Self-Cleaning Nozzle
20220203396 · 2022-06-30
Inventors
Cpc classification
B05B1/086
PERFORMING OPERATIONS; TRANSPORTING
B01J2/006
PERFORMING OPERATIONS; TRANSPORTING
B05B15/52
PERFORMING OPERATIONS; TRANSPORTING
B05B3/16
PERFORMING OPERATIONS; TRANSPORTING
B05B7/1281
PERFORMING OPERATIONS; TRANSPORTING
B05B7/066
PERFORMING OPERATIONS; TRANSPORTING
B05B1/323
PERFORMING OPERATIONS; TRANSPORTING
B05B7/1245
PERFORMING OPERATIONS; TRANSPORTING
B01J2/02
PERFORMING OPERATIONS; TRANSPORTING
B05B15/50
PERFORMING OPERATIONS; TRANSPORTING
International classification
B05B15/50
PERFORMING OPERATIONS; TRANSPORTING
B05B15/52
PERFORMING OPERATIONS; TRANSPORTING
B05B3/16
PERFORMING OPERATIONS; TRANSPORTING
B05B7/06
PERFORMING OPERATIONS; TRANSPORTING
Abstract
A nozzle for spraying materials, in particular dispersions, emulsions or suspensions, comprising a nozzle body having a nozzle mouthpiece.
Claims
1. A nozzle for spraying substances, comprising: a nozzle body which has a nozzle mouthpiece, wherein the nozzle body comprises an inner pipe, said inner pipe being connected to a feed for the material to be sprayed and comprising an inner wall and an exit opening, and an outer pipe, said outer pipe being distanced to the inner pipe, being connected to a feed for a gas and comprising an exit opening, wherein the exit opening of the inner pipe and the exit opening of the outer pipe are arranged in a region of the nozzle mouthpiece, wherein the inner pipe at least partly is designed of an elastic material, and wherein an inlay is arranged on the inner pipe, said inlay being able to be brought or being brought into oscillation by way of the substance to be sprayed which exits out of the exit opening of the inner pipe, in order to minimise or prevent deposits in the exit region of the substance to be sprayed and/or of the gas, wherein the inner pipe and the inlay are designed as a single-piece conduit.
2. The nozzle according to claim 1, wherein the inner pipe which is designed as a single-piece conduit at least partly comprises a reinforced wall.
3. The nozzle according to claim 1, wherein an additional inlay is arranged on the inner wall or on an outer wall or in a wall of the outer pipe and projects at least partly into an exit region of the substance to be sprayed and/or of the gas.
4. The nozzle according to claim 1, wherein the outer pipe and the inner pipe are arranged coaxially about an axis X-X.
5. The nozzle according to claim 1, wherein the outer pipe and the inner pipe are arranged to one another in a manner such that the exit opening of the outer pipe is arranged concentrically to the exit opening of the inner pipe.
6. The nozzle according to claim 3, wherein the additional inlay can be arranged or is arranged in an exchangeable manner.
7. The nozzle according to claim 1, wherein a part-section of the additional inlay is changeable in length.
8. The nozzle according to claim 3, wherein the additional inlay is manufactured from at least one elastic material.
9. The nozzle according to claim 1, wherein the additional inlay and/or the single piece conduit is manufactured from at least one polymer.
10. The nozzle according to claim 9, wherein the at least one polymer is a synthetic polymer.
11. The nozzle according to claim 1, wherein an attachment part in the form of swirl bodies, swirl plates or the like for leading the gas is arranged in the region of the nozzle mouthpiece between the outer pipe and the inner pipe.
12. The nozzle according to claim 11, wherein the attachment part is arranged for guiding the inner pipe.
13. The nozzle according to claim 11, wherein the attachment part is fixedly connected to the inner pipe and/or to the outer pipe.
14. The nozzle according to claim 1, wherein an additional inlay and/or the single-piece conduit has a variable wall thickness.
