The present invention relates to a powder level sensor unit detecting spraycoating powder in a powder container.
The powder container may be dimensionally stable or a flexible bag.
There is danger when measuring such a powder level that the spraycoating powder might adhere to the detection side of the sensor unit and that as a result there will be errors in detection.
The objective of the present invention is to eliminate detection errors of that kind.
This problem is solved by the present invention by the features of its claim 1.
Accordingly the present invention relates to a powder-level sensor unit for spraycoating powder and in a powder container containing at least one sensor measuring the powder level in said container, characterized in that it is fitted with a compressed air chamber which is bounded at its rear by a sensor detection surface pointing in the detection direction and constituting the sensor detection side and at its front side by a porous wall configured opposite to and some distance from the sensor detection surface; and it that said powder container is fitted with a compressed air duct connecting the compressed air chamber to an external, compressed-air hookup, the porous front wall being permeable on account of its pores only to compressed air but not to spraycoating powder and the front wall being designed in a manner that the sensor may detect, through it, spraycoating powder and transmit a sensor signal as a function of such a detection.
Further features of the present invention are defined in the dependent claims.
The inventions are elucidated below by illustrative embodiment modes and in relation to the appended drawings.
Illustratively such injectors are known from the European patent document EP 0 412 289 B1.
The powder pump(s) used may be the kind that sequentially move small doses of powder, each small powder dose (quantity of powder) being stored in a powder chamber and then being expelled by compressed air from the powder chamber. The compressed air remains behind the powder dose and pushes it ahead. Such pumps occasionally are called compressed-air thrust pumps or plug moving pumps because the compressed air pushes the stored powder dose like a plug/stopper before it through a pump outlet conduit. Various kinds of powder pumps moving packed coating powder are illustratively known from the following documents: DE 103 53 968 A1; U.S. Pat. No. 6,508,610 B2; US 2006/0193704 A1; DE 101 45 448 A1 and WO 2005/051549 A1.
The invention is not restricted to one of the above cited pump types.
A source of compressed air 6 is used to generate the compressed air to pneumatically move the coating powder and to fluidize it, said source being connected to the various components by corresponding pressure adjusting elements 8 such as pressure regulators and/or valves.
Fresh powder from the manufacturer is fed from a vendor's container—which may be a small container 12, for instance a dimensionally stable container or a bag holding for instance 10 to 50 kg powder, for instance 25 kg, or for instance a large container 14 also dimensionally stable or a bag holding for instance between 100 kg and 1,000 kg powder—by means of a powder pump 4 in a fresh powder conduit 16 or 18 to a sieve 10. The sieve 10 may be fitted with a vibrator 11. Herein the expressions “small container” and “large container” denote both dimensionally stable containers and those which are not, such as flexible bags, unless as otherwise noted.
The coating powder sifted through the sieve 10 is moved by gravity or preferably always by a powder pump 4 through one or more powder feed conduits 20 through powder intake apertures 26 into an intermediate receptacle chamber 22 of a dimensionally stable intermediate receptacle 24. Preferably the volume subtended by the intermediate receptacle 22 is substantially smaller than that of the fresh powder small container 12.
In a preferred embodiment mode of the invention, the powder pump 4 of the minimum of one powder feed conduit 20 leading to the intermediate receptacle 24 is a compressed air pump. In this instance the initial segment of the powder feed conduit 20 may serve as a pump chamber which receives the powder sifted through the sieve 10 as it drops through a valve, for instance a pinch valve. Once this pump chamber contains a given powder portion, the powder feed conduit 20 is shut off from the sieve 10 due to valve closure. Next the powder portion is forced by compressed air through the powder feed conduit 20 into the intermediate receptacle chamber 22.
The powder intake apertures 26 preferably are configured in a side wall of the intermediate receptacle 24, preferably near the bottom of the intermediate receptacle chamber 22, so that, when flushing the said chamber with compressed air, powder residues at the bottom can be expelled through the powder intake apertures 26; for that purpose the powder feed conduits 20 preferably are separate from the sieve 10 and are pointing into a waste vessel as schematically indicated in
Powder pumps 4, for instance injectors, are connected to one or preferably more powder outlet apertures 36 to move coating powder through powder conduits 38 to sprayers 40. The sprayers 40 may be spray nozzles or rotary atomizers used to spray the coating powder 42 onto the object 2 to be coated, which preferably is situated in a coating cabin 43. Preferably the powder outlet apertures 36 are configured in a wall opposite that wall which contains the powder intake apertures 26. Preferably the powder outlet apertures 36 also are configured near the bottom of the intermediate receptacle chamber 22.
