Three dimensional structured packing for improving the contact between a gas phase and a dispersed solid phase following in counter-current

US11168264B2 · US · B2

Patent metadata
FieldValue
Publication numberUS-11168264-B2
Application numberUS-201716469041-A
CountryUS
Kind codeB2
Filing dateDec 5, 2017
Priority dateDec 14, 2016
Publication dateNov 9, 2021
Grant dateNov 9, 2021

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  1. Title

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  5. First independent claim

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Abstract

Official abstract text for this publication.

The present invention describes a packing with a three-dimensional structure which is particularly suited to creating homogenous and anisotropic mixing between the gas phase and a dispersed solid phase moving in counter-current flow. Application of this packing to the stripper of fluidized catalytic cracking units.

First claim

Opening claim text (preview).

The invention claimed is: 1. A three-dimensional structured packing for homogeneous contact between a gas phase and an emulsion phase flowing in counter-current, said packing comprising: a plurality of three-dimensional structures, each three-dimensional structure having an elementary pattern produced by 3 secant planes, said elementary pattern being a complex volume comprising 3 vanes, each vane respectively belonging to one of the 3 secant planes and the 3 secant planes, when considered in pairs of the planes, always have an intersection, and wherein the plurality of elementary patterns are distributed in a plurality of parallel distribution planes with each distribution plane being distinct from the 3 secant planes of the three-dimensional structures therein with a triangular pitch spacing, these distribution planes each being referred to as a distribution layer and the plurality of parallel distribution planes being referred to as a plurality of parallel distribution layers, and wherein the plurality of parallel distribution layers are stacked in the form of a vertical stack, each distribution layer having the same density of elementary patterns, and wherein in said packing said elementary patterns are inscribed inside a triangular-pitch mesh, the pitch spacing being from 1 to 1.5 times the minimum distance (d) defined by d=(a+a*cos(60°)+b/2 sin(90°- α)), wherein angle (α) is the angle that the vanes of the pattern make with the horizontal, and which is between 45° and 75°, (a) is the width of the vanes and is between 3 cm and 30 cm, and (b) is the distance separating two successive distribution layers and is between 3 cm and 50 cm, and successive distribution layers being such that, from one layer to the next, the triangle formed by the 3 most closely-spaced elementary patterns belonging to the layer (N) is offset in layer (N+1) so that the vertex of a triangle of the layer (N+1) lies at center of a circle inscribed inside the triangle of the layer (N). 2. The three-dimensional structured packing as claimed in claim 1 , in which the triangular pitch spacing at which the elementary patterns in a given layer are distributed is between 1.1 and 1.3 times the minimum distance (d). 3. The three-dimensional structured packing as claimed in claim 1 , in which the rotational orientation of the elementary patterns changes by an angle of 180° from one layer to the next layer. 4. The three-dimensional structured packing as claimed in claim 1 , in which the rotational orientation of the elementary patterns changes randomly from one layer to the next. 5. The three-dimensional structured packing as claimed in claim 1 , in which both the rotational orientation of the elementary patterns and the offset of the triangles formed by 3 adjacent patterns change from one layer to the next. 6. The three-dimensional structured packing according to claim 1 , wherein angle (α) is between 55° and 65°. 7. The three-dimensional structured packing according to claim 1 , wherein (a) is between 5 cm and 15 cm. 8. The three-dimensional structured packing according to claim 1 , wherein (b) is between 6 cm and 20 cm. 9. The three-dimensional structured packing according to claim 1 , wherein angle (a) is between 55° and 65°, (a) is between 5 cm and 15 cm, and (b) is between 6 cm and 20 cm. 10. The three-dimensional structured packing as claimed in claim 1 , in which the rotational orientation of the elementary patterns changes by an angle between 10° and 180° from one layer to the next layer. 11. The three-dimensional structured packing as claimed in claim 1 , in which the rotational orientation of the elementary patterns changes by an angle between 120° and 180° from one layer to the next layer. 12. The three-dimensional structured packing as claimed in claim 1 , in which the rotational orientation of the elementary patterns changes by an angle between 150° and 180° from one layer to the next layer. 