by a gas injection device and a liquid injection device, said injection devices being arranged so that the injection of the liquid brings about a reduction, by shear, in the size of the gaseous olefinic feedstock bubbles, said process using a gas/liquid reactor for the oligomerization of the gaseous olefinic feedstock comprising a gas injection device ( 3 ) comprising at least one gas injection orifice and a liquid injection device ( 12 ) comprising at least one liquid injection orifice, each gas injection orifice being located close to an orifice of the liquid injection device ( 11 ) and positioned so that the injection trajectory of the gas is in the plane of the injection trajectory of the liquid.

2. The process according to claim 1 , in which the at least one liquid injection orifice and the at least one gas injection orifice are circular, and in which the at least one liquid injection orifice have a diameter greater than or equal to the diameter of the at least one gas injection orifice.

3. The process according to claim 1 , in which at least one gas injection orifice and at least one liquid injection orifice are positioned facing each other at an angle of between 0° and 180°.

4. The process according to claim 1 , in which the gas injection and liquid injection devices are chosen from a pipe, a network of pipes, a multitubular distributor, a perforated plate, a cylindrical tube or a concentric tube.

5. The process according to claim 1 , in which the gas injection device is a cylindrical tube in the form of a circular ring having injection orifices and the liquid injection device is a cylindrical tube in the form of a circular ring having injection orifices.

6. The process according to claim 1 , in which the gas injection device in the form of a circular ring has a diameter less than that of the liquid injection device in the form of a circular ring, and in which said gas injection device is positioned inside the liquid injection device on a different plane.

7. The process according to claim 1 , in which a sequence of several liquid and gas injection devices in the form of a circular ring of decreasing diameters are alternated from the periphery to the centre represented by the central axis of the device having the largest diameter, said devices being positioned so that a gas injection orifice of a gas injection device is positioned close to an orifice of the adjacent liquid injection device so that the injection trajectory of the liquid is in the same plane as the injection trajectory of the gas so as to bring about shear of said gas.

8. The process according to claim 1 , in which the orifices of the gas and liquid injection devices are each extended by a tube ( 13 , 15 ).

9. The process according to claim 8 , in which the tube(s) ( 13 ) of the gas injection device ( 3 ) have a diameter smaller than that of the tube(s) ( 15 ) of the liquid injection device ( 12 ) and an open outlet end of the tube ( 13 ) of the gas injection device ( 3 ) is positioned coaxially inside the liquid injection tube.

10. The process according to claim 8 , in which the liquid injection tube ( 15 ) comprises a deflector.

11. The process according to claim 8 , in which the end of the liquid injection tube ( 15 ) has tapering of the outlet diameter.

12. The oligomerization process according to claim 1 , in which the gaseous olefinic feedstock comprises between 2 and 6 carbon atoms.

13. The oligomerization process according to claim 1 , in which the injection speed of the liquid is greater than the injection speed of the gaseous olefinic feedstock so as to promote shear of the size of the olefin gas bubbles to gas bubbles of smaller size.

14. The oligomerization process according to claim 1 , in which the gaseous olefinic feedstock comprises between 2 and 4 carbon atoms.

15. The process according to claim 1 , comprising:
a reaction chamber, of elongated shape along a vertical axis, which may contain a liquid phase located in a lower zone, comprising the products of the reaction, dissolved and gaseous olefinic feedstock, a catalytic system and an optional solvent, and a gas phase, located in an upper zone above the lower zone, comprising gaseous olefinic feedstock, and also uncondensable gases,
a pipe for introducing the catalytic system, said pipe being located in the lower part of the reaction chamber,
a recirculation loop comprising a withdrawing pipe at the base of the reaction chamber for withdrawing a liquid fraction, a heat exchanger for cooling said liquid, and a pipe for introducing said cooled liquid, the introduction pipe being located in the upper part of the lower zone of the reaction chamber,
and optionally a gas phase recycling loop to recycle at least a fraction of the gas phase into the lower zone of the liquid phase, comprising a withdrawing pipe located in the upper zone of the reaction chamber to enable the withdrawal of a gas fraction in the gas phase and an introduction pipe positioned in the lower zone of the reaction chamber to enable the introduction of said withdrawn gas fraction into the liquid phase.

16. The process according to claim 15 , wherein the liquid phase located in the lower zone consists of the products of the reaction, dissolved and gaseous olefinic feedstock, a catalytic system and an optional solvent.

17. The process according to claim 15 , wherein, in the liquid phase located in a lower zone, the dissolved and gaseous olefinic feedstock is dissolved and gaseous ethylene.

18. The process according to claim 15 , wherein, in the gas phase, located in an upper zone above the lower zone, the gaseous olefinic feedstock is gaseous ethylene.

19. The process according to claim 15 , wherein the uncondensable gases include ethane.

Assignees

• Ifp Energies Now

Inventors

• Raynal Ludovic
• Vonner Alexandre
• Maximiano Raimundo Pedro

Classifications

• C07C2/24

  with metals · CPC title

• B01J4/002

  Nozzle-type elements (nozzle-type reactors B01J19/26) · CPC title

• B01J19/26 Primary

  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

• B01J2219/185

  vertical · CPC title

• B01J2219/00103

  in a heat exchanger separate from the reactor · CPC title