15. The nozzle according to claim 1, wherein the oscillation is a high-frequency oscillation.
16. The nozzle according to claim 10, wherein the synthetic polymer is a silicone.
Description
BRIEF DESCRIPTION OF DRAWINGS
[0022] The invention is hereinafter explained in more detail by way of the accompanying drawings. They are shown in
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DETAILED DESCRIPTION
[0039] A nozzle 1 which is known from the state of the art is represented in
[0040] The inner pipe 2 comprises a fluid channel 5 which is designed for feeding the substance to be sprayed, preferably a liquid, very particularly preferably a dispersion, suspension, or emulsion. This fluid channel runs out in the region of the nozzle mouthpiece 6 into an exit opening 7 of the inner pipe 2. In the region which is away from the exit opening 7 of the inner pipe 2, the inner pipe 2 comprises a connection location 10 for a feed conduit for the substance to be sprayed, said feed conduit not being represented.
[0041] The outer pipe 3 is arranged distanced to the inner pipe 2, by which means an annular gap 8 for feeding the gas, in particular atomisation air forms. The annular gap 8 runs out into an exit opening 9 of the outer pipe 3 in the region of the nozzle mouthpiece 6. In the region which is away from the exit opening 9 of the outer pipe 3, the outer pipe 3 comprises a connection location 11 for a feed conduit for the gas, said feed conduit not represented.
[0042]
[0043] The inner pipe 102 comprises a fluid channel 105 for feeding the substance to be sprayed, preferably a liquid, very particularly preferably a dispersion, suspension, or emulsion. This runs out into an exit opening 107 of the inner pipe 102 in the region of the nozzle mouthpiece 106. In the region which is away from the exit opening 107 of the inner pipe 102, the inner pipe 102 comprises a connection location 110 for a feed conduit for the substance to be sprayed, said feed conduit not being represented.
[0044] The outer pipe 103 is arranged in a manner distanced to the inner pipe 102, by which means an annular gap 108 for feeding the gas, in particular atomisation gas forms. The annular gap 108 runs out into an exit opening 109 of the outer pipe 103 in the region of the nozzle mouthpiece 106. Preferably, the exit opening 107 of the inner pipe 102 and the exit opening 109 of the outer pipe 103 are arranged concentrically to one another. By way of this, it is ensured that the flow conditions of the gas which is delivered in the annular gap 108 are formed in an optimal, in particular uniform manner, so that the symmetry and droplet size of the spray which is produced by way of the preferred nozzle 101 are matched precisely to the demands of the manufacturing and/or spraying process, in particular manufacturing process and/or spraying process for granulates, tablets or the like. A connection location 111 for a feed conduit for the gas, said feed conduit not being shown, is given in the region which is away from the exit opening 109 of the outer pipe 103. Preferably, the exit openings 107, 109 lie in a plane C-C and run out into the exit region 112 of the nozzle 101. In the exit region 112, the spray which coats the particles is produced by the colliding of the substance to be sprayed and the atomisation gas. Advantageously, the symmetry as well as the droplet size of the spray is set in an optimal manner during the manufacturing process and/or spraying process.
[0045] The inner pipe 102 comprises an inlay 113. The inlay 113 in
[0046] The inlay 113 in the first embodiment of the preferred nozzle 101 comprises four part-sections 115 to 118. The part-section 115 secures the inlay 113 in the nozzle 101, so that the inlay 113 is arranged in the preferred nozzle 101 during the complete manufacturing and/or spraying process. Advantageously, the inlay 113 is connected to the inner pipe 102 such that this is fixed there. The part-sections 116 and 117 in the preferred nozzle 101 are arranged between the part-section 115 and the part-section 118 and bear on the inner wall 114 of the inner pipe 102. The part-section 118 of the inlay 113 projects at least partly out of the exit opening 107 of the inner pipe 102. By way of the possibility of the adjustment of the holding point of the part-sections 115 on the inner pie 102, the length of the part-section 118 of the inlay 113 which projects out of the exit opening 107 of the inner pipe 102 can be changed.
[0047]
[0048] The part-section 117 of the inlay 113 bears on the inner wall 114 of the inner pipe 102 of the preferred nozzle 101 and is connected to the part-section 118 of the inlay 113. The part-section 118 of the inlay 113 projects at least partly out of the exit opening 107 of the inner pipe 102 of the preferred nozzle. 101. The part-section 118 of the inlay 113 is preferably changeable in length. The length changeability is represented by the dotted line which is adjacent to the part-section 118. The length change can either be effected in a direct manner by way of exchanging the inlay 113, by way of adjusting the holding point of the inlay 113 on the inner pipe 102 and/or any other change of the arrangement of the inlay 113 in the nozzle 101.
