Classifications

• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
  • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
  • B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
  • B01J8/005—Separating solid material from the gas/liquid stream
• • C—CHEMISTRY; METALLURGY
  • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
  • C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
  • C10G11/00—Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils
  • C10G11/14—Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils with preheated moving solid catalysts
  • C10G11/18—Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils with preheated moving solid catalysts according to the "fluidised-bed" technique
  • C10G11/182—Regeneration
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
  • B01D—SEPARATION
  • B01D45/00—Separating dispersed particles from gases or vapours by gravity, inertia, or centrifugal forces
  • B01D45/12—Separating dispersed particles from gases or vapours by gravity, inertia, or centrifugal forces by centrifugal forces
  • B01D45/16—Separating dispersed particles from gases or vapours by gravity, inertia, or centrifugal forces by centrifugal forces generated by the winding course of the gas stream, the centrifugal forces being generated solely or partly by mechanical means, e.g. fixed swirl vanes
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
  • B01D—SEPARATION
  • B01D50/00—Combinations of methods or devices for separating particles from gases or vapours
  • B01D50/20—Combinations of devices covered by groups B01D45/00 and B01D46/00
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
  • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
  • B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
  • B01J8/18—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles
  • B01J8/1872—Details of the fluidised bed reactor
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
  • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
  • B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
  • B01J8/18—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles
  • B01J8/24—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles according to "fluidised-bed" technique
  • B01J8/34—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles according to "fluidised-bed" technique with stationary packing material in the fluidised bed, e.g. bricks, wire rings, baffles
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
  • B01D—SEPARATION
  • B01D45/00—Separating dispersed particles from gases or vapours by gravity, inertia, or centrifugal forces
  • B01D45/12—Separating dispersed particles from gases or vapours by gravity, inertia, or centrifugal forces by centrifugal forces
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
  • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
  • B01J2208/00—Processes carried out in the presence of solid particles; Reactors therefor
  • B01J2208/00743—Feeding or discharging of solids
  • B01J2208/00761—Discharging
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
  • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
  • B01J2208/00—Processes carried out in the presence of solid particles; Reactors therefor
  • B01J2208/00796—Details of the reactor or of the particulate material
  • B01J2208/00823—Mixing elements
  • B01J2208/00831—Stationary elements
  • B01J2208/0084—Stationary elements inside the bed, e.g. baffles

Definitions

• TITLE SEPARATION AND STRIPING ENCLOSURE WITH A DEBRIS FILTRATION GRID
• the subject of the invention is a separation and stripping enclosure, in particular for an effluent from a fluidized bed catalytic cracking unit, comprising a debris filtration grid.
• Separation and stripping enclosures are generally used in fluidized bed catalytic cracking or FCC processes.
• the effluent leaving the catalytic cracking reactor is separated from the particles it contains, namely coked catalytic particles, which undergo a stripping operation before being sent to the regenerator of the FCC unit in order to be regenerated there by burning coke.
• separation and stripping enclosures also called “disengager/stripper”
• disengager/stripper thus usually comprise at least one particle separation system and a particle stripping section located downstream of the at least one separation system with respect to the circulation of particles inside the enclosure, generally from top to bottom.
• pieces of coke and/or of a protective coating covering the internal face of the side wall of the separation and stripping enclosure become detached and fall, thus ending up in the stripping section.
• Such pieces present at the level of this stripping section can degrade the course of the stripping, especially when the stripping section contains structured internal elements, also called “linings” or “packings”, which can be clogged by these pieces.
• an enclosure for separating and stripping an effluent containing particles comprising a side wall delimiting an internal volume having a longitudinal axis and, inside the internal volume, a particle separation section and a particle stripping section located downstream of the separation section with respect to the circulation of the particles inside the enclosure.
• the enclosure comprises, upstream of the stripping section or of a zone of the stripping section provided with stripping elements extending through the internal transverse section of the enclosure, at least a grid extending transversely to the longitudinal axis. It can be a single grid or two or more grids.