Preferably the size of the intermediate receptacle chamber 22 allows storing coating powder in amounts between 1.0 and 12 kg, preferably between 2.0 and 8.0 kg. In other words, the size of the intermediate receptacle chamber 22 preferably shall be between 500 and 30,000 cm3, preferably between 2,000 and 20,000 cm3. The size of the intermediate receptacle chamber 22 is selected as a function of the number of powder outlet apertures 36 and of powder conduits 38 connected to them in a manner to allow continuous spraycoating while also allowing rapidly cleaning the intermediate receptacle chamber 22 during pauses of operation for purposes of powder changes, preferably in automated manner. The intermediate receptacle chamber 22 may be fitted with a fluidizing means to fluidize the coating powder.
Coating powder 42 failing to adhere to the object 2 is aspirated as excess powder through an excess powder conduit 44 by means of a flow of suction air from a blower 46 into a cyclone separator 48. In the cyclone separator, the excess powder is separated as much as possible from the suction flow. The separated powder proportion is then moved as recovery powder from the cyclone separator 48 through a recovery powder conduit 50 to the sieve 10 and from there it passes through said sieve either by itself or admixed to fresh powder, through the powder feed conduits 20 once more, into the intermediate receptacle chamber 22.
Depending on the kind of powder and/or the intensity of powder soiling, the powder recovery conduit 50 also may be separated from the sieve 10 and the recovery powder may be moved into a waste vessel as schematically indicated by a dashed line 51 in
The intermediate receptacle 24 may be fitted with one or more sensors, for instance two sensors S1 and/or S2 to control feeding coating powder into the intermediate receptacle chamber 22 by means of the control 3 and the powder pumps 4 in the powder feed conduits 20. Illustratively the lower sensor S1 detects a lower powder level limit and the upper sensor S2 detects an upper powder level limit.
The lower end segment 48-2 of the cyclone separator 48 can be designed and used as a recovery powder supply bin and be used as such and be fitted for that purpose with one or several illustratively two sensors S3 and/or S4 which are operationally connected to the control 3. As a result the fresh powder feed through the fresh powder feed conduits 16 and 18 may be blocked, especially in automated manner, until enough recovery powder shall accumulate in the cyclone separator 48 to feed through the sieve 10 enough recovery powder into the intermediate receptacle chamber 22 for spraycoating by the sprayer 40. Once the recovery powder becomes insufficient in the cyclone separator 48 for such operation, the switchover to the fresh powder feed through the fresh powder conduits 16 or 18 may automatically kick in. The invention also offers the possibility to simultaneously feed fresh and recovery powders to the sieve 10 to mix them.
The exhaust air of the cyclone separator 48 passes through an exhaust air conduit 54 into a post filtration system 56 and therein through one or more filter elements 58 to arrive at the blower 46 and beyond latter into the atmosphere. The filter elements 58 may be filter bags or filter cartridges or filter plates or similar elements. Ordinarily the powder separated from the air flow by means of the filter elements 58 is waste powder and drops by gravity into a waste vessel, or, as shown in
Depending on the kind of powder and on the powder coating conditions, the waste powder also may be recovered and moved to the sieve 10 in order to be recirculated into the coating circuit. This feature is schematically indicated in
Typically only cyclone separators 48 and the post filtration system 56 are used for multicolor operation, wherein different colors each are sprayed only for a short time, and the waste powder of the post filtration system 56 is moved into the waste vessel 62. In general the powder-separating efficiency of the cyclone separator 48 is less than that of the post filtration system 56, but cleaning is more rapid than in the post filtration system 56. As regards monochrome operation, wherein the same powder is used for a long time, the cyclone separator 48 may be dispensed with, and the excess powder conduit 44 instead of the exhaust air conduit 54 may be connected to the post filtration system 56, and the waste conduits 60—which in this instance contain recovery powder—act as powder recovery conduits to the sieve 10. Typically the cyclone separator 48 is used in combination with the post filtration system 56 in monochrome operation only when the coating powder entails problems. In such eventuality only the recovery powder of the cyclone separator 48 is moved through the powder recovery conduit 50 to the sieve 10 whereas the waste powder of the post filtration system 56 is moved into the waste vessel 62 or into another waste vessel, said waste vessel being optionally free of waste conduits 60 and directly positioned underneath an outlet aperture of the post filtration system 56.