[0049] An inner pressure 119 acts upon the inlay 113 by way of the substance to be sprayed, preferably a liquid, particularly preferably a dispersion, suspension, or emulsion, which is conveyed in the fluid channel 105 in the direction of the exit opening 107 through the inner pipe 102 which comprises an inlay 113. The inlay 113 is pressed against the inner wall 114 of the inner pipe 102 by way of the inner pressure 119 which acts upon the inlay 113. In the region of the nozzle mouthpiece 106, in particular in the region of the exit opening 107 of the inner pipe 102, a force which moves the inlay 113 away from the axis X-X likewise acts upon the part-section 118 of the inlay 113 by way of the inner pressure 119 which acts upon the inlay 113.
[0050] Furthermore, a force 120 which acts in the direction of the axis X-X acts upon the part-section 118 of the inlay 113 which projects at least partly out of the exit opening 107 of the inner pipe 102. The force 120 which acts in the direction of the axis X-X is created by the gas, in particular atomisation air, which exits from the exit opening 109 out of the annular gap 108.
[0051] By way of this, the inlay 113 which projects at least partly out of the exit opening 107 of the inner pipe 102 is moved, advantageously in a high-frequency manner, by the liquid which exits out of the preferred nozzle 101 into the exit region 112 of the nozzle 101 and/or by the gas, in particular atomisation gas which exits out of the preferred nozzle 101 into the exit region 112 of the nozzle 101. Due to this advantageously high-frequency movement of the inlay 113 which projects at least partly out of the exit opening 107 of the inner pipe 102, deposits of the liquid to be atomised, on the nozzle mouthpiece 106, in particular in the exit region 112, or their agglomeration, is prevented. The symmetry and droplet size of the spray is therefore not influenced during the manufacturing and/or spraying process, so that an undesirable spray drying and/or a local over-humidification and agglomeration does not occur.
[0052] The vibration frequency of the part section 118 of the inlay 113 can be additionally changed for example by way of the length changeability of the part-section 118 of the inlay 113. By way of this, one can have a direct influence upon the manufacturing and spraying process. A further change of the vibration frequency is possible for example by way of adapting the pressures of the substance or gas which is to be sprayed. A change of the onflow angle α of the gas, in particular of the atomisation air also effects a change of the vibration frequency of the inlay 113 and therefore has an influence upon the spray and its quality, in particular with regard to the symmetry and the particle size. The arrangement of the outer pipe 103 and the inner pipe 102 to one another is to be adapted, in particular in the region of the nozzle mouthpiece 106, for changing the onflow angle α of the gas. Furthermore, the onflow of the inlay 113 can also be adapted by way of a changed flow guidance in the annular gap 108. Very preferably, it is only the annular gap 108 which is adapted, so that this has a different onflow angle with respect to the part-section 118 of the inlay 113.
