The invention relates generally to material application systems, for example but not limited to powder coating material application systems. More particularly, the invention relates to applying powder coating material to surfaces of tubular containers such as cans, for example.
Material application systems are used to apply one or more materials in one or more layers to an object. General examples are powder coating systems, as well as other particulate material application systems such as may be used in the food processing and chemical industries. These are but a few examples of a wide and numerous variety of systems used to apply particulate materials to an object and to which the present invention can be used.
Known supply systems for powder coating materials generally involve a container such as a box or hopper that holds a fresh supply of new or ‘virgin’ powder. This powder is usually fluidized within the hopper, meaning that air is pumped into the powder to produce an almost liquid-like bed of powder. Fluidized powder is typically a rich mixture of powder to air ratio. Often, recovered powder overspray is returned to the supply via a sieve arrangement. A Venturi pump may be used to draw powder through a suction line or tube from the hopper into a feed hose and then to push the powder under positive pressure through the hose to a spray gun.
There are two generally known types of dry particulate material transfer processes, referred to herein as dilute phase and dense phase. Dilute phase systems utilize a substantial quantity of air to push material through one or more hoses from a supply to a spray applicator. A common pump design used in powder coating systems is the Venturi pump which introduces a large volume of air at higher velocity into the powder flow. In order to achieve adequate powder flow rates (in pounds per minute or pounds per hour for example), the components that make up the flow path must be large enough to accommodate the flow with such a high air to material ratio (in other words lean flow) otherwise significant back pressure and other deleterious effects can occur.
Dense phase systems on the other hand are characterized by a high material to air ratio (in other words rich flow). A dense phase pump is described in pending U.S. patent application Ser. No. 10/501,693 filed on Jul. 16, 2004 for PROCESS AND EQUIPMENT FOR THE CONVEYANCE OF POWDERED MATERIAL, the entire disclosure of which is fully incorporated herein by reference, and which is owned by the assignee of the present invention. This pump is characterized in general by a pump chamber that is partially defined by a gas permeable member. Material, such as powder coating material as an example, is drawn into the chamber at one end by gravity and/or negative pressure and is pushed out of the chamber through an opposite end by positive air pressure. This pump design is very effective for transferring material, in part due to the novel arrangement of a gas permeable member forming part of the pump chamber.
An example of a dense phase powder coating system is also described in United States Patent Application Publication No. 2005/0126476 A1 published on Jun. 16, 2005, the entire disclosure of which is fully incorporated herein by reference. This disclosure describes a dense phase pump, as well as other system components including a spray gun, recovery system and control system, all of which may be but need not be used in the exemplary embodiments herein.
Many known material application systems utilize electrostatic charging of the particulate material to improve transfer efficiency. One form of electrostatic charging commonly used with powder coating material is corona charging that involves producing an ionized electric field through which the powder passes. The electrostatic field is produced by a high voltage source connected to a charging electrode that is installed in the electrostatic spray gun. Typically these electrodes are disposed directly within the powder path either within the spray gun nozzle or near the outlet orifice of the spray gun nozzle.
In an exemplary embodiment of one or more of the inventions described herein, a powder coating system may include a powder spray gun having a spray nozzle, a dense phase pump, a supply of powder coating material and a diverter valve. The diverter valve in one embodiment provides a means by which powder flow to the spray gun can be interrupted. In another embodiment, the powder that is diverted from the spray gun may flow in a closed circulation loop back to the supply.
In another exemplary embodiment of one or more of the inventions described herein, a diverter valve is provided that has first and second selectable valve outlets.
In another exemplary embodiment of one or more of the inventions described herein, a diverter valve is provided for a powder coating system that may be used, for example, for spray coating tubular containers.
In another exemplary embodiment of one or more of the inventions described herein, a spray nozzle is provided that produces a conical spray pattern.
Exemplary methods are also presented in this disclosure, including but not limited to a method for spray coating tubular containers, with an example of such a method being embodied in the use of the described apparatus.
These and other aspects and advantages of the present invention will be apparent to those skilled in the art from the following description of the preferred embodiments in view of the accompanying drawings.
