The present invention relates to an injection device, notably to a hydrocarbon charge injection device for a refining unit, particularly a fluid catalytic cracking (FCC) unit.
The liquid hydrocarbon charges processed in refining units are generally brought into contact with a solid catalyst which will encourage the chemical reaction or reactions used to process the charge. In order to improve this contact and maximise the efficiency of the reactions, these liquid hydrocarbon charges are atomized into fine droplets by injection devices. This atomization makes it possible to maximise the area for contact between liquid (liquid hydrocarbon charge) and solid (catalyst), encouraging the transfer of heat and therefore encouraging the vaporisation of these hydrocarbons which react in the gaseous phase. Although there is no real consensus regarding the optimum diameter for the droplets, the desire is generally to form droplets the diameter of which is of the same order of magnitude is the diameter of the particles of catalyst, namely under 200 microns, for example of the order of 50 to 80 microns.
In general, use is made of injection devices referred to as “diphasic”, which have a cylindrical hollow body and two inlet openings via which the liquid hydrocarbon charge and an atomizing gas, generally steam, are respectively injected into the said body. A contact chamber is formed inside the body, in which chamber the hydrocarbon charge and the atomizing gas are brought into contact in order to atomize the hydrocarbon charge. Once atomized, the hydrocarbon charge is ejected via an outlet opening that opens into the reactor. Each injection device is installed on a wall of the reactor so that one end of the injection device comprising the outlet opening is situated inside the reactor.
Impact-type injection devices are notably known, in which the charge is introduced radially and impinges on a target situated at the centre of the body, causing droplets to form. An atomizing gas circulating axially allows these droplets to be entrained, while being divided further, towards the outlet from the body. The phenomenon of target erosion may nevertheless be observed, notably when the charge that is to be injected contains particles, and this makes it necessary to reinforce the target, increasing the cost further.
In certain injection devices, additional atomizing gas may be injected into the body via a pipe surrounding the target: the atomizing gas then leaves at target level and impinges on the liquid introduced via the opening situated facing the target, encouraging atomization of the jet of liquid that it strikes head-on.
The mixing chamber of these injection devices with dual injection of atomizing gas is, nevertheless, complex and expensive to produce. It therefore has to be produced separately, and then secured to the hollow body of the injection device.
The invention seeks to at least partially alleviate the disadvantages mentioned hereinabove. Therefore, what is proposed is an injection device configured to atomize a liquid into droplets using a gas, comprising:
According to the invention, the body has an internal cross-section that varies continuously or is constant over its entire length and the internal wall of the body is provided, between the first and the second zone, with at least one chicane projecting from the internal wall towards the inside of the body.
In the usual way, a chicane is a device which impedes the passage of a moving fluid. The particular arrangement of the invention makes it possible to produce the body in a way that is very simple without detracting from the quality of atomization of the injection device.
The body has an internal cross-section that varies continuously, or in other words without any sudden variation and without any shoulder. The body may thus have a frustaconical or similar shape. For preference, the body has a constant internal cross-section. It may for example be a cylinder or the like.
The body may advantageously be made as a single piece. The end element may potentially be produced as one piece with the body.
In a first embodiment, the said at least one chicane may be configured so that, in each plane perpendicular to the longitudinal direction of the body containing the said chicane, the chicane extends over the entire periphery of the internal wall. The chicane or chicanes may thus be produced in a simple way. A chicane may then take the form of a simple ring. Advantageously, a single chicane may be provided. Such an arrangement may nevertheless give rise to a pressure drop, something which may prove problematical for processing heavy charges, which are increasingly used. Specifically, atomizing heavy charges involves a significant pressure drop at the injectors, this having the effect of increasing the pressure of the charge fed to the injectors. It is then necessary to use powerful and expensive pumps in order to achieve the desired injector-outlet pressures. It is therefore beneficial to limit the pressure drop brought about by the injection system. Depending on the configuration of the diphasic injection devices, it may also prove necessary to considerably increase the flow rate of atomizing gas in order to atomize heavy charges.
In order to overcome this disadvantage, in a second embodiment, the said at least one chicane may be configured so that, in each plane perpendicular to the longitudinal direction of the body containing the said chicane, the chicane extends over just part of the periphery of the internal wall.
Thus, in each plane perpendicular to the longitudinal direction of the body, each chicane reduces the through-area of the body on just part of its periphery so that the pressure drop is lower than the pressure drop that would arise if a chicane extended over the entire periphery of the internal wall.
What is meant by a through-area is the internal surface area of the body that is not occupied by an element and through which the fluid can circulate.
Advantageously, the said at least one chicane is configured in such a way that the orthogonal projection of the chicane onto a plane perpendicular to the longitudinal direction of the body extends over just part of the periphery of the internal wall in the said plane of projection. That makes it possible to reduce the pressure drop still further, despite the presence of (a) chicane(s). Note that when several chicanes are provided, their projections in one and the same orthogonal plane may overlap, or even extend over the entirety of the periphery of the internal wall.
