The present disclosure relates to powder coating systems that use a hopper for supplying or feeding powder to one or more coating application devices. More particularly, the disclosure relates to powder coating hoppers that produce a fluidized supply of powder, and also separately relates to powder coating equipment that may be used with such hoppers.
In powder coating systems, powder coating material is commonly transferred from a bulk supply or supply hopper to a feed hopper, and then a pump is used to convey the powder from the feed hopper to one or more application devices, such as, for example, a spray gun. A feed hopper is commonly a fluidized hopper which fluidizes the powder coating material before it is pumped to a spray gun or application device. For some powder coating applications, a very fine powder coating material must be used to achieve the desired surface finish or other coating property. While there are various applications in which powder coating equipment suitable for fine powders are useful, one example is a powder coating system for the inside coating of small diameter tube shaped containers.
In accordance with an embodiment of one of the inventions presented in this disclosure, a hopper for powder coating material comprises a hopper body, a fluidizing bed, a cover, and a baffle that is disposed inside the hopper body. A powder inlet is disposed between the baffle and the hopper body, with the baffle functioning to provide a low turbulence zone for fluidized powder. In a more specific embodiment the hopper body and baffle are cylindrical, so that an annular region is provided therebetween, with the powder inlet disposed in the annular region. Alternatively, the annular region may be the low turbulence zone with powder added inside the baffle. In another embodiment, the axial length of the baffle is such that a lower gap is provided between the baffle and the fluidizing bed, and an upper gap is provided between the baffle and the cover. In additional alternative embodiments, an optional agitator may be provided near the fluidizing bed in the region of the lower gap, one or more optional venting pumps may be used to keep the hopper at a negative pressure, an optional switch may be used to deactivate an optional air motor when the cover is separated from the hopper body, and one or more pumps may be used to pump fluidized powder from the low turbulence zone to one or more coating material application devices.
This disclosure also presents one or more inventions relating to a powder coating material application device and a nozzle therefor. In one embodiment, the nozzle may comprise a plurality of discrete flow passages disposed about a longitudinal axis of the nozzle.
The disclosure also presents one or more inventions relating to a powder coating material application system that utilizes the hopper as set forth above, a coating material application device as set forth above, and the combination thereof.
The disclosure also presents one or more inventions relating to a method for operating a powder supply hopper wherein the method includes the steps of venting air from an internal volume at a higher rate when powder is being added to the volume and at a lower rate to vent fluidizing air from the volume.
These and other aspects and advantages of the inventions disclosed herein will be understood by those skilled in the art from the following detailed description of the exemplary embodiments in view of the accompanying drawings.
The inventions are described herein with particular reference to exemplary illustrations and embodiments, however, the inventions are not limited to such exemplary embodiments. For example, the hopper concepts may be used with many different configurations of the hopper and associated optional components, and from a system standpoint may be used with many different types of coating material application devices, pumps, bulk feed and control systems, all of which are well known or may be later developed. The application device and nozzle concepts may be used with many different hopper arrangements, pumps and so on, including the embodiments illustrated herein. While the exemplary embodiments are illustrated and discussed in terms of a coating application system for small diameter tube shaped containers, other container shapes and types may alternatively be coated.
While various inventive aspects, concepts and features of the inventions may be described and illustrated herein as embodied in combination in the exemplary embodiments, these various aspects, concepts and features may be used in many alternative embodiments, either individually or in various combinations and sub-combinations thereof. Unless expressly excluded herein all such combinations and sub-combinations are intended to be within the scope of the present inventions. Still further, while various alternative embodiments as to the various aspects, concepts and features of the inventions—such as alternative materials, structures, configurations, methods, circuits, devices and components, software, hardware, control logic, alternatives as to form, fit and function, and so on—may be described herein, such descriptions are not intended to be a complete or exhaustive list of available alternative embodiments, whether presently known or later developed. Those skilled in the art may readily adopt one or more of the inventive aspects, concepts or features into additional embodiments and uses within the scope of the present inventions even if such embodiments are not expressly disclosed herein. Additionally, even though some features, concepts or aspects of the inventions may be described herein as being a preferred arrangement or method, such description is not intended to suggest that such feature is required or necessary unless expressly so stated. Still further, exemplary or representative values and ranges may be included to assist in understanding the present disclosure, however, such values and ranges are not to be construed in a limiting sense and are intended to be critical values or ranges only if so expressly stated. Moreover, while various aspects, features and concepts may be expressly identified herein as being inventive or forming part of an invention, such identification is not intended to be exclusive, but rather there may be inventive aspects, concepts and features that are fully described herein without being expressly identified as such or as part of a specific invention, the inventions instead being set forth in the appended claims. Descriptions of exemplary methods or processes are not limited to inclusion of all steps as being required in all cases, nor is the order that the steps are presented to be construed as required or necessary unless expressly so stated.