[0053] A section through a second embodiment of a preferred nozzle 201 with an optional attachment part 220 in the annular gap 208 in the form of a swirl plate for the guidance of the gas is represented in
[0054] The preferred nozzle 201 according to the second embodiment in its basic construction corresponds to the first embodiment of the preferred nozzle 101 which is shown in
[0055] The attachment part 221 can likewise be designed in the form of swirl bodies, e.g., flow guide plates or the like, for leading the gas. The attachment part 222 is preferably fixedly connected to the inner pipe 202 and to the outer pipe 203. By way of this, the stability of the nozzle 201 in the region of the nozzle mouthpiece 206 is increased. Furthermore, due to the installation of an attachment part 221 in the form of swirl bodies, swirl plates or the like, the leading of the flow of the gas, in particular of the atomisation air, at the nozzle mouthpiece 206, in particular in the exit region 212 of the nozzle 201 is influenced, by which means the movement behaviour of the inlay 213 which projects at least partly out of the inner pipe 202, in particular the vibration frequency of the part-section of the inlay 213, can be changed. The vibration frequency is therefore adjustable to the manufacturing and/or spraying process to an improved extent. Additionally, by way of this, the spray symmetry, and the droplet size of the spray, i.e., of the substance to be atomised, preferably of a liquid, very particularly preferably of a dispersion, emulsion or suspension can be adjusted in a direct manner. Furthermore, on installing, the inner pipe 202 is led in outer pipe 203 and always held in the desired position, in
[0056] Preferably, the inlay 213 which projects at least partly out of the exit opening 207 of the inner pipe 202 has a variable wall thickness. The wall thickness of the inlay 213, in particular of the part-section 218 which projects out of the inner pipe 202 can be adapted to the substance to be sprayed, preferably a liquid, particularly preferably a dispersion, emulsion or suspension, by which means the spray behaviour, preferably the spray symmetry and the setting of the droplet size, of the preferred nozzle 201 can be optimised. The inlay 213 can hence also be adapted to abrasive substances which are to be sprayed. By way of the change of the wall thickness given an equal length of the inlay 213 which projects at least partly out of the inner pipe 202 or by way of adapting the length of the inlay 213 given an equal wall thickness of the inlay 213, the oscillation behaviour of the part-section 218 which projects at least partly out of the exit opening 207 is changed, by which means the applied inlay 213 is specially adapted to the respective process with regard to method technology. The inlay 213 is advantageously connected to the inner pipe 202, so that this is fixed there.
[0057]
[0058] The preferred nozzle 301 comprises a nozzle body 304 which has an inner pipe 302 and an outer pipe 303, wherein the inner pipe 302 and the outer pipe 303 are arranged coaxially to an axis X-X.
[0059] The inner pipe 302 comprises a fluid channel 305 which is designed for feeding the substance to be sprayed. This channel opens out into an exit opening 307 of the inner pipe 302 in the region of the nozzle mouthpiece 306. In the region which is away from the exit opening 307 of the inner pipe 302, the inner pipe 302 comprises a coupling location 310 which for a feed conduit for the substance to be sprayed, preferably a liquid, very particularly preferably a dispersion, emulsion, or suspension, said feed conduit not being shown.
[0060] The outer pipe 303 is arranged in a manner distanced to the inner pipe 302, by which means an annular gap 308 for feeding the gas, in particular atomisation air, forms. The annular gap 308 runs out into an exit opening 309 of the outer pipe 303 in the region of the nozzle mouthpiece 306. In the region which is away from the exit opening 309 of the outer pipe 303, the outer pipe 303 comprises a coupling location 311 for a feed conduit for the gas, said feed conduit not being shown.
[0061] An attachment part 321 which comprises an opening 322 is arranged between the inner pipe 302 and the outer pipe 303. The attachment part 321 connects the inner pipe 302 and outer pipe 303 to one another, preferably in a fixed manner. By way of the attachment part 321, a swirl is imparted upon the gas, in particular the atomisation air, which flows through the annular gap 308. The frequency of the inlay 313 which projects at least partly out of the exit opening 309 of the out pipe 303 is influenced by way of the swirling. The inlay 313 is arranged on the outer wall 323 in the annular gap 308 and bears on the outer wall 33.
[0062] The inlay 313 which projects at least partly out of the exit opening 309 of the outer pipe 303 into the exit region 312 comprises four part-sections 315, 316, 317 and 318. Part-section 315 is fixed, for example clamped in a groove 324 which is arranged on the outer wall 323. The part-sections 316 and 317 connect the part-sections 315 and 318. The length of the inlay 313 is changeable, in particular the length of the part section 318 of the inlay 313 is adaptable to the parameters of the manufacturing and/or spraying process. Furthermore, the wall thickness of the inlay 313 which projects at least partly out of the exit opening 309 of the outer pipe 303 into the exit region 312, in particular the wall thickness of the part section 318 of the inlay 313 is adaptable to the process parameters with regard to method technology. In
[0063] The inlay 313 which projects at least partly out of the exit opening 309 of the outer pipe 303 into the exit region 312 is moved in particular at a high frequency by way of the substance, in particular a liquid, which is to be sprayed and which exits out of the preferred nozzle 301, and/or by way of the gas, in particular the atomisation gas, which exits out of the preferred nozzle 301. By way of the in particular high-frequency movement or oscillation of the inlay 313 which projects at least partly out of the exit opening 309 of the outer pipe 303 into the exit region 312, vibrations at a certain frequency arise at the inlay 313, by which means caking or adhesion of the substance to be sprayed, preferably a liquid, very particularly preferably a dispersion, emulsion or suspension, which leads to deposits on the nozzle mouthpiece 306, is prevented. Due to the prevention of deposits on the nozzle mouthpiece 306 in the exit region 312 and/or due to the prevention of agglomeration of the substance to be sprayed, the symmetry and droplet size of the spray are not influenced during the manufacturing and/or spraying process, so that an undesirable spray-drying and/or a local over-humidification and agglomeration does not occur.