• the projection of a single grid or all of the grids on a transverse plane perpendicular to the longitudinal axis covers 80 to 100% of the internal cross section of the enclosure.
• the screen(s) will make it possible to retain some of the pieces of coke and/or coating coming from the upper part of the enclosure and prevent them from entering the stripping section, thus reducing the risks of disruption of the stripping operation. stripping.
• the projection of the grille(s) may extend through the entire internal cross-section of the enclosure. However, this can be difficult to achieve when the available space is limited, in particular due to the presence of internal equipment such as particle separation devices, reactor, etc.
• the projection of a single grid or all of the grids on a transverse plane perpendicular to the longitudinal axis can cover from 80 to 100% of the surface of an internal free volume of the enclosure projected along the axis longitudinal in the plane of the single grid or in the plane of the proximal grid of the stripping section or of the zone of the stripping section provided with stripping elements (the lowest grid).
• This internal free volume of the enclosure is defined as a part of the internal volume of the enclosure devoid of any equipment other than a grid according to the invention and located upstream of the single grid or of the proximal grid.
• the grid or grids then do not necessarily extend under the equipment present inside the enclosure along the longitudinal axis.
• the geometry of the grid(s) may thus depend on the geometry of the equipment present inside the containment, in particular in the separation section thereof.
• one or more grids may be provided. Where two or more grids are provided, they may preferably be arranged at different positions along the longitudinal axis. When two or more grids are provided, their projections on a transverse plane perpendicular to the longitudinal axis may or may not partially overlap.
• said at least one grid, and in particular each grid can extend continuously over at least 300° around the longitudinal axis and its projection on a transverse plane perpendicular to the longitudinal axis can cover at least a part of the internal cross-section of the enclosure and extend radially over at least part of the distance separating the longitudinal axis from the side wall of the enclosure.
• the projection of said at least one grid can cover a part of the internal cross-section of the enclosure extending radially over only part of the distance separating the longitudinal axis from the side wall of the enclosure.
• This part may in particular be chosen from:
• the stripping section of an FCC unit generally has a part provided with stripping elements whose function is to promote contact between the stripping fluid and the solid particles to be stripped.
• These stripping elements can be baffles or packings, called “packing" in English, located upstream (with respect to the direction of circulation of the particles) of the main injection system of the stripping fluid, which circulates against the current of the particles. .
• These stripping elements extend through the internal cross-section of the enclosure and can be distributed in several stages along the longitudinal axis of the enclosure. Examples of packings are described in the documents EP719850, US7022221, US7077997 and W02007/094771, WOOO/35575, CN1763150, EP1577368, EP1577368A1.
• a stripping section can comprise one or more other systems for injecting stripping fluid located between stages of stripping elements and/or at the entrance to the stripping section, therefore upstream of the stripping elements.
• the solid particles entering the stripping section thus first pass through a stripping element located furthest upstream from the stripping section with respect to the circulation of the particles.
• said at least one grid may advantageously be formed of a plurality of intersecting walls defining meshes and the dimensions of a mesh, measured in a plane perpendicular to the longitudinal axis, can advantageously be smaller than the dimensions of an opening of the zone of the stripping section, measured in a plane perpendicular to the longitudinal axis.
• the grid only lets through debris whose dimensions are less likely to block the openings of the most upstream stripping element.
• said at least one grid may be formed of a plurality of intersecting walls defining meshes and these walls may extend parallel or substantially parallel to the axis of the enclosure. This reduces the impact of the grid on the circulation of the stripping fluid and the cracked hydrocarbons inside the containment. When the grid is located at the level of a particle circulation zone, this arrangement also makes it possible to reduce the impact of the grid on the circulation of the particles and to limit the erosion of the grid by the latter.
• said at least one grid can be formed of a plurality of intersecting walls defining meshes and adjacent meshes can have wall portions of different height measured parallel to the longitudinal axis. This can help limit coke chunks/debris being thrown back out of the grid. Such a return can result from a rebound during their fall or vibrations of the installation, in particular when the grid extends in a horizontal plane.