With reference to
The hopper 10 includes a hopper body 12 which may be in the form of a right cylinder having an upper end 14 and a lower end 16. Clamps or straps 18 or other suitable attachment means may be used to join a fluidizing drum 20 to the lower end 16 of the hopper body 12. A fluidizing subassembly 22 which may include the hopper body 12 and the fluidizing drum 20 is illustrated in greater detail in
Clamps or straps 24 or other suitable attachment means, which may be but need not be the same as the clamps 18, may be used to join a cover 26 to the upper end 14 of the hopper body 12. The cover, 26, when fully installed for operation, seals the hopper 10 and also supports various pumps, an air motor and related equipment used with the hopper 10 assembly. For example, one or more optional venting pumps 28 may be disposed on the cover 26. These venting pumps 28 may be used to reduce pressure buildup within the hopper 10, and in particular may optionally be used to maintain the hopper 10 interior at a somewhat negative pressure, for example, on the order of less than about three inches mercury. Although two venting pumps 28 are illustrated in
Also disposed on the cover 26 are one or more feed pumps 34, in this example four are shown. The feed pumps 34 are used to suck fluidized powder from the hopper 10 and pump the powder to one or more application devices (see
Each feed pump 34 further includes a suction tube connection 44 which connects a suction tube 46 (
Still referring to
A level sensor arrangement 54 may be provided on the outside of the hopper body 12 and may be conventional in design as needed. A suitable level sensor is part no. 237199 available from Nordson Corporation, Westlake, Ohio, but other level sensors may be used as needed. The level sensor is used to detect the level of fluidized powder in the hopper and produce a signal when powder coating material needs to be added to the hopper 10. In many system applications, powder will be consumed from the hopper 10 in a continuous or near continuous mode, so that the level sensor 54 provides the necessary feedback as to when there is a demand for powder to be added.
At least one, and in the exemplary embodiments herein there are two, powder inlet connection 56 is provided, in this example in the cover 26. Each powder inlet connection 56 is connectable to a supply hose 58 (
Finishing with the
With reference to
As illustrated in
The axial length of the baffle body 102 is also selected so as to allow for a lower gap 110 between a lower end 102b thereof and the fluidizing plate 84. This lower gap 110 allows powder coating material to flow into the interior region or low turbulence zone 106 of the baffle 100, and accommodates agitator arms 112 that are part of the agitator 66. The agitator arms 112 in this example may extend out from the main agitator shaft 114 like spokes on a wheel, so as to help fluidize and uniformly distribute powder coating material as the agitator 66 rotates. The agitator arms 112 preferably although not necessarily extend radially beyond the outer perimeter of the baffle 100 so as to stir the fluidized powder over most or all of the surface of the fluidizing plate 84 including within the low turbulence zone 106 and the annular zone 104. The agitator arms 112 may be disposed fairly near the surface of the fluidizing plate 84 and extend through the lower gap 110. The suction tubes 46 preferably although not necessarily extend axially down to near but above the lower end 102b of the baffle body 102, so as not to be exposed to the more turbulent flow that is present in the annular region 104 (as shown in phantom in
Inlet tubes 116 may be used to add powder coating material into the annular region 104. In the exemplary embodiments herein, two inlet tubes 116 are provided. Each inlet tube 116 has a first end 118 that extends up into its associated powder inlet connection 58, and a second end 120 that is positioned within the annular region 104. The second ends 120 thus present outlet openings 122 through which powder coating material is supplied to the hopper 10 within the annular region 104. These openings 122 preferably although not necessarily are positioned axially above the lower end 102b of the baffle body 102 so as to reduce turbulence in the quiet zone 104. These outlet openings 122 are preferably although not necessarily diametrically opposite each other, and if more than two inlet tubes are used, preferably evenly distributed about the circumference of the annular region. In some designs, however, a single inlet tube may be used. Using more than one inlet tube 116 allows for less delivery air volume to reduce over pressure, and also allows for a lower inlet air and powder velocity.