As an alternative, or in combination, the said at least one chicane may be configured in such a way that the orthogonal projection of at least one chicane onto a plane perpendicular to the longitudinal direction of the body may extend over the entire periphery of the internal wall in the said plane of projection, possibly with overlap.
In the second embodiment, the said at least one chicane may define a wall one edge of which is secured to the internal wall along a segment of a curve, notably of a helicoidal curve.
As an alternative, whatever the embodiment, the said at least one chicane may define a wall one edge of which is secured to the internal wall along a line extending in a plane perpendicular to the longitudinal direction of the said body.
Whatever the embodiment, the said internal wall may be provided with a plurality of disjointed chicanes. That makes it easier for the fluids to mix without, however, increasing the pressure drop. In particular, these chicanes may be distributed, particularly uniformly, on the periphery of the internal wall for better mixing without an increase in the pressure drop.
The features hereinafter also make it possible to improve the mixing between the liquid and the gas without appreciably increasing the pressure drop.
Thus, when there are several chicanes present, each chicane may advantageously be spaced away from at least one other chicane in the longitudinal direction of the body.
In that case, the chicanes may then extend over a relatively short length of the body.
In the case of the second embodiment, when several spaced-apart chicanes are present, each chicane may also be angularly offset from the other chicanes by rotation about an axis parallel to or coincident with the said longitudinal direction. In particular, the orthogonal projection of the chicanes onto a plane perpendicular to the longitudinal direction of the body may extend over the entire periphery of the internal wall. In this plane of projection, there may be an overlap of the projections of the chicanes or, for preference, a juxtaposition thereof, the chicanes then being arranged in a staggered configuration.
Whatever the embodiment, the wall defined by each chicane may be a planar wall, which is simple to produce, or alternatively a curved wall.
Said at least one chicane may thus, on the side of the inlet openings, exhibit a curved face arranged so as to direct a fluid impinging on this face towards the inside of the body, which may make it possible to improve the mixing.
In particular, several chicanes having a curved face may be arranged relative to one another in such a way as to impart to the fluid impinging on the curved face thereof one and the same rotational movement about an axis parallel to the longitudinal direction of the body.
Whatever its shape (curved or planar), a chicane (or the tangent thereto at the point at which it meets the internal wall of the body) may define a predetermined angle with respect to a plane orthogonal to the longitudinal direction of the body. This angle may be variable for one and the same chicane.
Whatever the shape (curved or planar) of a chicane, its free edge (the edge opposite to its edge secured to the internal wall of the body) may have one or two faces of rounded or bevelled shape.
In general, the chicane or chicanes may have a height, measured perpendicular to the longitudinal direction of the body, that is non-zero. Advantageously, this height is equal to at most ½ the maximum internal dimension of the body perpendicular to the longitudinal direction of the body. For preference, this height is equal to at most ¼ of the maximum internal dimension of the body, or even ⅛th of this maximum dimension, for example of the order of 1/10th of this maximum dimension. This height may furthermore be variable for one and the same chicane.
In general, the chicane or chicanes may have a thickness, measured in the longitudinal direction of the body, that is non-zero. Advantageously, this thickness is at most 35 mm, preferably at most 31 mm, or even at most 20 mm or at most 16 mm. This thickness may for example be of the order of 10 mm.
The invention is now described with reference to the appended, non-limiting drawings, in which:
In the various figures, elements that are identical bear the same references.
The body 12 comprises an internal wall 13 which defines a first zone Z1 referred to as contact zone, and a second zone Z2 situated downstream of the first zone Z1 with respect to a direction in which the liquid and the gas circulate inside the body (in this instance from left to right in
The injection device 10 further comprises:
The end element 25 is thus situated downstream of the zones Z1, Z2.
The openings 15, 17, 19 of the body 12 open into the first zone Z1, also referred to as contact chamber.
Inside the body 12, the fluids circulate from the inlet openings 15, 17, 19 towards the outlet orifice 25.
The injection device 10 depicted in
Here, the first zone Z1 and the second zone Z2 take the form of a straight internal pipe connecting the first inlet opening 15 the outlet orifice 25 in an axial direction of the said body. This internal pipe in this embodiment has a constant internal diameter. The invention is not, however, limited by this embodiment. The internal cross-section of this pipe (in other words of the body) could vary continuously or be constant over the entire length of the pipe (i.e. of the body), without, however, being circular.
In the embodiment depicted, the body 12 is a cylinder, in other words the internal wall 13 here is cylindrical, its axis coinciding with the longitudinal direction X of the body.