The lower end of the cyclone equipment 48 may be fitted with an outlet valve 64, for instance a pinch valve. Moreover fluidizing means 66 to fluidize the coating powder may be configured above said outlet valve 64, in or at the lower end segment 48-2, constituted as a supply bin of the cyclone separator 48. The fluidizing means 66 contains at least one fluidizing wall 80 made of material comprising open pores or fitted with narrow boreholes, this material being permeable to compressed air but not to the coating powder. The fluidizing wall 80 is situated between the powder path and a fluidizing compressed air chamber 81. The fluidizing compressed air chamber 81 may be connected by a compressed air adjusting element 8 to the compressed air source 6.
For the purpose of aspirating fresh coating powder, the fresh powder conduit 16 and/or 18 may be connected to allow powder flow at is upstream end either directly or through the powder pump 4 to a powder feed pipe 70, said pipe being dippable into the manufacturer's container 12 or 14. The powder pump 4 may be mounted at the beginning of, the end of, or in-between, in the fresh powder conduit 16 or 18 or at the upper or lower end of the powder feed pipe 70.
A small fresh powder container in the form of a fresh powder bag 12 is shown in
Two or more small containers 12 may be configured each in a bag-receiving hopper 74, also two or more large containers 14 operating alternately. This feature allows rapidly changing from a small container 12 to another or to one large container 14.
The invention may be modified in a number of ways without restricting it. For instance the sieve 10 may be integrated into the intermediate receptacle 24. Alternatively the sieve 10 may be omitted when the fresh powder quality is high enough. In that case a separate sieve may be used to sift the recovery powder of the conduits 44 and 50, illustratively upstream or downstream of the cyclone separator 48 or in it. Again, sifting the recovery powder will not be required when its quality is adequate for re-use.
Powder level sensor units of the present invention are elucidated below. The above cited sensors S1, S2, S3 and S4 may be designed in the manner of the powder level sensor units 100, 200 or 300. They may be switching or non-switching elements.
The powder level sensor unit 100 shown in
The powder level sensor unit 100 comprises a compressed air chamber 106 which is bounded at its rear by a sensor detection surface 108 pointing in the direction of detection and constituting the detection side of the sensor 102, at its front by a front wall 110 opposite to and spaced from the sensor detection surface 108, and at the chamber periphery/circumference by a peripheral/circumferential wall 112 enclosing the compressed air chamber.
The front wall 110 is porous and permeable to air in a manner that it is permeability applies over its full size to the compressed air in the compressed air chamber 106 but on the other hand this wall 110 is impermeable to the spraycoating powder 105 in the powder container on the outer side of the front wall 110 away from the compressed air chamber 106. Illustratively the front wall 110 is a membrane. The open pores or ducts (hereafter all called “pores”) of the porous front wall 110 are so tiny that the compressed air from the compressed air chamber 106 can only flow in the form of tiny compressed air bubbles or thin jets of compressed air 103 into the powder container.
The sensor 102 and the front wall 110 are designed in a manner that that said sensor is able to detect spraycoating powder 105 through said front wall and will transmit a signal on a signal line 114 as a function of its detection.
A compressed air duct 113 runs from the compressed air chamber 106 to an external compressed-air hookup 116. Control elements such as a pressure regulator 120 and/or one or several valves of a compressed air source 6 may be connected to said compressed air hookup 116. The compressed air flows through the compressed air duct 113 into the compressed air chamber 106 and from there is spread out thinly over the entire front wall 110, passing through this front wall's small pores into the inner container space 122 of which the powder level shall be detected.
The sensor 102, the porous front wall 110 and the enclosing wall 112 together preferably constitute a mechanical unit affixable to a container wall 124 either on a wall surface or as shown in
As indicated in
The sensor signal line 114 is connected to a control 130 generating a drive signal as a function of the signals transmitted to it by the sensor 102 and hence as a function of the measured powder level 104. The control signal may be optical, acoustic or of another kind and/or it may be a control signal driving components of the powder spraycoating facility of
The porous front wall 110 amounts to a detection measurement obstacle to the sensor 102 and therefore entails a measurement error unless corrected for. Such measurement error must be subtracted from the measurement value detected by the sensor 102 in order to form a measurement signal reflecting the actual powder level 104. For that purpose the sensor may be calibrated in a manner that the signal it transmits on the sensor signal line 114 already includes the corrected measured value, or the control 130 may be designed to perform such a correction.
Whereas the embodiment modes of
The powder container within which the powder level is measured may be a dimensionally stable container or a flexible bag or flexible pouch.
Number | Date | Country | Kind |
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10 2007 005 348.9 | Feb 2007 | DE | national |