Electrostatic powder coating

Abstract: Electrostatic powder coating apparatus comprises a spray module (8) located within a bight of a conveyor (3) having suspended from it a plurality of articles to be coated with powder prior to heat treatment to convert the powder into an adherent coat of paint or the like. The spray module comprises an impeller (8) able to rotate about a vertical axis and having charged powder projected towards its centre from a stationary nozzle (15) so that vanes on the impeller impart centrifugal force to the powder particles. The impeller and nozzle assembly may be reciprocated vertically so that the sprayed powder traverses the length of the suspended and moving articles. The powder spray nozzle comprises an inner metal tube (43) from which radial projections (44) extend towards a coaxial rod (42), the powder being charged electrostatically on its passage through the annular space between the tube and rod.

Description: This invention relates to apparatus for effecting electrostatic powder coating, in which process an article is first coated with powder by earthing it and spraying it with charged powder. Because of electrostatic attraction, the charged powder gets deposited over the article to be coated. Subsequently the coated article is conveyed or transferred to an oven in which it is heated to cause the powder to melt and cure to form a strong, adherent protective coat. The apparatus requires dry powder to be conveyed to a spray head in fluidised form, electrostatically charged and dispensed from the spray head towards the article. In known coating apparatus (powder spray guns) normally powder is carried to the spray head (gun) by fluidised form by using air, and is dispensed from the spray head by using a deflector, diffuser or other spray pattern shaper. The powder is charged electrostatically by either corona charging, using high tension pointed electrodes, or friction charging, alone or in combinations. The powder particles are carried to the articles under electrostatic field attraction, pneumatic force and their own momentum. The fine powder spray from the spray head, in a defined fan pattern in the plane of the article, coats the article surface. There are various limitations, like the Faraday cage effect from corona charging, chemical formulation of the powder for friction charging. The powder application process can be manual or automatic, using mechanical means like reciprocators, depending on the size and number of articles to be coated in a stipulated period. An alternative to pneumatic powder spraying uses an electrostatic fluidised bed, wherein articles are introduced into a fluidised powder bed, and coating is carried out under electrostatic field only (without the use of air to carry powder to the articles). This process can also be in manual or automated versions. Both the known processes, spray gun using pneumatic pressure, and fluidised bed using pure electrostatic attraction, have their advantages and limitations. However, the pneumatic type is more versatile and is used far more than is the fluidised bed. Pneumatic applications are not suitable for coating small articles as the pneumatic force required for dispersing the powder towards the articles causes strong oscillation of these articles as they are very light in weight. Secondly pneumatic applicators have a limitation of powder throughput, which is 500 g per minute maximum, and that is with very low transfer efficiency. The optimum value for powder throughput per applicator is 200 g per minute so as to coat very large surface areas in a unit time. To obtain high rates of powder application, one has to use large numbers of such pneumatic applicators. In the case of fluidised bed coating, the Faraday case effect is a major limitation for articles of complex shape. A further disadvantage is that the thickness of the coating, and therefore of the final film, varies to an unacceptable extent on articles above about 50 mm in height. GB-A-1 298 063 discloses apparatus for the electrostatic coating of articles with powder according to preamble of claim 1, comprising a spraying head mounted for rotation on a vertical shaft. The disc and cover are electrically charged, and are rotated at high speed. Powder to be sprayed is introduced into the gap between the cover and the disc, and is forced out of a narrow gap between the two in a generally horizontal direction. According to this invention, there is provided apparatus for electrostatic powder coating, having the features of claim 1. The apparatus comprises a spray chamber having in its upper part a conveyor adapted to be driven in an endless path, in which part of the path of the conveyor forms a substantially closed loop, in which a powder spray module is positioned with its substantially vertical axis of rotation lying within the loop, in which the articles to be coated are intended to be suspended from the conveyor in the path of the powder spray, and in which the powder spray module comprises a rotary impeller having positioned closely to it a non-rotatable nozzle assembly adapted to direct a stream of charged powder at the centre of the impeller. The nozzle assembly preferably received fluidised powder through a powder feed tube. The nozzle assembly is preferably fixed to a dielectric cover. The impeller can be rotated at a fixed speed, and reciprocate in a vertical direction at a linear speed selected in accordance with the articles to be coated. The vertical stroke length of the reciprocation can also be varied in accordance with the height of the articles to be coated. This stroke length is preferably at least 50 mm greater than the span of the article. The particles leaving the impeller are dispersed towards the article to be coated by: a) Centrifugal force; b) Aerodynamic force; c) Electrostatic field, and d) momentum a) CENTRIFUGAL FORCE The centrifugal force is imparted to the powder particles by rotation of the impeller. Any