Device for coating particles
Abstract
A fluidized bed apparatus for applying a coating liquid onto the surface of particles includes a vertically disposed cylindrical product container having a peripheral wall, at least one cylindrical partition defining a centrally located up bed region and a peripherally located down bed region. The product container further includes an upper end connected to an expansion chamber and a lower end including an orifice plate having a plurality of openings for passage of fluidized air or gas. A nozzle is centrally located through the orifice plate and is adapted to generate a spray of coating liquid upwardly into the up bed. Particles located within the product container circulate upwardly through the partition and the coating liquid spray, between the up bed and the down bed. A central discharge assembly is provided at the lower end of the product containers for emptying particles from the machine. Air is preferably discharged from the manifold during the emptying process to help direct particles towards the discharge assembly.
Term
Term ended
Projected expiry passed 20 November 2020, 5.8 years ago.
- Priority
- Filed
- Published
- Projected expiry
- Today
17 claims: 17 independent, 0 dependent
- 1Claims of equivalent WO 0137980 A2 Translation of claims of equivalent WO 0137980 A2 Device for coating particles with a container, which has a perforated distributor plate, can be supplied by the process gas flowing from bottom to top, with at least one riser arranged in the container at a distance from the distributor plate, which is open with its upper end to the container, and in the lower end of which a spray nozzle for spraying coating material is directed into the riser pipe, wherein a coating zone is formed within the riser and a return zone is formed outside the riser, and the particles are guided through the coating zone from the bottom up through the action of the process gas and the spray jet of the coating material and flow downwards in the return zone under the action of gravity and are returned to the coating zone via a gap, characterized , in that means for supporting gas supply (50) are provided in or on the container (12) in the vicinity of the perforated inflow base (14), initiating a backing gas stream having at least one laterally inwardly directed flow component in the direction of the gap to form a gas slip layer and transport the particles (27) between the return zone (37) and the coating zone (33) in a directional particle flow;and / or that means (22, 52 120) are arranged for structural molding in the lower region of the container (12), which form a transitional channel between the return zone (37) and the coating zone (33) with substantially continuous boundary surfaces, wherein the means for supporting gas supply and / or the means for constructive shaping lead the particles between the return zone and the coating zone in a directed particle flow. Patentansprüche Vorrichtung zum Beschichten von Partikeln mit einem Behälter, der einen gelochten Anströmboden aufweist, durch den von unten nach oben strömendes Prozeßgas zuführbar ist, mit mindestens einem mit Abstand zum Anströmboden in dem Behälter angeordneten Steigrohr, das mit seinem oberen Ende zum Behälter offen ist, und in dessen unteres Ende eine Sprühdüse zum Einsprühen von Beschichtungsmaterial in das Steigrohr gerichtet ist, wobei innerhalb des Steigrohres eine Be- schichtungszone und außerhalb des Steigrohres eine Rückführzone gebildet wird, und die Partikel unter Einwirkung des Prozeßgases und des Sprühstrahles des Beschichtungsmaterials von unten nach oben durch die Beschichtungszone ge- führt werden und in der Rückführzone unter Einwirkung der Schwerkraft von oben nach unten strömen und über einen Spalt in die Beschichtungszone zurückgeleitet werden, d a d u r c h g e k e n n z e i c h n e t , daß in oder an dem Behälter (12) in der Nähe des gelochten Anströmbodens (14) Mittel zur Stützgaszufuhr (50) vorgesehen sind, die einen Stützgasstrom mit mindestens einer seitlich von außen nach innen gerichteter Strömungskomponente in Richtung des Spaltes zur Bildung einer Gasgleitschicht und zum Transport der Partikel (27) zwischen der Rückführzone (37) und der Beschichtungszone (33) in einem gerichteten Partikelfluß einleiten, und/oder daß Mittel (22, 52, 120) zum konstruktiven Ausformen im unteren Bereich des Behälters (12) angeordnet sind, die einen Übergangskanal zwischen Rückführzone (37) und Beschichtungszone (33) mit im Wesentlichen stetigen Begrenzungsflächen bilden, wobei die Mittel zur Stützgaszufuhr und/oder die Mittel zum konstruktiven Ausformen die Partikel zwischen der Rückführzone und der Beschichtungszone in einen gerichteten Partikelfluß führen.
- 2Vorrichtung nach Anspruch 1, dadurch gekenn- zeichnet, daß die Mittel zur Stützgaszufuhr einen weiteren Stützgasstrom in den Übergangskanal einleiten, der um die Sprühdüse (18 ) herum vom Anströmboden (14) aus gesehen an Stellen mit unterschiedlicher Höhe zugeführt wird, wobei die Höhe der Stellen von außen nach innen zunimmt, derart, daß eine schräge oder bogenförmige Gasgleitschicht gebildet wird. Second Apparatus according to claim 1, characterized in that the means for supporting gas supply introduce a further support gas flow into the transition duct, which is supplied around the spray nozzle (18) from the distributor plate (14) at locations of different heights, the height of the Increase points from outside to inside, such that an oblique or arcuate gas sliding layer is formed.