While various embodiments are presented herein in the context of a dense phase powder coating system, some aspects and inventions described herein will find application beyond dense phase applications. For example, the concept of a diverter valve as presented herein may be used in dilute phase systems and even in systems that are not powder coating systems. The embodiments described herein for a diverter valve are also exemplary in nature, there being many different ways to achieve the desired functionality described herein. And while we illustrate a specific example of dense phase pump design and other system components, the inventions herein may be used with any number of different types of dense phase pumps, spray guns, hoppers and supplies, recovery systems, spray nozzles and so on. Moreover, while the exemplary embodiments herein disclose corona-type electrostatic coating processes, the inventions herein may also be used in non-electrostatic coating processes, as well as tribo-charge coating processes. Still further, while the exemplary embodiments are presented in the context of applying powder coating material to internal surfaces of a can or tubular container, the inventions may be used for coating any surfaces of a workpiece, either internal or external surfaces as well as for workpieces that are not generally cylindrical bodies, cans or tubular containers.
While the inventions are described and illustrated herein with particular reference to various specific forms and functions of the apparatus and methods thereof, it is to be understood that such illustrations and explanations are intended to be exemplary in nature and should not be construed in a limiting sense. For example, the present invention may be utilized in any material application system for applying powder coating material to a workpiece surface. The surface need not be a can surface, and need not be an interior surface, but may include exterior surfaces, generally planar, curvilinear and other surface geometries, end surfaces, and so on.
By “dense phase” is meant that the air present in the particulate flow is about the same as the amount of air used to fluidize the material at the supply such as a feed hopper. As used herein, “dense phase” and “high density” are used to convey the same idea of a low air volume mode of material flow in a pneumatic conveying system where not all of the material particles are carried in suspension. In such a dense phase system, the material is forced along a flow passage by significantly less air volume, with the material flowing more in the nature of plugs that push each other along the passage, somewhat analogous to pushing the plugs as a piston through the passage. With smaller cross-sectional passages this movement can be effected under lower pressures.
In contrast, a dilute phase flow system is a mode of material flow in a pneumatic conveying system where all the particles are carried in suspension. Conventional dilute phase flow systems introduce a significant quantity of air into the flow stream in order to pump the material from a supply and push it through under positive pressure to the spray application devices. For example, most conventional powder coating spray systems utilize Venturi pumps to draw fluidized powder from a supply into the pump. A Venturi pump by design adds a significant amount of air to the powder stream. Typically, flow air and atomizing air are added to the powder to push the powder under positive pressure through a feed hose and an applicator device. Thus, in a conventional powder coating spray system, the powder is entrained in a high velocity high volume of air, thus necessitating large diameter powder passageways in order to attain usable powder flow rates.
As compared to conventional dilute phase systems having air volume flow rates of about 3 to about 6 cfm (such as with a venturi pump arrangement, for example), the present inventions when used in dense phase systems may operate at about 0.8 to about 1.1 cfm, for example. Thus, powder delivery rates to the spray gun powder inlet may be on the order of about 150 to about 300 grams per minute. These ranges are given as an example for comparing and contrasting dense phase and dilute phase systems, and do not form any limitation on the use of the inventions disclosed herein.
Dense phase versus dilute phase flow can also be thought of as rich versus lean concentration of material in the air stream, such that the ratio of material to air is much higher in a dense phase system. In other words, in a dense phase system the same amount of material per unit time is transiting a cross-section (of a tube for example) of lesser area as compared to a dilute phase flow. For example, in some embodiments of the present invention, the cross-sectional area of a powder feed tube is about one-fourth the area of a feed tube for a conventional venturi type system. For comparable flow of material per unit time then, the material is about four times denser in the air stream as compared to conventional dilute phase systems.
While the described embodiments herein are presented in the context of a dense phase transport system for use in a powder coating material application system, those skilled in the art will readily appreciate that the present invention may be used in many different dry particulate material application systems, including but not limited in any manner to: talc on tires, super-absorbents such as for diapers, food related material such as flour, sugar, salt and so on, desiccants, release agents, and pharmaceuticals. These examples are intended to illustrate but not limit the broad application of the invention for dense phase application of particulate material to objects. The specific design and operation of the material application system selected provides no limitation on the present invention unless and except as otherwise expressly noted herein.
