The present invention relates to powder spray coating apparatus—hereafter “powder spraycoating facility”—defined in the preamble of the independent claim 1.
Powder spraycoating facilities are known for instance form the documents U.S. Pat. No. 3,918,641; EP 0 412 289 B2; DE 42 39 496 A1 and DE 103 53 968 A1.
The objective of the present invention to render powder spraycoating facilities and powder spraycoating methods more efficient.
This problem is solved in the present invention by the features of its claim 1 or by those of its claim 23.
Further features of the present invention are defined in the dependent claims.
The present invention is elucidated below by illustrative, preferred embodiment modes and in relation to the 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 outline 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.
Preferably the powder intake apertures 26 are configured in a side wall of the intermediate receptacle 24, preferably near the bottom of the intermediate receptacle chamber 22, so that, when compressed-air flushes the intermediate receptacle chamber 22, even powder residues at the bottom can be expelled through the powder intake apertures 26, and for that purpose the powder feed conduits 20 preferably are separated from the sieve 10 and directed into a waste vessel as indicated by a dashed arrow 28 in
Powder pumps 4, for instance injectors, are connected to one or more powder outlet apertures 36 to move coating powder through powder conduits 38 to the sprayers 40. The sprayers 40 may be fitted with spray nozzles or rotary atomizers to spray coating powder 42 onto the object 2 to be coated, said object being situated in a coating cabin 43. Preferably the powder outlet apertures 36 are situated in a wall that is opposite the wall containing 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 of 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.
Compared to
Individual components/elements and combined sub-assemblies of components/elements of
A powder spraycoating facility comprising an intermediate receptacle (24) from which coating powder may be pneumatically moved at least to one sprayer (40); further comprising at least one sensor (S1) at the intermediate receptacle to generate a “powder needed” signal when the powder level in the intermediate receptacle (24) has dropped below a predetermined minimum level; a cyclone separator (48) to separate recovery powder from an airflow containing sprayed, excess powder that missed an object being coated characterized in that a recovery powder supply bin (48-2) is configured in the path of the recovery powder from the cyclone separator (48) to the intermediate receptacle (24) acting as an interim storage for the recovery powder in the recovery powder supply bin (48-2) before being fed into the intermediate receptacle; in that the recovery powder supply bin (48-2) is fitted with at least one supply bin sensor (S3) to generate a recovery powder data signal based on whether the powder level is below a minimum level or at least at it; in that a fresh-powder feed (70-74) serves to feed unsprayed fresh powder from a fresh-powder container (12; 14) into the intermediate receptacle (24) along at least one powder path which bypasses both the cyclone separator (48) and the powder recovery supply bin (48-2); in that there is at least one control (3) operationally connected to the sensors (S1, S3) to automatically drive the powder spraycoating facility and designed in a way that in a first operational mode only recovery powder from the recovery powder supply bin (48-2) is fed into the intermediate receptacle (24), but no fresh powder from the fresh powder feed unit (70, 74), when simultaneously there is a “powder needed” signal from the intermediate receptacle sensor (S1) and a recovery powder data signal from the recovery powder supply bin sensor (S3), the latter signal corresponding to a recovery powder level at or above the predetermined minimum level of recovery powder, whereas in a second operational mode, only fresh powder is fed from the fresh powder supply unit (70, 74) to the intermediate receptacle (24), but no recovery powder from the recovery powder supply bin (48-2) if there is a “powder needed” signal from the intermediate receptacle sensor (S1) and simultaneously there is a recovery powder data signal from the supply bin sensor (S3), where the latter signal corresponds to a recovery powder level below the said minimum level.
Powder spraycoating facility as claimed in claim 1, characterized in that the minimum of one supply bin sensor (S3) is configured at such a height on the recovery powder supply bin (48-2) that this bin comprises a powder reserve segment (202) situated below the supply bin sensor (S3), the powder reserve segment (202) storing a predetermined quantity of reserve recovery powder up to said minimum level.
Powder spraycoating facility as claimed in claim 2, characterized in that the minimum of one control (3) is designed to automatically switch the powder spraycoating facility from the second operating mode into reserve operating mode wherein the intermediate receptacle (24) receives only recovery powder from the powder reserve segment (202) of the recovery powder supply bin (48-2) but no fresh powder from the fresh powder supply unit (70, 74) when—following a predetermined time delay after switching from the first operating mode to the second operating mode—there continues to be a “powder needed” signal from the intermediate receptacle sensor (S1), the minimum of one control (3) being fitted with a time delay circuit defining the time delay or the time delay being adjusted at said circuit.