- 3Vorrichtung nach Anspruch 2, dadurch gekennzeichnet, daß die Mittel zum konstruktiven Aus- formen einen rampenförmigen Körper (22) aufweisen, der auf dem Anströmboden (14) mittig angeordnet ist und der von außen nach innen ansteigt . Third Apparatus according to claim 2, characterized in that the constructional means comprise a ramp-shaped body (22) which is arranged centrally on the inflow base (14) and which rises from the outside to the inside .
- 4Vorrichtung nach Anspruch 3, dadurch gekenn- zeichnet, daß die rampenförmige Umfangsfläche (114) des Körpers (22,102) perforiert ist und das durch den Anströmboden (14) strömende Prozeßgas (15) als Stützgasstrom zur Bildung der schrägen oder bogenförmigen Gasgleitschicht an unterschiedlichen Stellen der rampenförmigen Umfangsfläche (114) austritt. 4th Apparatus according to claim 3, characterized in that the ramped peripheral surface (114) of the body (22, 102) is perforated and the process gas (15) flowing through the distributor plate (14) serves as a supporting gas stream to form the oblique or arcuate gas sliding layer at different locations ramp-shaped peripheral surface (114) emerges.
- 5Vorrichtung nach einem der Ansprüche 2 bis 4, dadurch gekennzeichnet, daß die Mittel zum kon- struktiven Ausformen einen an dem äußeren Umfang des unteren Endes des Steigrohres (24) vorgesehenen Ansatz (120) mit in Strömungsrichtung der Partikel geneigter Umfangsfläche zur Bildung ei- ner Ablenkfläche aufweisen. 5th Device according to one of claims 2 to 4, characterized in that the means for constructive molding provided on the outer circumference of the lower end of the riser (24) approach (120) with inclined in the flow direction of the particles peripheral surface to form a ner Have deflection.
- 6Vorrichtung nach Anspruch 5, dadurch gekennzeichnet, daß der Ansatz (120) in seinem dem Anströmboden (14) zugewandten Bereich eine im Wesentlichen horizontale oder in Richtung der Be- schichtungszone geneigte oder eine bogenförmige Leitfläche (126,127) aufweist, derart, daß die in der Rückführzone (37) nach unten strömenden und von der Ablenkfläche (122) nach außen abgelenkten Partikel durch die Leitfläche (126,127) in Richtung der Beschichtungszone (33) geleitet werden. 6th Apparatus according to claim 5, characterized in that the projection (120) has a substantially horizontal or in the direction of the coating zone inclined or an arcuate guide surface (126,127) in its the inflow base (14) facing region, such that in the Returning zone (37) downwardly flowing and deflected by the deflecting surface (122) outwardly directed particles through the guide surface (126,127) in the direction of the coating zone (33).
- 7Vorrichtung nach Anspruch 5 oder Anspruch 6, dadurch gekennzeichnet, daß der Ansatz konisch und eine Neigung zur Vertikalen zwischen 1° und 50°, vorzugsweise 10° bis 35° aufweist. 7th Apparatus according to claim 5 or claim 6, characterized in that the approach has conical and an inclination to the vertical between 1 ° and 50 °, preferably 10 ° to 35 °.
- 9Vorrichtung nach einem der Ansprüche 1 bis 8, dadurch gekennzeichnet, daß die Mittel zur Stützgaszufuhr den Stützgasstrom mit seitlich gerichteter Strömungskomponente über am unteren Ende des Behälters benachbart zum Anströmboden (14) angeordnete Einströmöffnungen (60) unter Druck einleiten. 9th Device according to one of claims 1 to 8, characterized in that the means for supporting gas supply the support gas flow with laterally directed flow component via at the lower end of the container adjacent to the distributor plate (14) arranged inlet openings (60) under pressure initiate.
- 10Vorrichtung nach einem der Ansprüche 1 bis 9, dadurch gekennzeichnet, daß die Mittel zur Stützgaszufuhr eine Gasquelle und einem mit der Gasquelle in Verbindung stehenden Gaskanal (62) aufweisen, der um den Umfang des Behälters (12) herum, benachbart zu dem Anströmboden (14) angeordnet ist und der mit den Einströmöffnungen (60) in Verbindung steht. 10th Device according to one of claims 1 to 9, characterized in that the means for supporting gas supply comprise a gas source and a gas channel (62) communicating with the gas source and arranged around the circumference of the container (12) adjacent to the inflow base (14 ) and which communicates with the inflow openings (60).
- 11Vorrichtung nach Anspruch 9 oder Anspruch 10, dadurch gekennzeichnet, daß die Einströmöffnungen (60) gleichmäßig um den Umfang des Behälters herum angeordnet sind oder als ringförmiger um- fänglicher Einströmschlitz ausgebildet sind. 11th Apparatus according to claim 9 or claim 10, characterized in that the inflow openings (60) are arranged uniformly around the circumference of the container or are formed as an annular circumferential inflow slot.