[0064]
[0065] Hereby, a section through a fourth embodiment of a preferred nozzle 401 is shown in
[0066] A section through the fifth embodiment of a preferred nozzle 510 is shown in
[0067] A section through a sixth embodiment of a preferred nozzle 601 is represented in
[0068]
[0069] All embodiments 101 to 701 can comprise an optional attachment part 101 to 701 for leading the flow in the annular gap 108 to 708. Furthermore, there is the possibility of the arrangement of an inlay 113 to 713 on the inner pipe 102 to 702 and of an additional inlay 113 to 713 on the outer pipe 103 to 703, so that the preferred nozzles 101 to 701 comprise two inlay 113 to 713.
[0070]
[0071] A section through a preferred nozzle 901 is shown in
[0072] According to
[0073]
[0074]
[0075] The device 1033, in particular the pressurised air ring, which is changeable in its volume comprises at least one inlet for a fluid feed and at least one outlet for a fluid discharge, said inlet and outlet not being represented here. By way of this, the volume of the device 1033 can be changed, specifically can be enlarged, or reduced in size by way of the feed or discharge of fluid, by which means the device 1033 can be brought or is brought from an open position which is shown by way of example in
[0076] It should always be noted that the substance to be sprayed, in particular the liquid should not exit from the nozzle 1001 in a non-atomised state. For this, it is to be ensured that at the beginning of each spraying procedure, it is firstly gas, in particular atomisation gas which flows through the annular gap 1008 and thus out of the nozzle 1001 and subsequently the substance to be sprayed, in particular the liquid. On completing the spraying procedure, firstly the feed of the substance to be sprayed is to be stropped or interrupted and subsequently that of the gas. By way of this, it is ensured at all times than given a spraying procedure, the substance to be sprayed is atomised and that no substance to be sprayed drips out of the nozzle, possibly onto (coated) material to be treated, in a non-atomised state at the end of each spraying procedure. On starting or ending a spraying procedure, this can be ensured for example by way of an automatic “leading” and “trailing” of the gas.
[0077] All positions, in which fluid can flow through the annular gap 1008 and/or the fluid channel 1005 are denoted as an open position. By way of this, it is possible to provide an infinite adjustment of the volume flow with a through-flow of 0% and 100% for the gas and for the substance to be sprayed, wherein the adjustment of the volume flows is dependent on one another given only one device 1033. With the application of several, in particular two devices 1033, specifically each for the substance which is to be spayed which is conveyed in the fluid channel 1005 and the gas which is conveyed in the annular gap 1008, the volume flows of the substance to be sprayed in the fluid channel 1005 of the inner pipe 1002 and of the gas in the annular gap 1008 can be adjustable independently of one another and can be adjusted independently of one another, specifically by way of volumes of the applied devices 1033 which can be changed independently of one another by way of fluid feed or fluid discharge. By way of the independent adjustability of the volumes of different devices 1033, an optimal adaption of the volume flow of the substance to be sprayed to the atomisation gas and vice versa is likewise possible. By way of this, one can also react to the smallest changes of symmetry or particle size in the spray. The devices 1033 for the substance to be sprayed and for the gas are closed-loop controlled and/or controlled independently of one another by way of control devices and/or closed-loop control devices which are not shown here. The device 1033 is preferably arranged concentrically around the conduit 1032 and is enclosed by the outer pipe 1003, wherein a part-section 1018 projects at least partly out of the exit opening 1009 of the outer pipe 1003 into the exit region 1012. In
[0078] The device 1033 is preferably connected to a closed-loop control or control device which is not shown here and which closed-loop controls or controls the fluid feed or fluid discharge to and from the device 1033, so that the volume of the device 1033 can be set or is set. Very particularly preferably, the volume of the device 1033 is infinitely changed or infinitely changeable by way of the fluid feed or the fluid discharge or the volumes of the devices 1033 are infinitely changeable or changed by way of the fluid feed or fluid discharge. By way of the infinite adjustability of the volume of the device 1033 or of the devices 1033, it is possible to adjust the volume flows of the substance to be sprayed and of the gas which atomises the substance to be sprayed, to one another in a precise and targeted manner, so that the symmetry and the droplet size of the spray is set or can be set in an optimal manner for the process, in particular for the coating process of particles, preferably tablets. In
