The present invention relates to film forming equipment.
In order to apply a coating of a uniform thickness to an object, a coating method has been conventionally employed using a spray pattern formed by a coating material sprayed from a spray gun. Layer coating is conducted using film forming equipment comprising an air conditioner, a spray gun, etc., in a manner as shown in, for example,
It is also possible to conduct layer coating by forming the spray pattern 153 by spraying a coating material from the spray gun to an object 152 fixed in the center of the coating booth 151, as shown in
When layer coating is conducted while fixing the spray gun and moving the object, as described above, the layer coating must be started when the object is at a position apart from the spray pattern and continued until the object has completely passed through the spray pattern. In other words, an unduly large space, i.e., (length of the object×2+width of the spray pattern)×(width of the object×2+width of the spray pattern), is necessary for coating.
Similarly, when the layer coating is conducted while fixing the object and moving the spray gun, the layer coating must be started when the spray pattern is at a position apart from the object and continued until the spray pattern has completely passed through the object. In other words, an unduly large space, i.e., (length of the object+width of the spray pattern×2)×(width of the object+width of the spray pattern×2), is necessary for coating. Furthermore, when coating is conducted in such a manner, extra space should be provided between the inner surface of the coating booth and the spray pattern in order to prevent the spray pattern from soiling the coating booth, requiring an even larger space.
The need for such an unduly large space for coating restricts the places in which the film forming equipment can be installed, and much energy is required to regulate the air in the coating booth.
The present invention has been accomplished in order to solve such problems, and provides film forming equipment that can reduce the space necessary for coating.
The object of the present invention can be achieved by film forming equipment comprising an object conveyor for moving an object; a spray gun conveyor for moving a spray gun that sprays a coating material; and a controller for controlling operations of the object conveyor, the spray gun, and the spray gun conveyor, wherein the controller moves the object in a specific direction while spraying a coating material from the spray gun and reciprocates the object so that partial layer coating can be sequentially conducted, and while coating the object, the controller shifts the object and the spray gun while keeping the positions of the object and the spray gun relative to each other constant.
In this film forming equipment, it is preferable that the direction in which the object and the spray gun are shifted be opposite to the direction in which the object subjected to partial layer coating moves.
It is also preferable that the shifts of the object and the spray gun be conducted when the center of spray emitted from the spray gun is positioned substantially in the longitudinal middle of the object in the shifting direction.
It is also preferable that the controller reciprocate the spray gun in a synchronized manner in the direction opposite to the reciprocation direction of the object.
The present invention provides film forming equipment that can reduce the space necessary for coating.
Equipment for forming coating films of the present invention is explained below with reference to the attached drawings.
As shown in
The coating equipment main body 20 is divided from the top to downward into an air supply chamber 21, a coating booth 22, and an exhaust chamber 23, such that the air supply chamber 21 and the coating booth 22 are partitioned from each other by an air supply filter 24, and the coating booth 22 and the exhaust chamber 23 are partitioned from each other by a dust-collecting filter 25.
The air supply chamber 21 comprises a temperature detector and a humidity detector (not shown) for detecting the temperature and humidity of the air supply chamber 21. Examples of temperature detectors are temperature sensors such as thermisters and thermocouples. Humidity sensors such as high polymer film humidity sensors, ceramic humidity sensors, and electrolyte humidity sensors can be used as humidity detectors.
The coating booth 22 comprises a spray gun 30 which functions as a coating material atomizer. A spray gun conveyor, coating material supplier, air control panel, high-voltage generator, cables, etc. (not shown) are connected to the spray gun 30. The spray gun 30 is structured so that its distance from the object 50 can be varied.
Rotational bell-type atomization coating devices, air-atomizing type coating devices, etc., may be used as the spray gun 30. A rotational bell-type atomization coating device comprises a bellcup that rotates at high speed on top of a coating gun, and the coating material discharged through the bellcup is atomized by centrifugal force generated by rotation of the bellcup. A rotational bell-type atomization coating device comprises an air nozzle for emitting shaping air that controls the width of the spray pattern of the coating material by regulating the scattering direction of the atomized particles of the coating material which scatter from the peripheral edge of the bellcup in the radially outward direction. An air-atomizing type coating device comprises nozzles around a coating material outlet for jetting out compressed air (atomized air), and atomizes a coating material by discharging the coating material from the discharge outlet while jetting compressed air from the nozzles. An air-atomizing type coating device usually comprises pattern air nozzles at the periphery of the compressed air nozzles so as to control the width of the spray pattern.
The spray gun conveyor (not shown) is a device that moves the spray gun 30 by receiving commands from the controller described later. Air cylinders, biaxial actuators, etc., are examples of spray gun conveyors. An example of a coating material supplier is a syringe pump wherein a coating material is supplied by a microactuator pressing the piston of a syringe filled with a specific amount of coating material. An air control panel controls the air pressure for rotating the bell, the flow rate of shaping air, and other conditions of the rotational bell-type atomization coating device. A high-voltage generator applies atomized particles which have been made into fine particles by an atomizer to an object 50 using static electricity.
The exhaust chamber 23 comprises an exhauster (not shown) for discharging the air supplied by the air conditioning system 10.
As shown in the sectional view of
The controller is connected to the air conditioning system 10, temperature sensor, humidity sensor, spray gun 30, spray gun conveyor, and object conveyor 41, etc., and controls the operations thereof.