- 12Vorrichtung nach einem der Ansprüche 9 bis 11, dadurch gekennzeichnet, daß der Bereich der Wand des Behälters, in dem die Einströmöffnungen (60) angebracht sind, schräg oder bogenförmig ist. 12th Device according to one of claims 9 to 11, characterized in that the region of the wall of the container in which the inflow openings (60) are mounted is oblique or arcuate.
- 13Vorrichtung nach Anspruch 11 oder Anspruch 12, dadurch gekennzeichnet, daß der Gaskanal (62) aus einem Kanalring (66) und einem Bodenabdichtring (68) besteht, wobei die Einströmöffnungen (60) zwischen dem Kanalring und dem Bodenabdich- tring ausgebildet sind. 13th Apparatus according to claim 11 or claim 12, characterized in that the gas channel (62) consists of a channel ring (66) and a Bodenabdichtring (68), wherein the inflow openings (60) between the channel ring and the Bodenabdich- are formed.
- 14Vorrichtung nach einem der Ansprüche 1 bis 13, dadurch gekennzeichnet, daß der Anströmboden mit einem geteilten Anströmkanal für die Zufuhr von Prozeßgas verbunden ist, wobei ein erster Teil- anströmkanal (170) mit der Beschichtungszone (33) ausgerichtet ist und ein zweiter Teilanströmkanal (172) mit der Rückführzone (37) ausgerichtet ist, derart, daß das Prozeßgas des ersten Teilanströmkanals in die Beschichtungszone und das Prozeßgas des zweiten Teilanströmkanals in die Rückführzone geleitet wird. 14th Device according to one of claims 1 to 13, characterized, that the distributor plate is connected to a split inflow channel for the supply of process gas, wherein a first partial flow channel (170) is aligned with the coating zone (33) and a second partial flow channel (172) is aligned with the return zone (37), so that the process gas of the first Teilanströmkanals is passed into the coating zone and the process gas of the second Teilanströmkanals in the return zone.
- 15Vorrichtung nach Anspruch 14, dadurch gekennzeichnet, daß das in den zwei Teilanströmkanälen (170,172) geführte Prozeßgas jeweils unabhängig von einander einstellbar, überwachbar und regelbar ist. 15th Apparatus according to claim 14, characterized in that in the two Teilanströmkanälen (170,172) guided process gas is each independently adjustable, monitorable and controllable.
- 17Vorrichtung nach einem der Ansprüche 1 bis 14, dadurch gekennzeichnet, daß in dem Anströmboden (146) eine mit einem Austragkanal (144) verbun- dene Austragöffnung (150) zum Austragen der beschichteten Partikel vorgesehen ist, die mit einem zwischen einer geschlossenen und einer geöffneten Stellung bewegbaren Verschlußorgan (152) versehen ist. 17th Device according to one of Claims 1 to 14, characterized in that a discharge opening (150) connected to a discharge channel (144) for discharging the coated particles is provided in the distributor plate (146), one between a closed and an opened one Position movable closure member (152) is provided.
Independent claims17
58 paragraphs, as filed
Translation of description of equivalent WO 0137980 A2
Apparatus for coating particles
The invention relates to a device for coating particles according to the preamble of the main claim.
From European Patent EP 0570546 Bl such a fluidized bed reactor is known and it is used to coat particles or small lozenges that circulate in a container by means of a bottom-up air or gas (eg nitrogen), the particles are passed through a vertically upward jet of a liquid coating material. With the circulation of the particle through the beam, a small amount of coating material respectively deposited on the surface of the particles, wherein the number of revolutions of the particles determines the layer thickness. Such a coating apparatus according to the prior art functions satisfactorily, if the particles are fine and light. However, if the particles are larger, as for example, tablets or the like, it has been found that the coating becomes uneven because the heavier tablets do not circulate uniformly through the container. The coating apparatus according to the prior art can not be used for applications are to requiring a uniform, predictable layer thickness of all tablets in a batch. In addition, there is a risk that the tablets because of the high speeds in circulating abut obstacles and be damaged. Since the active ingredients are dosed accurately into the tablet, it is not acceptable that the tablets due to damage and abrasion loss of value of the active ingredient.
The invention is therefore based on the object to provide an apparatus for coating particles, the large particles with different geometric shapes, which may also have rough edges, are for example, tablets, coated in a gentle way and with an even layer thickness, the want to keep dimensional stability of the particles or tablets.
This object is achieved by the characterizing features of the main claim in conjunction with the features of the preamble.