slippage in the tangential direction is reduced by radial fins incorporated in the impeller. The charged powder being fed to the rotary impeller gets uniformly ejected substantially radially by centrifugal force without any tangential slippage. This is achieved by providing an upward slant 1. The upper limit for 1 is the angle of repose at which the radial movement will be sluggish thus achieving accumulation of powder and then distribute it uniformly into the plurality of fins. Accordingly 1 is selected well below the angle of repose i.e. around 0 to 30°. The optimum uniform distribution of powder without excessive accumulation is achieved at an angle of about 10 degrees. The number of radial fins z is chosen as a compromise between the Eck recommendations, which produce z = 8.5 Sin B2 1 - d1 d2 = 18 and the Steppenhoff recommendations which give z = 1/3 B2 = 30 so the average preferably chosen in practice is z = (18+30)/2 = 24 where, in these equations, B2 = exit blade angle = 90 deg. d1 = Internal diameter of blade portions d2 = External diameter of blade portions A streamline shape for the radial fins is preferably chosen. The angular speed of these radial fins is imparted to the powder particles and because of centrifugal force these powder particles start travelling radially on the bottom surface of the impeller and achieve a sufficient ejection speed to get deposited over the articles to be coated. b) AERODYNAMIC FORCE The fins on the impeller when rotated eject air radially, which leads to a sub-atmospheric pressure being produced at the centre of the impeller. This in turn creates an axial airflow as shown in the Figure 4 of the accompanying drawings. The air being sucked through the space of annular cross-section between the impeller shaft and the cylindrical cover is used for conveying powder particles towards the articles to be coated. The speed of the air leaving the impeller is adjusted so that it will not impart any major oscillations to small objects but is sufficient to overcome the Faraday cage effect. c) ELECTROSTATIC FORCE The Powder is fed to the impeller through a nozzle assembly. The nozzle assembly constitutes 32 electrodes which are connected to a high-voltage generator generating 100 kV negative voltage which creates an intense electrostatic field. The powder is passed through this intensive electrostatic field and gets charged. This charged powder, when dispersed by the impeller, gets further propelled by electrostatic attraction towards the earthed articles to be coated. In the absence of any external corona-generating electrode, the charged powder gets deposited uniformly on the articles suspectible to Faraday cage effect. d) FORCE IN UPWARD DIRECTION The impeller disc, as shown in Figure 5 of the accompanying drawings, is dished. As the powder slides over the sloping surface under centrifugal force, an upward component of motion is imparted to the powder particles. This upward component helps in applying powder particles to the undersurfaces of articles to be coated. The invention will now be described by way of example with reference to the drawings accompanying this specification wherein salient features are shown and referred to in the following description. In the accompanying drawings: Figure 1 is a diagrammatic plan view of the powder coating apparatus of the present invention for powder coating of small articles; Figure 2 is a side elevation of the apparatus show in Figure 1; Figure 3 is a side elevation of the spray chamber shown-in Figure 2 on a larger scale; Figure 4 is a plan view of the rotary impeller shown in Figures 2 and 3; Figure 5 is a sectional view along line V-V of the impeller shown in Figure 4; Figure 6 is a sectional view of a nozzle assembly used for charging the powder, and Figure 7 is a view, part in section and part in elevation, of the means for suspending and rotating each article to be coated. The apparatus of the present invention comprises a closed spray chamber 2 having in its upper part a conveyor 3 driven by a motor 4. The conveyor 3 forms an endless loop 5, with the articles being loaded on to the conveyor at station 6 and unloaded at station 7. The supports defining the path of the conveyor have been generally omitted from the drawings, for clarity. The powder coating module consists of a rotary impeller 8 driven by a motor 9 through an insulated shaft 10. The motor 9 and the impeller 8 are mounted on a rod 11 of a reciprocating mechanism 12 driven by a motor 13. Extending around shaft 10 is a non-rotatable dielectric sleeve support 14, which is movable vertically with motor 9. On this sleeve 14 is mounted a non-rotatable nozzle assembly 15. High voltage is provided to the nozzle assembly by means of a high voltage cable 16 from a high voltage generator 17. To this nozzle assembly 15 is attached a bank 18 of resistors through another high-voltage cable 19, for selectively discharging any accumulated charge on the nozzle assembly. The powder paint to be sprayed is stored in a fluidised hopper 20 from which the fluidised powder is sucked by an ejector pump 21 and conveyed to the impeller assembly 8 through a pipe 22. The powder is projected at the centre 23 of the impeller 8. As shown in Figure 3, the impeller is dished so that the powder discharge passages 27 slope upwardly and outwardly of the axis of rotation of the impeller, first at angle 1 to the normal to the axis of rotation, and then at a greater angle 2. The powder impacting the impeller gets dispersed in a uniform manner because of centrifugal force and the inclination of the passages 27. The impeller assembly 8 comprises a set of two discs, the upper one 24 as viewed having a plurality of radial fins or septa 25, while the lower disc acts as a cover 26. As shown in Figure 4, the fins 25 preferably have a cross-sectional shape which tapers inwardly with increasing radius, so that they are thinner at the outside of the impeller than they are at their