Powder spraycoating as defined in either of the embodiment modes 2 and 3, characterized in that the recovery powder supply bin (48-2) is fitted with a second supply bin sensor (S4) generating an emergency signal anytime the recovery powder level in the recovery powder supply bin (48-2) has dropped to a predetermined lower limit level situated at a predetermined distance below the predetermined recovery powder minimum level of the first supply bin sensor (S3).
Powder spraycoating facility as claimed in one of the above embodiment modes, characterized in that the recovery powder supply bin (48-2) is configured underneath the cyclone separator (48) and that a vertical passage is subtended between them through which the recovery powder is allowed to drop by gravity from the cyclone separator (48) into the recovery powder supply bin (48-2).
Powder spraycoating facility as claimed in one of the above claims, characterized the recovery powder supply bin (48-2) is fitted with a container housing constituted by a lower extension of the housing of the cyclone separator (48).
Powder spraycoating facility as claimed in one of the above claims, characterized in that the housing of the recovery powder supply bin (48-2) tapers from top to bottom in frustoconical manner.
Powder spraycoating facility as claimed in one of the above claims, characterized in that the recovery powder supply bin (48-2) is fitted with a fluidizing unit (66) to fluidize, by compressed air, recovery powder present in the recovery powder supply bin (48-2), said compressed air being fed through the fluidizing unit (66) into the recovery powder supply bin (48-2).
Powder spraycoating facility as claimed in one of the above claims, characterized in that a blocking device (64) preferably in the form of at least one pinch valve is mounted at the lower end of the recovery powder supply bin (48-2) to alternatingly block or open a powder outlet (204).
Powder spraycoating facility as claimed in one of the above claims, characterized in that the minimum of one intermediate receptacle sensor (S1, S2) and/or the minimum of one supply bin sensor (S3, S4) are powder level sensors generating the said signals as a function of the powder levels they detect.
Powder spraycoating facility as claimed in one of the above claims, characterized in that the fresh powder supply unit (70, 74) is fitted with a sensor (76) generating a first signal—as a function of the quantity of fresh powder in a fresh powder container (12) in the fresh powder supply unit (70, 74)—preferably always when the quantity of fresh powder in the fresh powder container (12) drops below a predetermined residual quantity.
Powder spraycoating facility as claimed in claim 11, characterized in that the sensor (76) of the fresh powder supply unit (70, 74) is operationally connected to the minimum of one control (3) and generates a second signal in the minimum of one control when the quantity of fresh powder in the fresh powder container (12) has decreased to a lower quantity limit value that is a particular distance below a predetermined residual quantity at which said first signal is being generated.
Powder spraycoating facility as defined in embodiment mode 12, characterized in that upon receiving the second signal from the sensor (76) of the fresh-;powder supply unit (70, 74), the minimum of one control (3) switches the powder spraycoating facility to a mode of reserve operation provided a “powder needed” signal is also generated also by the minimum of one intermediate receptacle sensor (S1), where, during the reserve mode, only recovery powder from the powder reserve segment (202) of the recovery powder supply bin (48-2) is fed to the intermediate receptacle (24), but no fresh powder from the fresh powder supply unit (70, 74).
Powder spraycoating facility as claimed in claim 11, characterized in that the sensor (76) of the fresh powder supply unit (70, 74) is operationally connected to the minimum of one control (3) and in that the minimum of one control (3) is designed in a manner that—in response to the first signal from the sensor (76) of the spraycoating facility's fresh powder supply unit (70, 74)—it shall switch the spraycoating facility to the reserve mode provided the minimum of one intermediate receptacle sensor S1) also generates a “powder needed” signal, where, in the reserve mode only recovery powder from the powder reserve segment (202) of the recovery powder supply bin (48-2) is fed to the intermediate receptacle (24), but no fresh powder from the fresh powder supply unit (70, 74).
Powder spraycoating facility as defined in embodiment mode 11, characterized in that the sensor (76) of the fresh powder supply unit (70, 74) is operationally connected to the minimum of one control (3) and in that the minimum of one control (3) is designed in a manner that, in response to the first signal from the sensor (76) of the fresh powder supply unit (70, 74), it switches the spraycoating facility to a reserve mode provided a “powder needed” signal is also generated by the minimum of one intermediate receptacle sensor (S1), where—in the reserve mode—only recovery powder from the powder reserve segment (202) of the recovery powder supply bin (48-2) is fed to the intermediate receptacle (24), but no fresh powder from the fresh powder unit (70, 74), and where the control (3) contains a time delay circuit as a result of which the switching to the reserve mode takes place only after a predetermined time delay itself following receiving the first signal of the sensor (76) of the fresh powder supply (70, 74).