The liquid emanating from the introducing element 16 is sprayed against the impact surface 22 of the target 21 as soon as it enters the first zone Z1. The jet of liquid is broken open and carried in the form of droplets by a stream of atomizing gas introduced at high speed by the gas introducing element 14. Atomization of the liquid takes place in two stages. A first part of the atomization occurs at the target 21 as the jet of liquid impinges on the impact surface 22 of the target 21. The jet of liquid thus broken open undergoes shearing by the gas entering via the pipe 20 and by the gas introduced by the first gas introducing element 14. The second part of the atomization occurs at the reduced-diameter outlet orifice 25, where the narrowing in diameter accelerates the fluids.
According to the invention, the internal wall 13 of the body is also provided, between the first zone Z1 and the second zone Z2, with at least one chicane 26i (where i, the number of chicanes, is a non-zero whole number). Because this chicane locally reduces the diameter of the internal wall 13, it disrupts the movement of the fluid, encouraging mixing. In particular, the presence of a chicane makes it possible to avoid the formation of a film of liquid on the wall by bringing the liquid back into the axis of the stream of gas.
One or more chicanes may be provided.
The injection device 10 may thus comprise a single chicane 261, depicted in
In this example, four disjointed chicanes 26′1, 26′2, 26′3, 26′4 are provided.
It will be noted here that each chicane 26′1, 26′2, 26′3, 26′4 is configured in such a way that the orthogonal projection of the chicane onto a plane perpendicular to the longitudinal direction of the body extends over just part of the periphery of the internal wall in the said plane of projection (see
Two chicanes 26′1, 26′2 here extend in one and the same plane perpendicular to the longitudinal direction X, the other two chicanes 26′3, 26′4 extending in another perpendicular plane, spaced away from the plane of the chicanes in the longitudinal direction X (see
The chicanes 26′1, 26′2, 26′3, 26′4 are furthermore offset angularly by rotation about the longitudinal direction X, as visible in
As an alternative, provision could be made for the orthogonal projection of these chicanes 26′i onto a plane perpendicular to the direction X not to extend over the entire periphery of the internal wall 13 but to extend over just part, as depicted in
In another alternative form that has not been depicted, provision could be made for the orthogonal projection of the chicanes onto a plane perpendicular to the direction X to extend over the entire periphery of the internal wall 13, with the projections of the chicanes overlapping.
Thus, the relative layout of the chicanes may be chosen in such a way as to cause as much disruption as possible to the movement of the fluid circulating inside the injection device, without increasing the drop in pressure.
In the example depicted in
The chicanes depicted in
In this embodiment, each chicane 26″1, 26″2 defines a wall, one edge of which is secured to the internal wall 13 along a line extending in a plane perpendicular to the longitudinal direction X. Although not depicted, other chicanes 26″i spaced apart in the X-direction and/or angularly offset from one another could be provided.
One or more chicanes 26′″i may be provided, these for example being angularly offset and/or spaced apart in the longitudinal direction X. furthermore, they may be arranged relative to one another in such a way as to impart to the fluid impinging on the curved face thereof one and the same rotational movement about an axis parallel to the longitudinal direction of the body.
The chicanes described hereinabove may be produced as one piece with the body 12, for example by moulding or machining, or may be added-on elements which are fixed, for example welded, held between flanges, or the like. When several chicanes are present, they may be identical or different, it being possible to combine the various shapes and arrangements of chicanes described hereinabove.
The chicane or chicanes are arranged between the first and second zones Z1, Z2. Typically, the second zone has a length (in the longitudinal direction X) 2 to 10 times greater than the length of the first zone. The chicane or chicanes, notably the first chicane, may be situated at a distance “1” from the axis of the target 20 or of the openings 17, 19 that is less than the diameter of the internal wall 13, at the level of the first zone, for example at a distance corresponding to ¾ of this diameter (for the sake of clarity, the figures are not drawn to scale).
The chicane or chicanes may have a radial dimension or height (perpendicular to the longitudinal direction X) that is relatively small, for example less than ⅛th of the diameter of the internal wall 13, or even of the order of 1/10th of this diameter. This height may be variable along the length of a chicane, as depicted in
The non-zero thickness of each chicane, measured in the longitudinal direction X of the body is, for example, at most 16 to 35 mm.
It will be noted that, whatever its shape (curved or planar), a chicane (or the tangent thereto at the point at which it meets the internal wall 13 of the body) may define a predetermined angle with respect to a plane orthogonal to the longitudinal direction of the body (see
The chicane or chicanes inclined in this way may be inclined in the direction of the outlet orifice 25.
Whatever its shape (curved or planar), the free edge of a chicane (the opposite edge to the edge secured to the internal wall of the body) may have a face 28a of rounded shape (
When just one face is provided, it is preferably situated on the side of the mixing zone Z1 in the longitudinal direction X.
The various embodiments described hereinabove may be combined and implemented with equal preference for one or more chicanes.
Number | Date | Country | Kind |
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1752497 | Mar 2017 | FR | national |
Filing Document | Filing Date | Country | Kind |
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PCT/EP2018/057341 | 3/22/2018 | WO | 00 |