inner ends. The articles 28 to be coated are suspended from links 29 in the conveyor 3 in order to receive uniform powder coats. The excess powder 30 which does not adhere to the articles gets collected in a hopper 31 at the bottom of the chamber 2. The powder gets sucked through a duct 32 with the help of a suction pump 33 powered by a motor 34. The resultant air/powder mixture is fed to a cyclone separator 35. The recovered powder 36 collected at the bottom of the separator housing is sucked by pneumatic ejector pump 37 and is conveyed to a minicyclone separator 38 through a pipe 39, thus separating powder and air again. The separated powder from minicyclone 38 falls into a sifter hopper 40 in which it is sieved and fed back into hopper 20, thus maintaining a closed cycle for powder circulation. Fresh powder to replace that adhering to the coated articles is fed into hopper 20 as desired, by means which do not form part of the subject-matter of this invention and are therefore not described in any greater detail. As shown in Figure 7, each link 29 in the conveyor from which an article is suspended may be caused to rotate as the conveyor moves, thus rotating the article about its centre of gravity to expose fresh surfaces thereof to the impeller as the article is moved around the impeller. This is done by means of a rotary cogwheel 48 carried by link 29. The cogwheel carries a hook 50 from which the article 28 is suspended, and engages a rack 52 extending part way around the path of the conveyor. In this way the cogwheel, hook and article are rotated by movement of the conveyor relative to the rack. It will be observed that the nozzle is non-rotatable yet is capable of reciprocating with the impeller assembly. The impeller is not connected to a high-voltage source, so that its voltage is able to float. The high-tension wire 16 is connected to the nozzle assembly to establish a high electrostatic field between the powder leaving the nozzle and impeller, and the earthed articles to be coated. The dished shape of the impeller and the upwardly-directed discharge passages ensure that the discharged powder particles have a vertical component of movement. This counteracts the force of gravity and assists in depositing the powder on complex surfaces. The nozzle assembly 15 mounted on holder 41 has a conductive pin 45 connected to high-voltage generator 17 by cable 16 and to resistor bank 18 through cable 19. The pin 45 is connected to an inner conductive sleeve 43. The sleeve contains 32 electrode pins 44 distributed at an axial spacing of 10 mm and radially at 90 degree to each other. The conductive sleeve is press fitted into a dielectric nozzle body 46. High voltage is also conducted to electrode stem 42 by means of a pin 47. The 32 electrodes 44, conductive sleeve 43 and electrode stem 42 help to create an intensive radial electrostatic field. The sleeve 43 is preferably mde of polytetrafluoroethylene (PTFE) loaded with graphite to render it conductive. Although the annular space between the sleeve 43 and rod 42 is shown as being in the shape of a hollow cylinder, it may have other cross-sectional shapes. For instance, it could flare out towards its exit end, to reduce the particle speed and therefore to increase the period during which the particles remain in the charging field. The powder being fed to the nozzle assembly 15 passes through powder feed tube 22 and remains in this intensive electrostatic field sufficiently long to get charged thoroughly, thus reducing over-spray. The general arrangement shown in Figures 1, 2 and 3 is to be used for automatic plant for coating small articles. When the same powder coating apparatus is to be used for coating large surface areas, the powder throughput through the impeller can be increased by feeding the powder through multiple nozzle assemblies. The number of nozzles supplying charged powder to the impeller can be selected to suit the amount of powder to be dispersed or deposited in the stipulated time without hampering the powder charging efficiency or the transfer efficiency. Articles of larger size can be coated by increasing the diameter of the conveyor loop, which diameter is proportional to the size of the articles to be powder coated. For depositing charged powder efficiently on articles of greater size and further away from the powder sprayer, the speed of the powder particles near the articles is kept constant by replacing the impeller shown in Figures 3 and 5 by one with a different dish angle 2 and of greater diameter, but having the same number of fins. Utmost care should be taken when increasing the powder throughput of the impeller that the powder concentration in the spray chamber should be kept in the safe powder/air concentration to avoid any explosion hazard. Such safety measures are beyond the scope of this invention and hence are not described herein in any greater detail. It will be seen that the present invention provides a non-pneumatic powder spray apparatus capable of dispensing large amounts of charged powder, thus reducing the number of spray heads where very large surface areas are to be coated, and avoiding strong oscillations, in the case of small particles. It will also be seen that this invention provides apparatus which does not use pneumatic pressure but uses centrifugal force for dispensing the powder particles towards the articles to be coated. Moreover, the articles are carried on a conveyor or like mechanical means circumscribing the powder coating module so that they remain in the powder application area or spray zone for a sufficiently long time, thereby increasing the application flexibility for coating large articles. It will also be seen that this invention provides powder coating apparatus which is more efficient and less complicated for coating large numbers of small articles, or fewer long and thing articles. The apparatus is fully automatic and cost effective compared with known applicators.