Characterized in that means for the support gas supply are provided in the vicinity of the perforated inflow base, which in one NEN support gas stream with at least one laterally directed from outside to inside flow component Direction of the gap to form a gas overlay and / or that means for constructive forming the bottom of the container are located, which form a transition channel between the returning zone and the coating zone with substantially constant limiting surfaces, the particles, ie the tablets out in a directional particle flow, and there is a bouncing tablets at obstacles largely avoided, whereby the pockets bletten be transported in a gentle manner, so that no damage occurs. It can also particles with lower mechanical stability and such are coated with rough edges. Due to the means for constructive molding, ie by inserted into the lower region internals, a transition duct into the coating zone adjoins the recirculation zone of quasi wherein the boundary surfaces of this transition duct at least partially from the peripheral surfaces of the means of constructive molding together with the inflow and the boundary walls of the container, but can also be formed by the gas overlay, which is supplied from the supplied auxiliary gas stream.
Furthermore -both avoided by means of constructive molding as well as by the flow of gas delivered by the means for supporting gas supply so-called dead zones at which tablets could receive so that a uniform circulation of the tablet through the coating zone and thus on the tablets of batch uniform coating is ensured.
By measures indicated in the dependent claims, advantageous developments and improvements are possible. It is particularly advantageous that around the spray nozzle, a ramp-shaped body is arranged, which is perforated and on the one hand part of the means for constructive forming of the lower portion of the container to the transition duct and on the other hand is part of the means for the support gas supply. Through the perforation of the ramp-shaped body by the supplied air in this area, process a vertical supporting air is formed so that the tablets in the transition duct of the ramp-shaped circumferential surface are guided along as on an air cushion. There is prevented the direct impingement of the tablets on the shaft of the spray nozzle.
Preferably, the means direct to the supporting gas supplying the supporting gas flow with a laterally directed flow component at the lower end of the container adjacent to the inflow one, thereby forming a horizontal supporting air is formed (in the case of air as the gas), which prevents the tablets in inadequately from below at zero incidence areas lie of the inflow, and to simultaneously also ensure that the tablets are transported via the distributor plate as on an air overlay from the outside inward to coat zone. Additionally, it is advantageous that the region in which the inflow openings are mounted at the same time slightly inclined or cone-shaped or arc-shaped as a ring, whereby an adapted
Transition created by the inclination of the container wall towards the inflow to the drain, the tablet more easily and are thereby transported well from the outside inwards. The supply for the hori- zontal supporting air can take place by external air or conducted in the bypass part process air gen, where appropriate, a more flexible process control is given by the possibility of regulating the amount of air temperature and pressure in the first case, while in the second case, advantageously no additional monitoring of the resulting product quality through homogeneous purity of the main and sub-process stream, the common be produced and processed, is necessary.
In an advantageous manner is provided at the lower end of the
Riser an approach or an "apron" arranged, whose peripheral surface is inclined in the direction of flow of the tablet. In his the inflow region facing the approach the circumferential surface horizontally or in the direction of the coating zone is inclined or arcuate. Thus, the flow direction of the tablets is adapted in the recirculation zone so that they move easily and guided towards the coating zone and that there is not one nem backwater in the recirculation zone or on the outer edge of the inflow. This is also achieved by the cross-sectional constriction results in the recirculation zone to an increase in the gas velocity, which in turn over the upper region of the recirculation zone may lead to a partial relaxation of the recirculation zone, whereby the tablets can be oriented in the direction of flow better, and these are the more easily transported in particular through the gap between inflow and riser. In the arcuate configuration of the peripheral surface or at a drop-shaped cross-section results in terms of flow, a venturi effect similar to the coating zone.
It is also advantageous if the gas flowing through the inflow into the container process gas for coating Administrative Region and is supplied to the recirculation zone in separate Teilanströmkanälen since the respectively supplied process gas then set differently, can be monitored and regulated.
The fact that a discharge channel connected to a discharge opening is provided for discharging the coated tablets in the inflow, which is covered by a movable closure member, the tablets may be removed from the container in a simple and gentle manner.
Embodiments of the invention are shown in the drawing and are explained in the following description of letters. Show it:
Fig. 1 shows a section through an embodiment of the device according to the invention,
Fig. 2 is an enlarged view of a portion of the
Device according to Fig. 1,
Fig. 3 is a plan view of the device for supporting the gas supply,
Fig. 4 is a section through the device for supporting the gas supply,
Fig. 5 shows a section through the nozzle casing,
Fig. 6 is a view of a ramp body,
Fig. 7 is a plan view of the ramp body,
Fig. 8 is a section through a first embodiment of the neck, Fig. 9 shows a section through a second embodiment of the neck,
Fig. 10 is a view of a further embodiment of the coating apparatus according to the invention,
FIG. 11 is a sectional view of still another example of the coating apparatus of the invention,
Fig. 12 is a bottom view corresponding to FIG. 11,
Fig. 13 is a discharge device in a first position,
Fig. 14 is a discharge device in a second position.