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
One or more spray guns 20 are used to spray coat powder coating material M onto surfaces S of the workpieces W. Typically the work pieces are presented to the spray guns 20 by a conveyor or other mover system C. As an example, the system C may include a conveyor type device that is used in part to load workpieces into a rotatable wheel, perhaps eight or ten at a time. The containers may be held for example by a vacuum chuck and spun for a coating operation. As the wheel rotates, the spray gun is lanced in and out of each container for a coating operation. Many other ways may be used to convey the containers and present them to the spray guns for coating. Each spray gun, more notably the spray nozzle (200) and a forward portion of the spray gun body such as a forward portion of the extension (60) typically are translated or lanced into the interior volume of the container for the spray coating operation. The spraying may occur while the spray nozzle is moving into the container, being withdrawn from the container or both. Those skilled in the art are familiar with many different ways that cans, containers and other workpieces may be presented to a spray gun for a coating operation, and any number of these techniques may be used with the present inventions. In this disclosure, the exemplary workpieces may be cylindrical cans, for example, and more particularly tubular containers that may optionally be closed at one end with a container end E. The ends E may be integrally formed with the container body, such as with a mono-block can, or the container may be a two or three piece container with an end welded or otherwise attached thereto as is well known in the art. In powder coating systems, a fire detection system is often provided when flammable coatings are being used particularly in electrostatic application processes.
Tubular containers, for example aerosol cans, are characterized by comparatively small diameters, for example in the range of about one to three inches, but lengths in the range of about four to twelve inches. These size examples however are not intended as any limitation on the use of the inventions disclosed herein. These narrow long bodies are difficult to uniformly coat the interior surfaces, particularly with Venturi-type spraying systems. This is because the high velocity powder and air volume produce considerable blow back. Venturi systems are also difficult to switch on and off rapidly. As a result, there can be considerable overspray and also low transfer efficiency.
The system 10 in the exemplary embodiment preferably but not necessarily is a dense phase system. Dense phase systems feature lower powder velocities and less air volume. As a consequence, by using dense phase delivery we can improve the transfer efficiency. We have also found that by using dense phase delivery we are able to provide a switching function that operates quickly to turn powder flow on and off to a spray gun without having to interrupt operation of the powder pumps. The faster switching times allow for less overspray and higher throughput. In contrast, a Venturi style dilute phase system is harder to switch because of the high velocity of the powder and the high volume of air. Venturi based systems typically utilize a vacuum source to interrupt powder flow to a spray gun nozzle but response times tend to be slow because of the large amounts and velocity of the air. Therefore, the Venturi pumps typically must be close to the spray guns, for example about four to six feet away. Venturi based systems also have the drawback of needing shorter hose runs between the supply hopper and the pumps because Venturi pumps operate by using high velocity air to suck powder from a hopper. These systems therefore have been characterized by the need to use satellite hoppers positioned closer to the spray guns than the main feed hopper back at the feed center.
Dense phase pumps on the other hand may be positioned near the feed center but can accurately pump the dense phase powder to the spray guns over long hose run lengths, for example sixty feet. This can have the benefit, for example, of facilitating plant layout where the feed centers can be conveniently positioned relative to the can coating lines.
It is common in the powder coating material application industry to refer to the powder applicators as powder spray guns, and with respect to the exemplary embodiments herein we will use the terms applicator and gun interchangeably. However, it is intended that the inventions are applicable to material application devices other than powder spray guns, and hence the more general term applicator may be used to convey the idea that the inventions can be used in many material application systems in addition to powder coating material application systems. Some aspects of the inventions are applicable to electrostatic spray guns as well as non-electrostatic spray guns. The inventions are also not limited by functionality associated with the word “spray”. Although the inventions are especially suited to powder spray application, the pump concepts and methods disclosed herein may find use with other material application techniques beyond just spraying, whether such techniques are referred to as dispensing, discharge, application or other terminology that might be used to describe a particular type of material application device.
As an example, the diverter valve concepts disclosed herein would allow for using the diverter valve itself as a dispensing apparatus. For example, the output from the diverter valve could be used as a shot meter or applicator, or could alternatively be used for dispensing greater quantities during an application process.