• At least one grid among said at least one grid may have the shape of a cone or a truncated cone widening from upstream to downstream with respect to the circulation of the particles.
• the grid is thus inclined with respect to the longitudinal axis, favoring the evacuation of debris towards the side wall of the enclosure and their retention.
• This type of grid will therefore preferably be fixed to the side wall of the enclosure, in particular only to the latter, the debris then accumulating between the edge of the grid and the side wall of the enclosure and freeing the center of the enclosure for the circulation of fluids.
• this type of grid may extend radially from the side wall towards the longitudinal axis over part of the distance separating the side wall from the longitudinal axis, in particular over 360° around the longitudinal axis.
• the apex angle of a cone or truncated cone grid can be 20° to 70°, preferably 30° to 50°.
• At least one grid among said at least one grid can be a flat grid which extends in a plane perpendicular to the longitudinal axis. This type of grid can be attached only to the side wall or only to at least one separation device located in the separation section.
• said at least one grid can be fixed only to the side wall of the enclosure.
• said at least one grid can be fixed only to at least two separation devices, or even to at least four fixing devices, optionally to each of the separation devices.
• said at least one grid may not extend radially beyond the separation devices, which may reduce the risks of vibration of the grid. In other words, the grid then extends only between the separation devices, at a distance from the side wall.
• said at least one grid can be fixed only to at least two evacuation pipes, or even to at least four evacuation pipes, optionally to each evacuation pipe.
• said at least one grid may comprise at least one orifice through which said at least one separation device passes.
• This orifice may in particular surround the separation device at a distance from the latter corresponding to an expansion clearance. This will prevent the grid from coming into contact with the separation device at the orifice.
• the separation device is a separation device provided with a discharge pipe towards the stripping section, this pipe extending generally parallel or substantially parallel to the longitudinal axis, the orifice can be crossed by the evacuation pipe.
• the enclosure includes a separation device extending along the longitudinal axis, the orifice can then be central to surround this separation device.
• the separation section comprises at least a separation device provided with a pipe for discharging the particles towards the stripping section, extending generally parallel or substantially parallel to the longitudinal axis
• said at least one grid can be located downstream of the discharge pipe of said at least one separation device. It may then include an orifice located under the discharge pipe of said at least one separation device in a direction parallel to the longitudinal axis.
• the grid may advantageously be located just below the ends of the evacuation pipe(s), so that the orifices are located as close as possible to the ends of these evacuation pipes, but nevertheless at a distance greater than the displacement of a valve attached to the end of the evacuation pipe.
• said at least one grid may be located upstream of one end of the particle evacuation pipe of at least one device for separating the stripping section. separation, even upstream of the ends of the evacuation pipes of all the separation devices of the separation section.
• the invention thus describes the use of one or more grids in an enclosure for separating and stripping an effluent containing particles, the grid or grids being as previously described and positioned as previously described.
• the grid or grids are able to (allow to) retain pieces of coke and/or coating coming from the upper part of the enclosure and prevent them from entering the stripping section, thus reducing the risks of disturbance of the stripping operation.
• Figure 1 shows a longitudinal section of a separation and stripping enclosure according to one embodiment.
• FIG. 2 represents a longitudinal section of a separation and stripping enclosure according to another embodiment.
• FIG. 3 represents a longitudinal section of a separation and stripping enclosure according to yet another embodiment.
• Figure 4 shows a perspective view of a grid according to one embodiment.
• FIG. 7 represents a perspective view of a grid according to another embodiment.
• the terms upper, lower, above, below refer to a vertical or substantially vertical direction, in the direction of gravity, corresponding to the longitudinal direction of the enclosure in its usual position of use.
• substantially horizontal, longitudinal or vertical is meant a direction/plane forming an angle of at most ⁇ 20°, or even at most 10° or at most 5° with a horizontal, longitudinal or vertical.
• substantially parallel, perpendicular or at a right angle is meant a direction/an angle deviating by at most ⁇ 20°, or even by at most 10° or by at most 5° from a direction parallel, perpendicular or from a right angle.