In Fig. 1 is a section through an embodiment of the device for coating particles, for example, of tablets. The apparatus for coating 10 comprises a container 12 with conical peripheral walls 72, the bottom of which is formed by a serving as inflow 14 well plate. In the container 12 a substantially cylindrical support tube is centered 24 with -distance to the distributor plate 14, wherein a spray nozzle 18 which passes through a central opening 20 of the inflow 14 is directed into the interior of the support tube 24 and an implied spray 32 coating material is sprayed. The inflow 14 is gas-tightly connected to an inflow channel 16 for supplying process gas 15th Designed as a perforated plate distributor plate 14 has a plurality of holes 30 which are arranged such that the process gas 15, which may be for example air, nitrogen or the like can flow from the purchase flow channel 16 through the holes 30 into the product container 12 to produce a fluidized bed, as will be described later.
In the container to be coated particles or tablets 27 are arranged, extending through an opening formed in the interior of the support tube 24 and coating zone 33 move a formed between support tube 24 and wall 72 of the container 12 return zone 37th Preferably, the porosity of the designed as a perforated plate formed inflow base 14 respectively to the coating zone 33 and matched the return zone 37, ie, the number, arrangement and size of the holes 30 are chosen and arranged such that in the coating zone 33, a large volume of gas from the inflow channel 16 into the container, ie into the support tube 24 at relatively high speed, and in the region of the return zone 37, a sufficient flow of gas is supplied in order to keep the particles 27 in such a loosened or flowable state that the particles due to gravity move as individually against the process air in the direction of the inflow base down and can not agglomerate.
For coating the particles or tablets 27 are disposed in the container and it is supplied to filtered process air or process gas 15 via blower or compressed gas sources not shown, typically there is a negative pressure in the container 12 and in one ner subsequent expansion chamber, so that process air 15 drawn through the inflow becomes. This flowing both into the coating zone and the recirculation zone process air fluidizes the particles 27, and it is the sweeping through the central opening 20 spray nozzle 18 is activated to spray one NEN controlled spray 32 into the support tube 24th In this case, the coating material at high speed and under pressure, the amount of the type and size of the particles to be coated, is dependent on 27 the type of coating material and the desired coating properties, injected. In the coating zone 33, the particles 27 rise at a high speed, which is given by the process gas stream and through the spray, in the support tube 24 high, and they come with the Zerstäubungströpfchen the Beschichtungsflüssig- speed in contact and be coated before the end the support tube 24 are forced into the flash zone as indicated by arrow 35 radially outward. Once they come out of the influence of directed GE upward gas flow, the particles or tablets 27 to fall by gravity into the recirculation zone 37 downwards, they formed the basis of the differential pressure between the coating zone 33 and recirculation zone 37 in the bottom of the container "transition zone" be retracted into the coating zone 33rd In this manner, the particles or tablets 27 circulate several times through the coating zone 33 and the return zone 37, which is coated in the upward movement and dried and in the downward movement of the coating material is dried to an end.
In order to channel the flow of particles between the return zone 37 and the coating zone 33, means are provided for constructive forming of the lower portion of the container 12 and / or means for supplying support gas provided individually or jointly form a transition channel between recirculation zone 37 and coating zone 33 with substantially continuous boundary surfaces, the boundary surfaces can also be realized by gas overlays in no physical way. As shown in FIG. 1, consisting of the means to design molding and the means for supplying the supporting gas from a shoulder 120 and on the lower end of the support tube 24, from a nozzle ramp 22 and a gas supply means 50 which of the lower peripheral is the container 12 is provided. Further measures to line the ring-transition channel between recirculation zone 37 and coating zone 33 are feasible.
In the following, said means for molding and structural support for the supply of gas will be described in more detail. As seen from FIGS. 3 is to recognize and 4, the gas supply means 50 includes a ring-shaped gas channel 62 which is formed by a distributor plate 14 arranged on the sealing ring 68 and a downwardly open channel ring 66th Channel ring 66 and Bodenabdichtring 68 are overlapped by an outer ring 70 and the entire assembly is supported on the gas distributor plate 14 from and surrounds the lower part of the container 12 and is part of the boundary wall of the container 12. For this purpose, the outer ring 70 with a circumferential groove 58 provided on the inner circumference, the lower end of the sawn container wall 72 engages in this peripheral 58th As can be seen from Fig. 4 and Fig. 1, the inner leg 52 of the channel ring 66 is obliquely formed so that an extension of the container wall 72 is provided without jumps. The bottom at the lower end of the inner leg are openings 60 through the periphery, preferably one another at equal intervals are arranged, which are directed radially inwardly. A supply tube 64 communicates with the annular channel 62 in connection, so that under pressure 64 supplied gas or air supplied evenly flows radially through the supply pipe via the plurality of openings 60 to the inside, which is indicated in Fig. 3 by the arrows 65th The ring assembly shown in FIG. 4 can be taken apart in a simple manner, to permit cleaning.