The spray guns 20 receive powder from a feed center 22 through an associated spray gun powder feed or supply hose 24. The term “feed center” is used herein to refer to any source of particulate material suitable for use with the present inventions as are well known or later developed. The feed center 22 may include a supply hopper 25 which may serve as a main source of powder coating material in which the powder is fluidized prior to being pumped to the spray guns 20. Powder coating material M may be virgin powder meaning not previously sprayed, or reclaimed powder overspray that is recovered. Virgin powder can be added to the supply hopper either manually from bags or automatically using a transfer pump 25a to transfer powder from a bulk supply 25b, such as a box of new powder, to the supply hopper 25.
The spray guns 20 in this example may be automatic spray guns meaning that the guns are electronically or pneumatically turned on and off for coating operations, as distinguished from being manually triggered. However, those skilled in the art will readily appreciate that some inventive aspects of the disclosure, for example the spray nozzle, may be used with manual spray guns.
The automatic guns 20 typically are mounted on a support that is part of the coating line 12. The gun support (not shown) may be a simple stationary structure, or may be a movable structure, such as an oscillator that can move the guns up and down during a spraying operation, or a gun mover or reciprocator that can move the guns in and out of the collection hood 16 to translate the spray nozzle into and out of the container interior, or a combination thereof. The workpieces may also be spun during a coating operation.
The hood 16 is designed to contain powder overspray, usually by a flow of containment or entrainment air. This air flow that is drawn via the hood 16 may be effected by a powder overspray reclamation or recovery system 26. The recovery system 26 pulls air with entrained powder overspray from the hood 16, such as for example through the duct work 18. The exemplary recovery system 26 includes a cyclone separator 28 to remove much of the powder overspray that is entrained in the containment air from the hood 16. In some systems, the powder overspray is returned to the feed center 22 from the cyclone outlet 30 via a return line 32. A transfer pump 34 may be used if needed to pull recovered powder from the cyclone outlet. In this example, the transfer pump 34 pumps the recovered powder overspray to an optional sieve 36 which then returns the recovered powder to the supply hopper 25. In other systems the powder overspray may either dumped or otherwise reclaimed into a separate receptacle or hopper. The sieve 36 is commonly used as well for sieving the virgin powder from the bulk supply 25b.
There is provided a dense phase pump 38 for each spray gun 20. The design and operation of the pumps may be as described in the applications noted above or may be selected from different available high density pump designs well known to those skilled in the art. Dense phase is preferred for coating lines that are used to coat tubular containers as noted above. Each pump 38 draws powder from the supply hopper 25 via a pump powder inlet hose 39.
With reference to
A control system (not shown) is commonly used with a coating system 10 and may be a conventional control system architecture such as a programmable processor based system or other suitable control circuit. The control system as is well known executes a wide variety of control functions and algorithms, typically through the use of programmable logic and program routines, which are generally indicated in
With reference to
The spray applicator 20 includes a main housing 52 that encloses most of the applicator components. The housing 52 has a powder inlet end 54 and an open outlet end 56. A powder tube 58 extends substantially through the housing 52. The powder tube 58 forms a straight and uninterrupted powder path from an inlet end 54 thereof to about the outlet end 56. The powder tube 58 is preferably a single piece of tubing to minimize joints that can trap powder. This makes the applicator 20 easy to clean and purge internally. A lance or extension 60 is joined to the outlet end 56 of the main housing. The lance 60 may have a selectable length depending on the overall coating system including the geometry of the work piece W and the distance between the outside of the hood 16 to the work pieces. In this manner the main housing 52 and the diverter valve 100 need not be exposed to large quantities of powder overspray. Typical lance 60 lengths may be about ten, twelve or fourteen inches as compared to the main housing 52 which may fourteen inches or so. But longer lance 60 lengths may also be used depending on the can depth, hood size and other factors that affect the decision of how long to extend the lance 60 for a particular spraying machine. Thus the lance 60 is typically elongated compared to the main housing 52 and allows for greater flexibility when designing the coating system 10. The lance 60 may be joined to the main housing 52 by a push fit or friction fit connection, for example.
At the back end of the main housing 52 is a mounting arrangement 62 which may be used to support the spray gun 20 on a support bar 62a of a frame, gun mover, or other suitable structure as is well known in the art. In this example, the mounting arrangement 62 may be realized as a clamp that can be tightened and loosened with a manual adjustment knob 64. The mounting arrangement 62 may further include a bracket 66 that is attached to the back end of the spray gun 20. A diverter valve support arm or flange 68 extends or is attached to the bracket 66 to support the diverter valve 100.