Claims: Apparatus for electrostatic powder coating comprising: a spray chamber (2) having in its upper part a conveyor (3) adapted to be driven in an endless path, in which part of the path of the conveyor (3) forms a substantially closed loop (5); and a powder spray module positioned within the loop (5) such that articles suspended from and conveyed by the conveyor (3) are coated by spray from the powder spray module, comprising an impeller (8) rotatable about a substantially vertical axis, having a non-rotatable nozzle assembly (15) for directing a stream of charged powder at the centre (23) of the impeller (8); characterised in that the impeller (8) has an upwardly dished inner surface and a plurality of substantially radial fins (25) for directing charged powder delivered to the rotating impeller (8) upwards as it moves radially outwards. Apparatus according to claim 1, in which the nozzle assembly comprises a tube (46) of dielectric material having on its inner surface a tube (43) of electroconductive material having inwardly-extending projections (44) from its inner face; a central electrode rod (42) spaced radially inwards from the ends of the projections; means for connecting both the inner tube and rod to a source of high voltage, and means (22) for passing into the nozzle assembly powder to be sprayed, the powder being intended to flow axially of the assembly through the annular space between the inner tube and the rod. Apparatus according to claim 2, in which part of the outer surface of the dielectric tube is screw-threaded. Apparatus according to any preceding claim, in which the powder-spray module is adapted to be reciprocated along the axis of rotation. Apparatus according to any preceding claim in which the impeller (8) has an upper part presenting a complementary concave surface adapted to contact the fins (25) to define a plurality of radial and inclined discharge passages (27). Apparatus according to any preceding claim, in which the impeller (8) is secured to one end of a rotary shaft (10) of dielectric material circumscribed by a non-rotatable sleeve (14) supporting the nozzle assembly (15). Apparatus according to any preceding claim, in which there are two or more nozzle assemblies (15) adapted to direct charged powder at the same impeller (8). Apparatus according to claim 7, in which each nozzle assembly is connected to its own powder supply and voltage generator. Apparatus according to claim 6, 7 or 8 in which the or each nozzle assembly (15) is connected to a high-voltage source (17), and to means (18) for electrically discharging the nozzle assemble selectively. Apparatus according to any preceding claim, in which the impeller (8) is driven by a motor (9) mounted on a non-rotatable support (11) which is reciprocable along its length under the action of a motor (13). Apparatus according to claim 10, in which the range of reciprocation of support (11) is adjustable. Apparatus according to any preceding claim, in which the spray chamber (2) is connected to means (33 to 38) for extracting surplus powder from the chamber and recirculating it to the nozzle assembly in a closed path. Apparatus according to any preceding claim , in which means (29) are provided to rotate each article about its centre of gravity as it traverses at least some part of the endless conveyor path. Apparatus as claimed in claim 5 or any claim dependent therefrom, in which the concave inner surface of the impeller (8) includes an inner frustoconical surface of large apex angle, and a contiguous outer frustoconical surface of smaller apex angle.

Inventors: GHAISAS YASHWANT GOPAL, GHAISAS, YASHWANT GOPAL, GHAISAS, YASHWANT GOPAL, 'ANAND TARANG'
Applicants: INTECH EXPORTS
Application year: 1992
Main classification: B05B5
IPC codes: B05B5, B05B15