[0079] A section through the preferred nozzle 1001 is shown in
[0080] The preferred nozzle 1001 with a volume of the device 1003 which is enlarged in comparison to the open position according to
[0081] In the present embodiment example, the conduit 1032, in particular the part-sections 1017 and 1018 which are arranged in the nozzle mouthpiece 1006, as well as the annular gap 1008 are sealed off by way of the enlarged volume of the device 1033. The conduit 1032, here the part-sections 1018 are pressed together and the exit opening 1009 additionally closed due to the enlarged volume, so that a fluid can flow neither through the fluid channel 1005 nor through the annular gap 1008. By way of this, for example in the case of the filling of a granulator, a coater, in particular a drum coater, or a fluidisation apparatus, one succeeds in no pellets or particles being able to penetrate into the exits openings 1007, 1009 of the nozzle 1001 and therefore blocking these already before the beginning of the manufacturing process.
[0082] Further developments of the preferred nozzle 1001 which comprises a device 1033 which is changeable in its volume are conceivable. For example, there is the possibility of the nozzle 1001 comprising several devices 1033, in particular two devices 1003. Preferably, these are separated from one another by devices such as plates or the like, so that these can be operated independently of one another. Advantageously, the nozzle 1001 comprises a first device 1033 for the closure of the annular gap 1008 and a second device 1033 for the closure of the fluid channel 1005. Hereby, the two devices 1033 are preferably to be separated by way of a plate or the like which functions as a separating wall, so that the volume change of a first device 1033 closes or opens the fluid channel 1005 and the volume change of a second device 1033 closes or opens the annular gap 1008, without a volume change of the one device 1033 influencing the other device 1033. By way of this, it is possible to provide an infinite adjustment of the volume flow with a through-flow of 0% and 100% for the atomisation gas as well as for the substance to be sprayed, wherein the adjustment of the volume flows can be effected independently of one another or in a manner depending on one another. On using at least two devices 1033, it is to be noted that the substance to be sprayed, in particular the liquid cannot exit out of the nozzle 1001 in a non-atomised manner, since otherwise a product rejection can occur, for example by way of agglomerated tablets. For this, it is to be ensured that at the beginning of each spraying procedure, it is firstly the gas, in particular the atomisation gas which flows through the annular gap 1008 and thus out of the nozzle 1001 and subsequently the substance to be sprayed, in particular the liquid. On completing the spraying procedure, the feed of the substance to be sprayed is firstly to be stopped and subsequently that of the gas. A closed-loop control or control device can accomplish this. By way of this, it is ensured at all times that the substance to be sprayed is always atomised given a spraying procedure and that no substance to be spayed drips out of the nozzle possibly onto material to be treated (coated), at the end of each spraying procedure.
[0083] It is always to be ensured than on bringing the device 1033 from the one closure position of the inner pipe 1002 into the at least one open position of the inner pipe 1002, the gas which flows through the annular gap 1008 begins to flow through the annular gap at least simultaneously with the bringing of the device 1003 from the one closure position of the inner pipe 1002 into the at least one open position of to inner pipe 1002. It is further advantageous that on bringing the device 1033 from the at least one open position of the inner pipe 1002 into the one closure position of the inner pipe 1002, the gas which flows through the annular gap 1008 stops flowing through the annular gap 1008 at the earliest simultaneously on bringing the device 1033 from the at least one open position of the inner pipe 1002 into the one closure position of the inner pipe 1002.