The powder inlet end portion of the powder tube 58, which also serves as the powder inlet to the spray gun 20, includes an inlet end tube connector 70 that receives and retains one end of a diverter valve connector 72 having a tubular end 72a. A seal 74 such as an o-ring, for example, may be used to provide a fluid tight connection between the connector tubular end 72a and the powder tube connector end 70. The tube connector 70 may include a retention mechanism 76 to help grip and retain the tubular end 72a within the tube connector 70. The retention mechanism 76 may be push actuated by pushing the tubular end 72a into the tube connector 70, and also a release member 78 that may be push actuated to release the retention mechanism so that the tubular extension can be easily withdrawn from the tube connector 70. This would allow, for example, easy removal of the diverter valve 100 from the back end of the spray gun 20.
In this manner, the diverter valve 100 has a fluid tight and direct fluid flow path into the back end or powder inlet end 54 of the spray gun 20.
The main housing 52 may support an internal voltage multiplier 80 that receives a low voltage electrical input from an input electrical connector 82. The voltage multiplier 80 is used to provide a high voltage to an electrode tip 84 up at the nozzle end of the spray gun to ionize the air in the region of the powder spray pattern so as to electrostatically charge the powder particles as is well known in the art of corona charging. The electrode tip 84 is electrically connected to a high voltage output of the multiplier 80 by any suitable arrangement such as a high voltage cable or electrode 86, for example. The electrode 86 may be supported inside the lance 60 by any suitable means such as a spider 88 as is well known in the art.
The lance 60 includes a hollow housing 90 that supports the electrode arrangement as well as allows powder to flow from the outlet end of the powder tube outlet end 58a to a spray nozzle 200. The spray nozzle 200 may be threadably, press fit or otherwise attached to the distal end of the lance 60. The spray nozzle will be further described herein below, but includes an integral conical deflector 202 for producing a conical powder spray pattern. The spray nozzle 200 supports the electrode tip 84.
As an introduction to the diverter valve 100, and in view of
In a first operating mode, the diverter valve 100 simply provides a first powder path 108 from the powder inlet 102 to the first selectable diverter valve powder outlet 104 to the associated spray gun 20. In a second operating mode, the diverter valve 100 blocks powder flow to the spray gun and diverts the powder flow to a second powder flow path 110 from the powder inlet 102 to the second selectable diverter valve powder outlet 106 to the feed center 22. As best understood from
The selection of which diverter valve powder outlet is being used at any point in time may be controlled with first and second diverter control valves 114 and 116 as further described below.
As an example, suppose a run speed of 120 cans per minute, or 0.5 seconds per can cycle time. Spraying time may be in the range of about 100-150 milliseconds with the balance of the cycle time being off time. For a Venturi type system it is difficult to immediately stop the high velocity powder flow and air volume and so there is much overspray and less control on the amount of powder transferred to the work piece. This slow shutoff also consumes much of the balance of the half second cycle time. But the diverter valve 100 can have a response time of about 30 milliseconds or less and provides a very precise powder shutoff, which allows more throughput if desired as the system does not need to use the full half second cycle time per can. The more precise on and off powder flow also provides better uniformity of the coating and less overspray.
We refer to the circulating loop as closed because there is no need for adding air or boosting pressure to the powder flow in order to circulate the powder back to the feed center 22. The same pump pressure that delivers powder to the inlet of the diverter valve 100 and the inlet to the spray gun 20 in the first operating mode of the diverter valve 100 is sufficient to return the powder flow to the feed center 22 within a closed powder flow path. A continuous circulating powder flow is thereby achieved in the second operating mode of the diverter valve 100.
In the example of
With reference to
The control mechanisms 114, 116 in
The spool valve 122 is mounted on a cap member 124 that is mounted on the valve body 101 using bolts 126 or other suitable means. The valve body 101 has two pressure cavities 128, 130 machined therein that each closely receive a respective one of the valve members 118, 120. Each valve member 118, 120 may be in the form of single ended bladder with a seal flange 132 that is compressed between the cap 124 and the valve body 101 (see
To reduce overall weight the diverter valve 100 may be made of plastic materials such as molded or machined Tyvar™ for example, and the bladders 118, 120 may be made of rubber or any other suitable flexible material.