• FIGS. 1 to 3 show a chamber 10 for separation and stripping.
• This type of enclosure is used to treat an effluent containing particles, in particular from a catalytic cracking reaction in a fluidized bed.
• This enclosure 10 is for example part of a fluid catalytic cracking unit.
• the enclosure 10 has a side wall 11, here of generally cylindrical shape but whose lower part has a smaller diameter than the upper part.
• This side wall 11 delimits an internal volume 12 having a longitudinal axis X parallel to the plane of FIGS. 1 -3.
• an internal cross-section of the enclosure designates a section of the enclosure perpendicular to the longitudinal axis X.
• enclosure 10 comprises an inlet 100 for the effluent to be treated, an upper outlet 101 for the separated gaseous effluent and a lower outlet 102 for the solid particles.
• the inlet 100 opens inside the enclosure 10 radially (horizontally).
• this inlet 100 opens axially (vertically) inside the enclosure, a reactor 1 extending axially inside the enclosure 10.
• the enclosure 10 comprises within its internal volume, a separation section 13 and a stripping section 14 of the particles located downstream of the separation section with respect to the circulation of the particles inside the enclosure. .
• This circulation of particles typically takes place from top to bottom.
• the separation section 13 the solid particles are separated from the gaseous fluids contained in the effluent entering the enclosure 10.
• the separation section comprises at least one separation device, usually several.
• These separation devices which may or may not be directly connected to the outlet of the catalytic cracking reactor, are essentially ballistic or centrifugal type separators, which impart a rotational movement to the suspension, so that the particles separate from the gas by centrifugal effect.
• a separation section comprises two stages of separation devices of the cyclone type or even a primary separation device (for example of the QTS or RSS type described below) and one or two stages of separation devices of the cyclone type.
• the invention is however not limited to a particular type of separation device.
• a ballistic separation device 15 with a horizontal winding axis is placed substantially in the center of the enclosure and receives the effluent loaded with particles entering the enclosure 10 via the inlet 100
• a plurality of separation devices 16 of the cyclonic type (hereinafter called cyclones) are distributed around the longitudinal axis and receive at the inlet the gas flow leaving the separation device 15.
• the separation section thus comprises a separation device primary 15 and a cyclone stage 16.
• the separation device 15 is here of the QTS type (four turn separator - quarter turn separator) and has an inlet 150, a body 151, an outlet 152 extending parallel or substantially parallel to the longitudinal axis X above the body 151 for evacuating gaseous fluids lightly loaded with residual particles and a lower evacuation pipe 153 for evacuating particles and a little gaseous fluid towards the stripping section 14.
• This outlet 152 is connected to the input 161 of the separation devices 16 detailed below.
• the separation section 13 is equipped with a ballistic separation device 15' of the RSS type (Riser Separator System - separation device for a reactor, connected to the outlet end thereof) .
• This type of separation device 15' is positioned centrally, along the longitudinal axis.
• This device 15' also comprises an inlet 150', a body 151', an outlet 152' extending parallel or substantially parallel to the longitudinal axis X above the body 151' for the evacuation of gaseous fluids lightly charged with particles. residues to the cyclones 16 and a lower evacuation pipe 153' for the evacuation of the particles and a little gaseous fluid towards the stripping section 14.
• Separation section here also comprises a primary separation device 15' and a cyclone stage 16.
• Cyclones 16 are well-known devices and comprise an enclosure, generally essentially cylindrical-conical, designed to impose a rapid rotation on the gas and the particles which it contains introduced into the body, for example by causing the gas charged with solid particles to enter tangentially to the circumference of the enclosure, near the wall. Under the effect of centrifugal force, the solid particles caught in the vortex move towards the wall, lose their speed there by friction and fall into the lower part of the device, before exiting through the apex of the cone. The gas follows the wall up to the vicinity of the apex, and once rid of the particles, rises to the upper part to exit through an evacuation pipe, which partly protrudes inside the enclosure.