[0084] Advantageously, on starting up or ending the spraying procedure, by way of this method it is ensured that no exit of the substance to be sprayed occurs at the nozzle mouth, which is to say at the exit openings 1007, 1009 of the inner pipe 1002 and the outer pipe 1003, without this substance being atomised directly by the gas which flows through the annular gap 1008. An atomisation of the substance to be sprayed is therefore always ensured by the method. By way of this, on the one hand deposits on the nozzle mouth for example given the drying of the substance to be sprayed which has exited too early and on the other hand an agglomeration of particles to be sprayed on account of the non-atomised substance to be sprayed do not occur.
[0085] The monitoring of the nozzle mouthpiece with regard to deposits by way of the sensor 134 in the embodiment example of
[0086] As soon as a certain stored limit values has been exceeded, for example due to deposits, by which means the symmetry and droplet size of the spray is compromised during the manufacturing and/or spraying process, the control unit 135 transmits a signal to be device 136. In the embodiment example of
[0087] The continuous monitoring of the preferred nozzle 101 which is carried out by the sensor 134 is preferably effected as an inline, atline or online measurement. For example, an ultrasound sensor detects the actual shape and the current dimensions of the preferred nozzle 101 (actual values). This data is subsequently used in the control unit 135 for assessing the spray quality and is compared to the initial data (setpoint) of the preferred nozzle 101. Preferably, given too large a difference between the actual value and the setpoint, a signal is transmitted from the control unit 135 to the device 136 and the necessary measures (vibration) are started. Hereby, the device 136 which is designed as a vibration unit is connected to the nozzle 101 and on receiving a signal from the control unit 135 brings the nozzle into a vibration, so that the deposits at the nozzle mouthpiece 106 detach. The incorporation of the aforementioned steps into the manufacturing and/or spraying process permits the automatic monitoring of the spray quality over the entire duration of the manufacturing and/or spray process.
[0088] The monitoring of the nozzle mouthpiece 106 by the sensor 134 with regard to deposits is effected by a sensor 134 which is arranged within the nozzle 101 in the embodiment example of
[0089] A second schematic construction of a method for monitoring the nozzle 101, in particular the nozzle mouthpiece 106, very particularly preferably the exit openings 107, 109 in the exit region 112 of a first embodiment of the preferred nozzle 101 is shown in
[0090] The two sensors 134 are sampled at a certain adjustable rate, or at a certain cycle. Should deposits or agglomerations occur at the nozzle 101, in particular at the nozzle mouthpiece 106, very particularly preferably at the exit openings 107, 109 in the exit region 112, then the pressure in the fluid channel 105 and/or the annular gap 108 increases (actual value).
[0091] This pressure increase is detected by the sensor 134 and is transferred to a control unit 135. For example, the mass flow and thus also the volume flow of the substance to be sprayed and/or of the atomisation gas can be computed by way of the detected physical measured variable, here for example the absolute pressure. The pressure which is detected with measurement technology at the sensors 134 provides information of the deposits on the nozzle mouth piece 106. Deposits b on the nozzle mouthpiece 106 lead to a pressure increase in front of the exit openings 107, 109 in the fluid channel 105 or annular gap 108 and thus to a larger flow speed of the substance to be sprayed and/or of the gas, so that given a suitable specification of thresholds values (setpoint) or tolerance ranges (for example ±10% deviation) and their exceeding or falling-short, the control unit 135 can initiate suitable counter measures for removing the deposits by way of transmitting a signal to the device 136.
[0092] On monitoring, a continuous comparison between the actual value and the setpoint takes place by the control unit 135.
[0093] As soon the exceeding or falling-short of a certain limit value (setpoint) is registered by the control unit 135, the control unit 135 transmits a corresponding signal to a device 136. In the embodiment example of
[0094] The monitoring of the droplet size of the spray during the manufacturing and/or spraying process, for example by way of a laser measuring method, forms a third method. Given deviations of the actual value from the setpoint of the droplet size, i.e., given a non-optimal droplet size, the measures which are to be made generally correspond to the measures of the first and second method according to