Method for separating gas in a fluidized gas/solid mixture

1. A process for separating gases from a fluidized gas/solid mixture contained in a reactor, characterized in that the process comprises at least one step of injecting gas and at least one step of discharging gas, and optionally at least one step of injecting solids and at least one step of discharging solids, and further comprises a step of separating the solids entrained by the gas by passing the fluidized gas/solid mixture along an internal placed parallel to a free cross-sectional area of the reactor in a portion of the fluidized gas/solid mixture where a voidage is greater than 0.7, a cross section of the internal occupying less than 10% of the free cross-sectional area of the reactor and the internal comprising at least one unitary internal which comprises at least a first layer and a second layer of deflectors, and a ratio of a projected surface area of the internal to the free cross-sectional area of the reactor is greater than 0.75, wherein each of the deflectors comprises at least one plate, and wherein each of the first and second layers of deflectors comprises a plurality of deflectors such that the deflectors of the first layer are inclined in an opposite direction to the deflectors of the second layer, and wherein a lower edge of each of the plurality of deflectors of the first layer is immediately above an upper edge of each of the plurality of deflectors of the second layer.

2. The process according to claim 1 , characterized in that said internal is configured to limit an entrainment of the solids and not to increase a velocity of the gas passing through it by more than 10%.

3. The process according to claim 1 , characterized in that the internal occupies less than 5% of the free cross-sectional area of the reactor and the ratio of the projected surface area of the internal to the free cross-sectional area of the reactor varies from 0.8 to 1.

4. The process according to claim 1 carried out in a reactor for gas/solid separation in a fluidized catalytic bed, the reactor designed to contain the fluidized mixture and comprising gas and solid inlet ducts, at least one gas discharge duct and at least one solid discharge duct, an internal placed parallel to the free cross-sectional area of the reactor and occupying at most 10% of the free cross-sectional area of the reactor, and an area of the internal projected onto said free cross-sectional area of the reactor corresponds to more than 75% of said free cross-sectional area, the internal being placed in a portion of said reactor where the voidage is greater than 0.7, and in that said internal comprises at least one unitary internal which comprises at least two layers of deflectors, wherein each of the deflectors comprises at least one plate, and wherein each of the first and second layers of deflectors comprises a plurality of deflectors such that the deflectors of the first layer are inclined in an opposite direction to the deflectors of the second layer, and wherein a lower edge of each of the plurality of deflectors of the first layer is immediately above an upper edge of each of the plurality of deflectors of the second layer.

5. The process according to claim 4 , wherein gas/solid separation occurs in the fluidized bed of a regenerator of a catalytic cracking unit and/or of a disengager/stripper at an outlet of the reactor, in a least dense portion of the gas/solid mixture.

6. A reactor for implementing the process according to claim 1 , wherein the reactor is designed to contain the fluidized mixture, and comprises gas and solid inlet ducts, at least one gas discharge duct and at least one solid discharge duct, an internal parallel to and occupying at most 10% of said free cross-sectional area of the reactor, a surface area of the internal projected onto said free cross-sectional area of the reactor corresponds to more than 75% of said free cross-sectional area, and the internal being placed in a portion of said reactor where the voidage is greater than 0.7, and the internal comprises at least one unitary internal which comprises at least a first layer and a second layer of deflectors, wherein each of the deflectors comprises at least one plate, and wherein each of the first and second layers of deflectors comprises a plurality of deflectors such that the deflectors of the first layer are inclined in an opposite direction to the deflectors of the second layer, and wherein a lower edge of each of the plurality of deflectors of the first layer is immediately above an upper edge of each of the plurality of deflectors of the second layer.

7. The reactor according to claim 6 , characterized in that the lower edges of each of the deflectors of the first layer and the upper edges of each of the deflectors of the second layer placed immediately therebelow make an angle α that varies from 0 to 90 degrees.

8. The reactor according to claim 7 , characterized in that when the angle α is 0, the lower edges of the deflectors of the first layer are placed at a distance d from the upper edges of the deflectors of the second layer, d varying from 0 to E i .

9. The reactor according to claim 6 , characterized in that each of the plates in the first layer C 1 makes an angle θ 1 with the free cross-sectional area of the reactor, and each of the plates in the second layer C 2 makes an angle θ 2 with the free cross-sectional area of the reactor, wherein the first and second layers are successive layers and are identical or different, and wherein θ 2 is equal to θ 1 +90 or 180−θ 1 degrees.

10. The reactor according to claim 6 , characterized in that the at least one unitary internal comprises at least three layers of deflectors making an angle θ i to the free cross-sectional area of said reactor, and a rectifying layer comprising deflectors perpendicular to the free cross-sectional area of the reactor placed above the at least three layers of deflectors.

11. The reactor according to claim 6 , characterized in that the at least one plate makes an angle θ with the free cross-sectional area of the reactor such that sin θ is equal to a ratio of a thickness h of a single layer of deflectors to a width L of the plate.

12. The reactor according to claim 11 , characterized in that the at least one plate comprises at least two fins, the two fins having same widths and making a pairwise angle that varies from 0 to 90 degrees.

13. The reactor according to claim 11 , characterized in that the angle θ varies from 10 to 90 degrees.

14. The reactor according to claim 13 , characterized in that the angle θ varies from 10 to 60 degrees.

15. The reactor according to claim 13 , characterized in that the angle θ varies from 30 to 60 degrees.