• a cyclone thus usually comprises: a separation enclosure 160, which generally comprises a cylindrical upper part and a conical lower part, a first inlet pipe 161 opening out inside this separation enclosure, located in the upper part of this ci, a second gas outlet pipe 162 located in the upper part of the separation enclosure, and a third particle evacuation pipe 163 located in the lower part of the separation enclosure, also called “dipleg", which is extends parallel or substantially parallel to the longitudinal axis X.
• the end of this discharge pipe is generally equipped with a valve regulating the flow of particles towards the stripping section 14 and maintaining a level of particles above of it.
• a stripping section 14 In the stripping section 14, the particles leaving the separation section 13 undergo stripping during which the hydrocarbons trapped in these particles are extracted by means of a gaseous stripping fluid, generally steam.
• a stripping section 14 usually comprises a main stripping fluid injection system 140 arranged in the lower part of the stripping section. Other stripping fluid injection systems can be provided upstream of the main injection system 140.
• a secondary injection system 141 is positioned at the inlet of the stripping section 14, to perform a pre - stripping of the particles before they enter the stripping section.
• the stripping section 14 is most often equipped with stripping elements which can extend in one or several stages upstream of the main injection system 140.
• stripping elements of the structured packing type occupy the zone 142 of the stripping section 14.
• the particles circulating from top to bottom enter the zone 142 by openings 143 defined by an entry face 144 thereof, this entry face extending transversely to the longitudinal axis X.
• These openings 143 are represented schematically in FIGS. 1 and 2 and correspond for example to the openings 143 d a stripping element located furthest upstream, namely at the entrance, in zone 142.
• the stripping section 14 generally corresponds to the part of the enclosure 10 of reduced section.
• a separation and stripping chamber 10 in particular of the type shown in FIGS. 1 to 3, there may be deposits of coke 1 at the upper level of the side wall 11, as shown schematically in FIG. Chunks of coke can break off, fall and reach the stripping section 14. Debris of refractory material covering the side wall can also fall in the same way.
• the invention provides for positioning, upstream of the stripping section 14 or of an area 142 of the stripping section provided with stripping extending through the internal cross section of the enclosure, at least one grid 20, 21, 22, 23 extending transversely to the longitudinal axis.
• the grid or grids thus have the function of retaining the debris falling inside the enclosure 10 in order to prevent them from entering the stripping section 14. They are therefore arranged rather in the separation section 13, preferably upstream of the end of a conduit for discharging one or more (or even all) of the separation devices present in the separation section.
• the grid(s) could be placed in the stripping section, upstream of the zone 142 containing stripping elements, for example between the secondary injection system 141 and this zone 142, or even distributed over the height of the enclosure upstream of zone 142 or of the stripping section.
• the shape and dimensions of the grid(s) will be chosen so that the projection of a single grid (grids 22 or 23 in FIGS. 2 and 3) or all the grids (grids 20 and 21 in FIG. 1) on a transverse plane perpendicular to the longitudinal axis covers 80 to 100% of the internal cross section of the enclosure. Note that grids can be partly superimpose along the longitudinal axis (in other words their projections can partially overlap), or not.
• the grid(s) are thus “bare” grids which do not support functional elements or functional particles on their surface.
• no bed of particles or no assembly of functional elements rests on these grids, only any pieces of coke or other debris initially attached to the side wall of the containment or to internal equipment of the enclosure are likely to be supported by the grille or grilles.
• FCC defined as the time between two scheduled maintenance shutdowns.
• a first grid 20 is placed at the level of the evacuation pipes 163 of the cyclones 16 and extends between them so central.
• This grid 20 does not extend radially beyond the evacuation pipes 163, in particular, in this example, its projection on a transverse plane perpendicular to the longitudinal axis X covers a central part of the enclosure 10 s' extending radially from the longitudinal axis towards the side wall 11 of the enclosure.
• This grid 20 is here a flat grid which extends in a plane perpendicular to the longitudinal axis X and which is fixed only to the evacuation pipes 163 of the cyclones 16.