In FIG. 2, the ring assembly of FIG. 3 and 4, shown in more detail in the installed condition, wherein it can be seen that a radially inwardly directed gas stream is blown 65 via the openings 60 into the container, whereby dead zones are avoided because all tablets 27, which are provided in the transition region between the container wall 72 and inflow 14, inward to the spray nozzle 18 toward and for coating zone 33 are forced out. In this case can the volume and velocity of the gas, which is injected via the openings 60, ER controlled according to the conditions of the tablets and the changes in the flow properties of the tablets due to the different phases of the coating. Due to the gas-inflow via the openings
60 a gas overlay is formed, which is horizontally inward and the lower tablets the recirculation zone 37 are indicated by the arrow 65 to move radially inwards to make room for other tablets to make 27 of the recirculation zone. Here, the horizontally inwardly directed air flow cooperates with the light passing through the openings 30 of the inflow process gas stream.
In FIG. 2, directed into the interior of the container surface of the leg 52 is formed obliquely. Even- of course it can also be arcuate in order to ensure a smooth transition to the inflow.
The openings 60 of the circumferential flow channel 62 are formed as round holes in Fig. 3 and 4, they may also be slot-shaped or it may also be a circumferential slot may be provided.
The gas supply through the supply pipe 64 is independent of the supply of process gas 15 through the inflow passage 16, whereby a good adjustability of the flow parameter is given in accordance with the process parameters. However, it is also possible to support the gas flow via the supply means 50 to branch off from the process gas.
In Fig. 1 to be recognized nozzle ramp 22 is closer shown in FIGS. 2, 5, 6, 7 is shown. The nozzle ramp 22 prevents the 33 from the return zone 37 inwardly sucked tablets 27 are represented by the existing horizontal component of movement, especially for heavy and large tablets abut against the nozzle and damaged due to the strong negative pressure in the area of the coating zone. Accordingly, FIGS. 5 to 7 is the nozzle ramp of a nozzle casing 90 and a perforated body 102. shown in Fig. 6 and 7 shown in FIG. 5, the nozzle casing 90 is hollow and includes an chen essentially cylindrical base portion 92 and a tapered upper portion 96. The spray nozzle 18 passes through the center of nozzle casing, wherein between nozzle 18 and nozzle casing remains a distance such that 14 flowing process gas is passed through the interior of the nozzle casing 90 through the openings 30 of the inflow. The upper end of Düsenman- means 90 may be so shaped that the emerging therefrom gas contributes to formation of the spray 32nd In another embodiment, the upper end be formed so that the nozzle 18 is sealingly received, so that no gas or only a small amount passes through the nozzle casing 90th
The perforated body 102 according to FIGS. 6 and 7, shows an arcuate peripheral surface 114 as a ramp surface, similar to a hat on, said the inflow base 14 facing surface has a larger diameter than the support tube 24 facing upper surface. Further, the hole body 102 is provided with a cylindrical through hole 108th
As shown in FIG. 1, the nozzles ramp 22 is arranged centrally on the distributor plate 14 wherein a steady transition area between inflow and peripheral surface 114 of the perforated body 102 is formed. The perforated body 102 surrounds the nozzle casing 90, which is received in the central through hole 108, such that the ramp-like peripheral surface 114 of the perforated body 102 continues substantially by the conical circumferential surface of the upper part 96 of the nozzle jacket 90th Of course, also an integral part consisting of perforated body and nozzle casing, be provided, it is conceivable that the lower part 92 of the nozzle jacket 90 is left path.
The perforated body 102 has a plurality of vertically arranged through-holes 116, which are preferably arranged as shown in FIG. 7 in concentric rings gene. The through holes 116 preferably have such dimensions that they can with the corresponding openings 30 of the form of a perforated plate inflow base 14 can be oriented so that the air flowing through the openings 30 from the inflow channel process gas 15 released by the geared ended through holes of the nozzle ramp 22 can flow through and at the upper end of each through hole 116 along the arcuate ramp surface 114 may emerge at different heights. The through holes 116 may be equal to or greater than its corresponding openings 30 of the onflow tray 14, whereby the process gas flow can be controlled in the through holes 116th
The purpose of the nozzle ramp 22 is to align the process gas from the inflow channel 16 along a curved arcuate ramp surface 114, so that the fast-moving, horizontally driven tablets to be 27 deflected by the air cushion formed or air overlay formed in the vertical direction. The use of the nozzle ramp 22 minimizes undesired triggering of the tablet 27 against an obstacle, since they are directed according to the arrow 118 in FIG. 2 in continuous movements in the coating zone back.
Optionally, the nozzles 22 be formed ramp that not through holes 116 are provided in a form of the body, but that the nozzle ramp as a whole is designed to be hollow, and only through-are-holes punched in its scope.