As best illustrated in
The inlet tubes 116 each introduce powder coating material into the annular region 104 preferably in the same direction of rotation Z. Optionally, but preferably, the agitator 66 is rotated in this same direction Z. The direction Z may be clockwise or counterclockwise as needed. In an exemplary hopper 10, fluidizing air flow may be about 3-4 cubic feet per minute (cfm), while the bulk air flow for adding powder coating material into the annular region 104 may be about 5-6 cfm. The agitator may rotate at any suitable speed, and we have found 90-100 rpm works well.
As noted hereinabove, in many applications it may be preferred to maintain a negative pressure inside the hopper 10 for containment and to prevent over-pressurizing the hopper 10. Too much pressure inside the hopper may have deleterious effects on fluidization of the powder, powder flow rate to the spray guns, powder density and uniformity, and may also adversely affect operation of the Venturi pumps 34 which pull powder from the hopper with suction and, therefore, may be affected by the internal hopper pressure. Even when powder coating material is not being added, the venting pumps 28 may be operated so as to reduce pressure within the hopper 10 that may otherwise build up due to the fluidizing air from the fluidizing plate 84. When powder coating material is added to the hopper 10, the venting pumps 28 will typically need to vent even more air because of the increase in air flow into the hopper 10 from the bulk supply pumps 62.
As best viewed in
With reference to
Moreover, in accordance with one of the inventions herein, the control circuit 204 may include with the bulk feed control input signal 216 from the level sensor 54. This signal may be used to indicate a demand for powder into the hopper 10. When powder needs to be added, the feed control 212 activates via control line 213 the bulk supply pump 62 which may use transport air to move powder from the bulk supply 60 into the hopper 10 via the inlet tubes 116. The feed control 212 (or another control circuit or function as needed) may also be used to control operation of the venting pumps 28. As noted above, for Venturi-type venting pumps, the air flow or suction pulled by the venting pumps 28 may be controlled by the flow air to the pump inlets 30. The feed control 212 may use a venting pump control signal 218 to operate a control valve 220. The control valve 220 may be used to deliver two different pressures or air flow rates 222 to the venting pump inlets 30. When powder is not being added to the hopper 10, the venting pumps 28 may be operated at a lower or idle suction rate, for example, about 3-4 cfm. This lower suction is used to remove fluidizing air so as to maintain a negative pressure within the hopper 10. When powder is added, however, in addition to the fluidizing air there is transport air added with the powder feed from the feed pumps 62. Therefore, the feed control 212 may be used to switch the control valve 220 so as to increase the flow air 222 to the venting pump inlets 30 to increase the suction, for example, to about 7-8 cfm. The amount of venting suction for any given system will depend in part on the fluidizing air flow rate and the flow rate of air for transporting powder from the pumps 62 to the hopper 10. The increased flow air to the venting pumps 28 increases the suction of the venting pumps 28 to pull more air from the hopper 10 as powder is being added. When powder feed stops, the venting pumps 28 may be returned to the idle suction rate.
The amount of increased venting suction needed when powder is added to the hopper 10, as well as the idle suction needed when powder is not being added, will be a function of many factors including but not limited to the amount of fluidizing air, size of the hopper, properties of the powder material such as density and particle size, amount of transport air, feed rates into the hopper and so on. Accordingly, for each set-up, the required idle suction and increased suction may be determined empirically and pre-set into the venting control system 204 as part of the set-up procedures.
Alternatively, pressure sensors (not shown) that monitor internal pressure in the hopper 10, such as near the cover 26, for example, may be used to provide a closed loop pressure feedback control in order to maintain the desired internal hopper pressure when powder is being added and when powder is not being added. The pressure sensor feedback signals may be used to control either fluidizing air flow, the venting pump 28 suction, or both. As still another alternative, pressure data could be viewed and manual adjustments made to control the fluidization air flow, the venting pump suction, or both.
With reference to
With reference to
The feed hose 256 extends into the main housing and fits over a barbed end 274 of a powder tube 276 that may be provided as part of the lance assembly 258. Preferably, although not necessarily, the powder tube 276 inside diameter is about the same as the inside diameter of the feed hose 256 that extends back to the feed pump outlet. The powder tube 276 extends through the lance assembly 258 up to an electrode assembly holder 278 (
With reference to
The nozzle 260 may include nozzle information-related coding or indicia, for example, one or more optional grooves 292. These grooves 292 (one shown in
The charging electrode first contact spring 282 has a contact end that makes electrical contact with the resistor/conductor assembly 268 (
Preferably the electrode tip 272 exits the nozzle 260 so as to be about in the center of the powder coating material spray pattern. The charging electrode 287 may pass through an outer portion of the nozzle 260 before terminating in the central region of the powder flow passages (296), or alternatively may extend straight through the center of the nozzle, for example. Still further the charging electrode may extend through a rib (not shown) along an outer periphery of the nozzle 260.