• Another grid 21 is placed higher along the longitudinal axis X, above the entrance 100 of the enclosure.
• This grid 21 has the shape of a truncated cone widening from upstream to downstream with respect to the circulation of the particles, in particular, in the example, its projection on a transverse plane perpendicular to the longitudinal axis X covers an annular peripheral part of the enclosure 10 extending radially from the side wall 11 of the enclosure towards the longitudinal axis X, here over a distance allowing the passage of the parts 152, 160 of the separation devices 15 and 16 respectively, present at this location in the enclosure 10.
• This grid 21 is here fixed only to the side wall 11 .
• a single grid 22 is arranged around the separation device 15, under the evacuation pipes 163 of the cyclones 16.
• the grid 22 has the shape of a truncated cone widening from upstream to downstream with respect to the circulation of the particles, in particular, in the example, its projection on a transverse plane perpendicular to the longitudinal axis X covers an annular peripheral part of the enclosure 10 extending radially from the side wall 11 of the enclosure towards the longitudinal axis X, here over a distance allowing the passage of the part of the separation device 15 present at this location in the enclosure 10, namely the pipe of evacuation 153.
• This grid 22 is thus similar to the grid 21 of Figure 1, but is located lower in the enclosure 10, at the level of a conical part 103 of the side wall 11, located here in the lower the separation section 13.
• the grid 22 can here come to rest on the side wall 11 of the enclosure 10.
• a single grid 23 is arranged at the height of the separation device 15 ', this grid 23 being crossed by the evacuation pipes 163 of the cyclones 16 and by the body 151 'of the separation device 15 '.
• This grid 23 has the shape of a truncated cone widening from upstream to downstream with respect to the circulation of the particles.
• its projection on a transverse plane perpendicular to the longitudinal axis X covers an annular peripheral part of the enclosure 10 extending radially from the side wall 11 of the enclosure towards the longitudinal axis X , here over a distance allowing the passage of the part 150 of the separation device 15.
• the grid 23 has orifices for the passage of the evacuation pipes 163 and the body 151 '. This grid 23 is here fixed only to the side wall 11 .
• the upper grid 21 represented in FIG. 1 as well as the single grid 22, 23 in FIGS. 2 and 3 has the shape of a cone, here a truncated cone, widening from upstream to downstream with respect to the circulation of the particles. .
• This grid extends over 360° around the longitudinal axis.
• This type of grid is represented in FIGS. 4 to 6 and is formed of a plurality of intersecting walls 30, 31 defining meshes 32.
• walls 30 extend radially while the other walls 31 are walls rings centered on the longitudinal axis X.
• the invention is however not limited to a particular relative arrangement of these walls 30, 31 provided that they define meshes 32.
• Adjacent meshes 32 can then have portions of wall 30a, 31a of different height measured parallel to the longitudinal axis, as represented in FIG. 6. Higher wall portions can extend over the entire dimension of the wall of a mesh such as the portions 31a shown in FIG. 6, or over a part of this dimension, such as portions 30a in FIG. entry face 144 of zone 142 of stripping section 14.
• the dimensions of these meshes, measured in a plane perpendicular to the longitudinal axis will thus preferably be chosen smaller than the dimensions of an opening 143 of the stripping zone. stripping, measured in a plane perpendicular to the longitudinal axis.
• the grid shown in Figures 4 to 6 is fixed only to the side wall 11 of the enclosure. It has a central orifice 33 for the passage here of the separation device 15, 15'.
• This central orifice 33 has a rectangular shape corresponding to the shape of the cross section of the separation device 15, 15'.
• the central hole will be such that an expansion clearance between the grid and the separator 15 will be maintained in all circumstances to allow free differential thermal expansion between the grid and the separator during operation of the FCC unit.
• the grid also comprises a plurality of orifices 34 distributed around the longitudinal axis X. These orifices 34 are here circular and can be used either for the passage of the evacuation pipes of the cyclones 16, for example for the grid 23 of FIG. , or to facilitate the descent of the particles leaving these evacuation pipes 163, when the grid is located under these pipes, such as the grid 22 of FIG.