13. The three-dimensional structured packing according to claim 1 , wherein the elementary patterns repeat in each distribution layer with the triangular pitch spacing being such that there is no overlap between the vanes of adjacent elementary patterns in each distribution layer. 14. The three-dimensional structured packing according to claim 1 , wherein each of said vanes is rectangular. 15. A method for catalytic cracking comprising: conducting said catalytic cracking using the packing as claimed in claim 1 as a means for improving contact between an upflow gas phase and a downflow emulsion phase, said packing being placed inside a stripper of a catalytic cracking unit, said stripper operating as a fluidized bed with a fluidization rate of between 10 cm/s and 40 cm/s. 16. A method for catalytic cracking comprising: conducting said catalytic cracking using the packing as claimed in claim 1 , said packing being placed inside a stripper of a catalytic cracking unit, and said stripper operating with a solid stream flow rate of between 25 and 200 kg/m 2· s. 17. The method according to claim 16 , wherein said stripper operates with a solid stream flow rate of between 50 and 150 kg/m 2 ·s. 18. A method for catalytic cracking comprising: conducting said catalytic cracking using the packing as claimed in claim 1 , said method being a deep catalytic cracking (DCC) method for catalytic cracking of hydrocarbon fractions. 19. A method of manufacturing the packing as claimed in claim 1 , comprising manufacturing said packing by additive manufacturing. 20. A three-dimensional structured packing for homogeneous contact between a gas phase and an emulsion phase flowing in counter-current, said packing comprising: a plurality of three-dimensional structures, each three-dimensional structure having an elementary pattern produced by 3 non-parallel planes, said elementary pattern being a complex volume comprising 3 vanes, each vane respectively belonging to one of said 3 non-parallel planes, and the 3 non-parallel planes, when considered in pairs of the planes, always have an intersection, and wherein the plurality of elementary patterns are distributed in a plurality of parallel distribution planes with each distribution plane being distinct from the 3 non-parallel planes of the three-dimensional structures therein with a triangular pitch spacing, these distribution planes each being referred to as a distribution layer and the plurality of parallel distribution planes being referred to as a plurality of parallel distribution layers, and wherein the plurality of parallel distribution layers are stacked in the form of a vertical stack, each distribution layer having the same density of elementary patterns, and wherein in said packing said elementary patterns are inscribed inside a triangular-pitch mesh, the pitch spacing being from 1 to 1.5 times the minimum distance (d) defined by d=(a+a*cos(60°+b/2 sin(90°- α)), wherein angle (α) is the angle that the vanes of the pattern make with the horizontal, and which is between 45° and 75°, (a) is the width of the vanes and is between 3 cm and 30 cm, and (b) is the distance separating two successive distribution layers and is between 3 cm and 50 cm, and successive distribution layers being such that, from one layer to the next, the triangle formed by the 3 most closely-spaced elementary patterns belonging to the layer (N) is offset in layer (N+1) so that the vertex of a triangle of the layer (N+1) lies at the center of a circle inscribed inside the triangle of the layer (N).

Assignees

Inventors

Classifications

  • Dimensions or size aspects · CPC title

  • Basic shape of the elements · CPC title

  • Counter-current flow · CPC title

  • Inclined orientation · CPC title

  • Details relating to packing elements in the form of grids or built-up elements for forming a unit of module inside the apparatus for mass or heat transfer · CPC title

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What does patent US11168264B2 cover?
The present invention describes a packing with a three-dimensional structure which is particularly suited to creating homogenous and anisotropic mixing between the gas phase and a dispersed solid phase moving in counter-current flow. Application of this packing to the stripper of fluidized catalytic cracking units.
Who is the assignee on this patent?
Ifp Energies Now
What technology area does this patent fall under?
Primary CPC classification C10G11/18. Mapped technology areas include Chemistry & Metallurgy.
When was this patent published?
Publication date Tue Nov 09 2021 00:00:00 GMT+0000 (Coordinated Universal Time) (B2). Legal status and post-grant events are not shown on this page.
What related patents are in patentsdb?
We list 1 related publication on this page (citations in our corpus or others sharing the same primary CPC).