The in the recirculation zone 37 that are available tablets 27 move as a rate of one meter in 10 to 30 seconds down. When these tablets are 27 drawn into the coating zone, they are an example to approximately 5 to 10 meters per second speeds, this relatively sudden speed a large transition burden on the relatively low stability of tablets containing 27 exerts in the prior art. To reduce these stresses is shown in FIG. 1 on or at the lower end of the support tube 24, a neck 120, through which the loads exerted on the tablets by the sudden changes is reduced. In the FIG. 1 exemplary embodiment illustrated the approach 120 is designed as an annular cone 130 having an inclined at an angle A to the vertical peripheral surface 122. This is more particularly shown in Fig. 8. The cone 130 is provided with an inner cylindrical bore 124 to receive the lower end of the support tube 24 to which it is attached.
In the embodiment of FIG. 8, the approach 120 of two elements, the cone 130 and attached to the cone ring 130 is 128. The bottom, the distributor plate 14 facing surface 126 of the extension 120 and the ring 128 is preferably in accordance with angle B inclined inwards, in order to accelerate that are available in the vicinity tablets 27th Here, the outer edge 132 of the ring 128 is rounded. The angle B is selected depending on the size, shape and weight of the tablets 27 and the dimensions of the container and the coating properties and other sizes. The divided form of the approach different rings may be 128 provided with different inclinations of the surface 126 corresponding to different requirements. Of course, can also be formed as an integral part of the approach.
In Fig. 9 is another embodiment for one NEN approach 120 shown, in which the lower end of the support tube 24 is inserted. This approach has an approximately drop-shaped cross-section, ie, the tapered surface 122 extends in an arc towards the coating zone and the coating zone 33 facing inner surface of the through hole 124 is slightly inclined at an angle C. Characterized a venturi-like effect is achieved. The predetermined by the arc at the lower end of the teardrop-shaped approach angle (tangent to the peripheral surface) are chosen according to the operating variables and parameters. The A in FIGS. 8 and 9 designated angle may be between 1 ° and 50 °, preferably 10 ° to 35 °, while angle C is between 1 ° and 15 °.
The in the return zone 37, especially near the neck 120 that are available tablets 27 are obliquely deflected by the inclined surface 122, until they reach the arcuate 127 or lower surface 126 and are accelerated due to the pressure difference. The arcuate peripheral surface 127 as shown in FIG. 9 and the inclined surface 122 as shown in FIG. 8 contribute to a more uniform acceleration so that the loads are kept low on the tablets. The peripheral surfaces also form part of the continuous boundary surfaces of the transition duct 22 formed by the projection 120, the inclined container wall 72, optionally, an arc-shaped or the inclined inner wall of the leg 52 of the support gas supply device and the distributor plate 14 and the nozzle ramp. The is located under the approach 120 tablets 27 are easily lifted by the by the inflow 14 strömen- de process gas, since there is less downward force exerted on it than in the upper region reaching the recirculation zone 37. The result is that the tablets are easier and stress-poorer led by the return zone 37 through the transition duct into the coating zone 33rd
In Fig. 10, a further embodiment of the apparatus for coating tablets is shown which in contrast to FIG. 1 having a modified arrangement of the process gas supply. is know how to achieved, the inflow channel is divided into two sub-channels, a central channel 170 and an outer annular duct 172. The central channel 170 is used to supply the process gas in the coating zone 33, ie, it is mounted on the gas distributor plate 14 in the region of the nozzle senrampe 22 arranged. The central channel 170 is connected to a suitable gas source (pressure gas source or blower) and comprises a measuring device 174 for measuring the velocity, the pressure, the gas volume, the humidity and / or the temperature of the guided into the coating zone 33 the process gas. The measuring device is connected to the gas source, not shown, can be achieved so that a gas stream having suitable flow characteristics and maintained using known control devices.
Similarly, the outer ring channel 172, the process gas for controlling the fluidized bed properties of the recirculation zone 37 in the region is the same feeds, to a gas source (not shown), wherein also a measuring device 176 measures the parameters mentioned above. Regardless can be adjusted via a, likewise not shown, and control system of the gas stream supplied.
In FIGS. 11 and 12 is another embodiment example shown, three support tubes 24 are arranged in which to increase the efficiency in a container 12, a plurality in the embodiment. The support tubes are each within the container provided at the same distance, with a higher number of support tubes can be selected. In the coating apparatus 142 of Fig. 11 is by way of example, an embodiment of the support tube 24 is shown with a flared trumpet-shaped end 145, which can of course be used also in the previously described embodiments. Optionally, the widening may also earlier, ie in smaller height of the support tube 24, begin. The in Figs. 1 described elements to 10 are also provided in this coating device 142, but the clarity not executed due here.
In Fig. 11 and 12 an improved discharge device is provided which allows a gentle and contamination-free dispensing. In the prior art, the inflow channel 16 is usually folded down together with the distributor plate 14 and the total charge is poured into a container. Here again, the tablets may be damaged, and in addition, the effluent process gases are not always without problems. There is also the risk of contamination of the process environment and the operators due to dust, and abrasion of the product. Therefore, the invention is a closed discharge system provided accordingly.