Powder spraycoating facility as defined in one of embodiment modes 11 through 15 characterized in that the sensor (76) of the fresh powder supply unit (70, 74) is a scale weighing the fresh powder in a fresh powder container (12).
Powder spraycoating facility as claimed in one of the above claims, characterized in that a sieve (10) is configured in the path followed by the recovery powder from the recovery powder supply bin (48-2) to the intermediate receptacle (24).
Powder spraycoating facility as claimed in claim 17, characterized in that the path followed by the fresh powder from the fresh powder supply unit (70, 74) to the intermediate receptacle (24) also passes through the sieve (10), whereby the fresh powder also will be sifted.
Powder spraycoating facility defined by either of embodiment modes 17 and 18, characterized by a powder pump (4) configured in a powder path segment (50)—which is preferably sealed relative to the atmosphere—of the recovery powder from the recovery powder supply bin (48-2) to the intake side of the sieve (10), preferably said sieve input side also being coating-powder tight relative to the atmosphere.
Powder spraycoating facility defined in either of embodiments 18 and 19 characterized by one powder pump (4) each in the minimum of one powder path segment (16)—which is preferably sealed relative to the atmosphere—of the fresh powder, from the fresh powder container (12) of the fresh powder supply unit (70, 74) to the intake side of the sieve (10), preferably said sieve intake side also being coating-powder tight relative to the atmosphere.
Powder spraycoating facility as defined in one of embodiment modes 17 through 20, characterized by one powder pump (4) each in the powder path segment (20)—which preferably is sealed relative to the atmosphere—from an output side of the sieve (10) into the intermediate receptacle (24), preferably the output side of the sieve (10) and the intermediate receptacle (24) also being coating-powder tight relative to the atmosphere.
Powder spraycoating facility as defined in at least one of the above embodiment modes, characterized by one powder pump (4) each in the minimum of one coating powder path (38) from the intermediate receptacle (24) to the minimum of one sprayer (40).
A powder spraycoating method, in particular to operate the powder spraycoating facility claimed in one of the above claims, whereby coating powder is pneumatically moved from an intermediate receptacle (24) to a minimum of one sprayer (40); further by at least one sensor (S1) at the intermediate receptacle (24) generating a “powder needed” signal when the powder level in the intermediate receptacle (24) drops below a predetermined coating powder level; by a cyclone separator (48) separating recovery powder from an airflow, where said recovery powder contains sprayed excess powder that missed an object being coated; characterized in that, on the path from the cyclone separator (48) to the intermediate receptacle (24), the recovery powder is temporarily held in a recovery powder supply bin (48-2), in that by means of at least one supply bin sensor (S3) a recovery powder data signal is generated as a function of the powder level in the recovery powder supply bin (48-2) being below a minimum level or at least at the minimum level; that unsprayed fresh powder is fed from a fresh powder container (12) to the intermediate receptacle (24) along a powder path bypassing the cyclone separator (48) as well as the recovery powder supply bin (48-2); that depending on signals transmitted by the sensors (S1, S3) and by means of a control (3), the powder spraycoating facility is automatically driven in a first operating mode wherein the intermediate receptacle (24) receives only recovery powder from the recovery powder supply bin (48-2) but no fresh powder from the fresh powder supply unit (70, 74) when the intermediate receptacle sensor (S1) transmits a “powder needed” signal and simultaneously the recovery powder supply bin sensor (S3) transmits a recovery powder data signal which corresponds to a recovery powder level at or above the predetermined minimum level, but switching into a second operating mode automatically taking place and the powder spraycoating facility being operated in said second mode whereby only fresh powder from the fresh powder supply unit (70, 74) is fed to the intermediate receptacle (24) but no recovery powder from the recovery powder supply bin (48-2) when the intermediate receptacle sensor (S1) transmits a “powder needed” signal and simultaneously the recovery powder supply bin sensor (3) transmits a recovery powder data signal which corresponds to a recovery powder level below the said minimum recovery powder level.
Powder spraycoating facility method as defined in embodiment mode 23, characterized in that a reserve quantity of recovery powder is stored in a lower powder reserve segment (202) of the recovery powder supply bin (48-2) during the first operating mode and in that switching from the second operating mode into a reserve operating mode which shall be automatically implemented and during which the intermediate receptacle (24) only receives recovery powder from the reserve quantity of recovery powder of the powder reserve segment (202) but no fresh powder from the fresh powder supply unit (70, 74) when, following a predetermined delay time after switching from the first operating mode to the second operating mode a “powder needed” signal is still being transmitted from the intermediate receptacle sensor (S1).
Number | Date | Country | Kind |
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10 2007 005 309.8 | Feb 2007 | DE | national |