• the grid is formed of a plurality of portions 35, here forming sectors 35, assembled to each other by their radial sides. This assembly can be achieved by keys, bolts, by interlocking, or any other appropriate means or by a combination of these means.
• six sectors 35 are provided.
• the grille is further attached to the side wall 11 of the enclosure by a plurality of struts 36 extending from a radius of the grille to the side wall, on top of the grille.
• a strut 36 is provided at each radial junction between two sectors.
• the lower grid 20 represented in FIG. 1 is a flat grid which extends in a plane perpendicular to the axis of the enclosure. This type of grid is shown in Figure 7. This grid 20 differs from the other grid described with reference to Figures 4 to 6 only in that it is flat and does not extend all around the axis. The same references thus designate the same elements.
• the walls 30, 31 can intersect at right angles and define meshes 32 of rectangular or square shape. The dimensions of the meshes 32 can be chosen as described above.
• the walls 30, 31 extend parallel or substantially parallel to the longitudinal axis X. It is also possible to provide meshes having wall portions of different height to promote the maintenance of the debris on the surface of the grid.
• the grid 20 also has a central orifice 33 for the passage of the separation device 15 and in addition a lateral orifice 33 'located under the separation device 15. It is in fact not necessary (although possible) to provide a grid under the separation device 15 because the latter will deflect the fall of the debris on its periphery. Thus, the grid 20 does not extend over 360° around the longitudinal axis X, but rather over 300°.
• the grid 20 is also formed of a plurality of portions 35, here five in number, assembled together along edges extending radially.
• the grid 20 is fixed only to the evacuation pipes 163 of the cyclones 16, here by sleeves 38 surrounding these pipes and integral with them, supporting the grid directly or by struts 39, 40 some of which extend in the plane of the grid (struts 40) and the others are angled upwards from the grid towards a sleeve 38 (struts 39).
• the grid 20 is fixed by struts to four of the evacuation pipes 163, arranged symmetrically with respect to the longitudinal axis X.
• the shape and dimensions of the grid(s) will be adapted according to the equipment other than grids present inside the enclosure and in particular above the lowest grid, namely the proximal grid. of the stripping section 14 or of its zone 142.
• the shape and dimensions of the grid(s) will be chosen so that, seen from above along the longitudinal axis, the entire internal cross section of the enclosure (or at least 80%) is covered by the grille(s).
• the enclosure includes internal equipment other than the grid(s), typically one or more separation devices, or even a reactor, then the shape and dimensions of the grid(s) will be chosen so that, seen from above along the longitudinal axis, the entire internal cross-section of the enclosure (or at least 80%) is covered by the grid(s). grills and internal equipment(s).

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• Chemical & Material Sciences (AREA)
• Chemical Kinetics & Catalysis (AREA)
• Organic Chemistry (AREA)
• Engineering & Computer Science (AREA)
• Combustion & Propulsion (AREA)
• Oil, Petroleum & Natural Gas (AREA)
• General Chemical & Material Sciences (AREA)
• Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
• Centrifugal Separators (AREA)
• Separation Of Solids By Using Liquids Or Pneumatic Power (AREA)
• Devices And Processes Conducted In The Presence Of Fluids And Solid Particles (AREA)
• Cyclones (AREA)

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• 2020
  • 2020-12-23 FR FR2014103A patent/FR3117895B1/fr active Active
• 2021
  • 2021-12-21 CN CN202180087061.4A patent/CN116801969A/zh active Pending
  • 2021-12-21 JP JP2023536025A patent/JP2024501486A/ja active Pending
  • 2021-12-21 EP EP21852043.5A patent/EP4267701A1/de active Pending
  • 2021-12-21 US US18/269,210 patent/US20240226838A9/en active Pending
  • 2021-12-21 KR KR1020237025186A patent/KR20230132792A/ko active Pending
  • 2021-12-21 WO PCT/FR2021/052413 patent/WO2022136790A1/fr not_active Ceased

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