With reference to
With reference again to
Still with
In some applications it may be desired to add atomizing air to the dense phase powder before the powder is sprayed through the nozzle 200. In the illustrated embodiment herein and reference to
In another alternative, the atomizing air may be input to the powder flow path at a location within the spray gun body and even up near or at the spray nozzle.
With reference next to
With reference to
The deflector 202 is conical in the sense that it presents a deflector surface 206 (
The nozzle body 204 may include at a back end opposite the deflector 202 a threaded extension 208 which allows the spray nozzle 200 to be attached to the outboard distal end of the lance 60.
The nozzle body 204 includes a hollow first end or bore 212 that defines an internal volume or cavity 214. Powder coating material that enters the spray gun 20 at the powder inlet 70 flows through the powder tube 58 in the housing 52, through the lance 60 and into the nozzle body cavity 214.
Approximately halfway into the nozzle body 204 at the forward end 216 of the bore 212, a series of powder flow passages 218 are formed that extend to an outlet end 220 of the nozzle body 204. These passages 218 are preferably but not necessarily uniformly spaced circumferentially about the nozzle body 204 as best illustrated in
Each powder flow passage 218 forms a discrete flow path through the nozzle body and each is tapered outwardly at an angle α in order to shape a conical spray pattern. The powder will impact the frusto-conical surface 206 which may be formed at an angle β. Typical values for a and may be in the range of about 3° to about 7° and about 20° to about 90° respectively, but the actual values used will depend on the nature of the spray pattern desired.
As best illustrated in
The electrode holder 224 includes a forward portion 224a that preferably is close fit in the center bore 222 and may also be provided with a seal 231 such as an o-ring to prevent powder from flowing backward into the nozzle body 204. This assures as well that powder entering the internal cavity 214 flows out of the nozzle via the powder flow passages 218.
It will be further noted that the front deflector face 230 may also be formed to have a shape other than flat, which the latter may also be used as needed. Typically though it will not be concave, but rather either convex or flat. The front face 230 may be formed at an angle θ in the approximate range of about 5° to about 20° although other angles may be used.
In order to form an integral deflector 202, a groove 232 may be milled out to a depth that exposes the flow passages 218, thereby forming a plurality of outlet holes 234. The milling operation is performed at the angle and with a selected width λ. Powder flow from the spray gun powder tube 58 enters the nozzle body cavity 214 and is distributed into the multiple powder flow paths 218 which may be oriented in a radial pattern about the centerline of the nozzle. As the powder exits each flow path 218 through the respective hole 234, the powder impacts the frusto-conical face 206 of the nozzle deflector 202. This change in direction mechanically shapes the powder into a conical fan pattern and directs the flow of powder to the interior walls of the work piece. The impact with the conical face 206 also helps break up the “fingers” of powder that result from the individual powder flow paths 218, thus creating a more uniform distribution of the powder coating material. The size and shape of the pattern can be varied by the changing the angle of the conical face, a, and the width of the slot, λ.
When the groove 232 is formed, an end surface 236 of the nozzle body 204 is also formed with the plurality of holes 234 radially spaced thereon. Since the nozzle 200 has been machined from a single block of material, the conical deflector 202 is integrally supported on the nozzle body via lands 238 that are part of the end surface 236 between respective pairs of the holes 234.
It will be noted, particularly from
Whether the conical deflector 202 is integrally formed with the nozzle body 204 or separately attached therewith, it will be desirable that there be no obstructive material between the outlet holes 234 and the frusto-conical surface 206, in other words that the groove 232 be circumferentially continuous and open between the end surface 236 of the nozzle body 204 and the frusto-conical face 206 of the conical deflector 202. It will be noted that in the exemplary
The invention has been described with reference to the preferred embodiment. Modifications and alterations will occur to others upon a reading and understanding of this specification and drawings. The invention 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 divisional of pending U.S. Non-Provisional patent application Ser. No. 13/098,640 filed on May 2, 2011, for DENSE PHASE POWDER COATING SYSTEM FOR CONTAINERS, the entire disclosure of which is fully incorporated herein by reference.
Number | Date | Country | |
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Parent | 13098640 | May 2011 | US |
Child | 14692898 | US |