The discharge device has a discharge channel 144 that extends from the center of the inflow base 146 to a remote location. The inflow 146 is similar to the above-described inflow bottom 14, comprises with the exception that it is designed for three nozzles 18, which are arranged at an angle of 120 ° to each other and, therefore, three large passage openings for the nozzles. The Anströmbo- the 146 includes a central discharge opening 150, in which the discharge channel 144 is taken up, as more specifically shown in Figs. is illustrated. 13 and 14 A tapered duct cover 152 is movable above the gas distributor plate 146 in alignment with the center discharge opening 150 disposed off. The tapered duct cover 152 is arranged with the tip up and moved between two positions, a sealed position as shown in FIG. 13 and an open position as shown in FIG. 14 generating device An actuation 154 is connected to the cover 152 and moves them between the two positions.
If the channel cover 152 is closed, remain- ben the tablets 27 in the container and can be coated in the manner described above, as indicated by the arrows 155th The conical cover 152 serves as a dividing element, which distributes the tablets 27 of the common return zone to the three supporting tubes 24th
If the coating process is completed, the actuator 154 is activated, whereby the cover 152 vertically rises upward and a gap 156 between the periphery of the discharge port 150 and the periphery of the cover 152 is formed. Thus, the tablets may be sucked into the discharge channel 144, as indicated by the arrows 158 in FIG. 14, if it continues processing device in the coating 142 to circulate between the coating zone and recirculation zone. The tablets are pre- preferably sucked by using a pressure difference between the container 12 and the discharge channel into the latter. In the embodiment, the discharge opening is disposed in the middle, of course, they may also be provided elsewhere, particularly in other arrangements of the coating apparatus.
The discharge channel 144 can also serve in cleaning the coating device for discharging larger remaining particles. For example, can be injected by the means for supplying supporting gas, ie set on the supporting gas supply device 50 into the container cleaning fluid under high pressure, which larger particles are forced into the center of the device and can be discharged via the discharge channel 144th
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| Document | Relation | Office | Cited during |
|---|---|---|---|
| US8187663B2 | Cited by | United States of America | Applicant |
18 members in 9 offices
Priority claims9
| Document | Office | Kind | Date |
|---|---|---|---|
| 166799P | United States of America | – | |
| 16679999 | United States of America | P | |
| 16679999 | United States of America | P | |
| 0011513 | European Patent Office (EPO) | W | |
| 0011513 | European Patent Office (EPO) | W | |
| 166799P | – | – | – |
| EP0011513 | – | – | – |
| US19990166799P | – | – | – |
| WO2000EP11513 | – | – | – |
Members18
| Document | Office | Kind | |
|---|---|---|---|
| WO0137980A2 | World Intellectual Property Organization (WIPO) | A2 | |
| WO0137980A3 | World Intellectual Property Organization (WIPO) | A3 | |
| EP1232003A2This record | European Patent Office (EPO) | A2 | |
| US6579365B1 | United States of America | B1 | |
| JP2003525726A | Japan | A | |
| US2003196598A1 | United States of America | A1 | |
| US2003200919A1 | United States of America | A1 | |
| US2003200920A1 | United States of America | A1 | |
| US6692571B2 | United States of America | B2 | |
| US6695919B2 | United States of America | B2 | |
| EP1232003B1 | European Patent Office (EPO) | B1 | |
| AT276823T | Austria | T | |
| ATE276823T1 | Austria | T1 | |
| DE50007932D1 | Germany | D1 | |
| DK1232003T3 | Denmark | T3 | |
| PT1232003E | Portugal | E | |
| ES2228651T3 | Spain | T3 | |
| US6911087B2 | United States of America | B2 |
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Numbers
- Publication
- 1232003
- Publication, DOCDB
- 1232003
- Publication, EPODOC
- EP1232003
- Application
- 988727
- Application, DOCDB
- 00988727
- Application, EPODOC
- EP20000988727
Titles3
- German
- VORRICHTUNG ZUM BESCHICHTEN VON PARTIKELN
- English
- DEVICE FOR COATING PARTICLES
- French
- DISPOSITIF DE REVETEMENT DE PARTICULES
Classification
- CPC, 6
- B01J8/386
- B01J2/006
- B01J2/16
- B01J8/44
- B01J2219/1946
- Y10S118/05
- IPC, 4
- B01J2 00
- B01J2 16
- B01J8 38
- B01J8 44
Designated states26
- Contracting states, 20
- Austria
- Belgium
- Switzerland
- Cyprus
- Germany
- Denmark
- Spain
- Finland
- France
- United Kingdom
- Greece
- Ireland
- Italy
- Liechtenstein
- Luxembourg
- Monaco
- Netherlands (Kingdom of the)
- Portugal
- Sweden
- Türkiye
- Extension states, 6
- Albania
- Lithuania
- Latvia
- North Macedonia
- Romania
- Slovenia