The nozzle 260 may include a main nozzle body 294 with a plurality of powder coating material flow passages 296 formed therein. The nozzle body 294 may be attached to the electrode holder 278 by any suitable arrangement, such as a press fit as illustrated in
The flow passages 296 extend from an interior surface 298, about the base of a conical tip 400. The conical tip 400 extends axially rearward to assist uniform distribution of powder coating material that flows into the nozzle 260 to pass through the plurality of flow passages 296. The cone angle β, which is the half angle referenced to the axis Y, may be the same or different from the angle α. Suitable but not required ranges for the angle α is about 0° to about 20° and will be determined in part by the internal diameter of the container being coated, as well as whether more than one nozzle is being used for a coating operation. Suitable but not required ranges for the angle β is about 10° to about 15°, with 15° being illustrated in the drawings.
The use of the nozzle 260 and the flow passages 296 provide a more uniformly dispersed powder spray pattern than is achieved in prior nozzle designs. Accordingly, the nozzle 260 with a plurality of discrete powder flow passages 296 facilitate use of the applicator 250 to coat open or closed end containers while the container may be rotationally stationary during a coating operation. By “rotationally stationary” is meant that there is no relative rotation between the powder coating material applicator 250, such as the nozzle 296, for example, and the container being coated during a coating operation. In a more specific example, the container may be coated without having to rotate the container itself. The use of discrete multiple flow passages also produces a more uniform film thickness. Can or nozzle rotation may be alternatively used as needed.
For electrostatic embodiments, placing the charging electrode tip 272 in about the center of the spray pattern improves the charging of the powder particles, particularly with the more uniform distribution of powder in the spray pattern due to the use of the nozzle 260 with a plurality of discrete flow passages 296.
Each flow passage 296 in the exemplary embodiment has a circular cross-section and a diameter that is constant along the entire length of each flow passage. However, such geometry is not required, and may be changed as needed to achieve particular spray patterns, flow velocities and so on. For example, the flow passages might alternatively have a varying diameter, or may have a cross-sectional shape other than circular. The discrete flow passages 296 open at an end face of the nozzle 260 (see the examples below), with the openings preferably being evenly spaced about the longitudinal axis of the nozzle. It is further preferred, although again not required, that the total cross-sectional area of the flow passages be at least equal to or greater than the cross-sectional area of the nozzle inlet flow passage 402 that is just upstream from the nozzle 260. The cross-sectional area of the nozzle inlet flow passage 402 is preferably but need not be about the same as the cross-sectional area of the inside diameter of the powder tube 276, such that there is a generally constant cross-sectional area for the powder flow path that extends from the outlet of the feed pump 34 all the way through the nozzle 260.
An example of a typical tube shaped container C that may be coated with the apparatus disclosed herein is illustrated in phantom in
With reference to
The inventive aspects have been described with reference to the exemplary embodiments. Modification and alterations will occur to others upon a reading and understanding of this specification. It is intended to include all such modifications and alterations insofar as they come within the scope of the appended claims or the equivalents thereof.
The present application is a national phase entry under 35 U.S.C. §371 and claims priority to International Application No. PCT/US2009/068238, with an International Filing Date of Dec. 16, 2009, for POWDER HOPPER WITH QUIET ZONE, A COMBINATION OF A POWDER HOPPER AND A POWDER SPRAY GUN AND A METHOD OF OPERATING A POWDER HOPPER, which claims priority to U.S. Provisional Patent Application Ser. No. 61/138,246, filed Dec. 17, 2008, for POWDER HOPPER WITH QUIET ZONE, the disclosures of which are all fully incorporated herein by reference.
Filing Document | Filing Date | Country | Kind | 371c Date |
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PCT/US2009/068238 | 12/16/2009 | WO | 00 | 6/16/2011 |
Publishing Document | Publishing Date | Country | Kind |
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WO2010/077936 | 7/8/2010 | WO | A |
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Number | Date | Country | |
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20120021133 A1 | Jan 2012 | US |
Number | Date | Country | |
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61138246 | Dec 2008 | US |