A method for forming a coated film on the object 50 using the film forming equipment 1 of the present embodiment is explained below.
Initially, a predetermined amount of coating material is supplied to the coating material supplier provided with the spray gun 30. An object 50 is then affixed to the conveying jig 42 provided with the conveyor 41 in the coating booth 22. The air conditioning system 10, temperature sensor, humidity sensor, spray gun 30, object conveyor 41, spray gun conveyor, exhauster and controller are operated by turning on the film forming equipment 1.
The air conditioning system 10 supplies air to the air supply chamber 21 via piping 15. While feed backing the signals output from the temperature and humidity sensors provided in the air supply chamber 21, the controller regulates the temperature and humidity of the air supplied from the air conditioning system 10 to be substantially constant. The air whose temperature and humidity has been conditioned is fed to the coating booth 22 via an air supply filter 24.
A coated film is formed by reciprocating the object 50 while spraying a coating material from the spray gun 30 under conditions wherein the temperature and humidity in the coating booth are regulated, and moving the object 50 in a specific direction so that partial layer coating is conducted sequentially, forming a coated film on the object 50. The methods and operations for controlling the object 50 and the spray gun 30 during forming a coated film are described later.
Excess atomized particles of coating material which do not deposit on the object 50 are carried by the air flow supplied from the air conditioning system 10 and sent toward the exhaust chamber 23. In this process, atomized particles of coating material are removed by a dust-collecting filter 25. The air passing through the dust-collecting filter 25 is sent to the exhaust chamber 23, and then discharged via an exhauster.
Methods for controlling the object 50 and the spray gun 30 and operations thereof are explained below with reference to the sectional views of the principal parts of coating booth 22 shown in
Secondly, as shown in
The timing for shifting is set so that the object 50 is shifted when the center of the spray pattern 31 (corresponding to the center of the spray emitted from the spray gun) is positioned substantially in the longitudinal middle of the object 50, in order to sequentially conduct partial coating in the shifting direction for the object 50 (the direction shown by the arrow S). By shifting the object at such a time, enough space is secured to prevent the spray pattern 31 from soiling the inner surface 22a of the coating booth 22, while reducing the space necessary for coating. The timing for shifting may be when the object 50 is traveling in the direction shown by the arrow S, or the object 50 is reciprocating.
The shifting amount of the object 50 and the spray gun is set so that the spray pattern 31 of the coating material emitted from the spray gun does not soil the inner surface of the coating booth.
Thereafter, as shown in
As described above, the film forming equipment 1 of the present embodiment is structured so that the object 50 and the spray gun can be shifted during coating of the object 50 while keeping the relative position of the object 50 and the spray gun constant, and therefore it is possible to reduce the space necessary for coating and to prevent misalignment of the layer coating on the object 50.
Furthermore, due to the reduction of the space necessary for coating, the coating booth 22 can be miniaturized. This reduces the energy necessary for keeping the temperature and humidity in the coating booth 22 constant.
Because the temperature and humidity in the coating booth 22 can be kept constant with reduced energy, a compact air conditioner 10 with a low air-conditioning capability can be used. This achieves further miniaturization of the film forming equipment 1 and reduction of the facility's cost.
Miniaturization of the coating booth 22 also miniaturizes the film forming equipment 1 as a whole, and therefore this enhances the operational efficiency of installation of the film forming equipment 1, and eases constraints in the places in which the film forming equipment can be installed.
The shifting amount of the spray gun is set in a range that the spray pattern 31 of the coating material sprayed from the spray gun does not soil the inner surface 22a of the coating booth 22. Therefore, there is no risk of the coating material adhering to the inner surface 22a, and cleaning or other maintenance steps can be reduced, enhancing the efficiency of the coating process.
One embodiment of the present invention is explained above; however, the scope of the present invention is not limited to this. For example, it is also possible to control the operation of the spray gun conveyor so that the spray gun 30 is reciprocated in a synchronized manner in the direction opposite to that of the object 50. The operations of the object 50 and the spray gun 30 when such a control method is employed are explained below with reference to
When coating is started, as shown in
The operations of the object conveyor and the spray gun are regulated so that when the first half of the round-trip of the object 50 is completed, the first half of the round-trip of the spray gun is also completed, and, as shown in
As shown in
Thereafter, as shown in
By conducting coating while reciprocating the object 50 and the spray gun in directions opposite to each other in a synchronized manner as described above, the distance between the positions at the start and completion of the reciprocation of the object 50 can be reduced. This further reduces the space necessary for coating in the direction of reciprocation of the object 50.
In the present embodiment, the shifting direction of the object 50 and the spray gun 30 is opposite the direction shown by the arrow S; however, the direction is not limited to this as long as the space necessary for coating can be reduced.
In the present embodiment, shifts of the object 50 and the spray gun 30 are conducted when the center of the spray pattern 31 sprayed from the spray gun 30 is at substantially the longitudinal middle of the object 50 in the direction shown by the arrow S; however, the timing for the shift is not limited to this.
In the present embodiment, as shown in
Furthermore, in the present embodiment, the controller controls the operation of the object 50 so that the object 50 is sequentially shifted in the direction shown by the arrow S at the completion of each half of the round-trip of the object 50 as shown in
In the film forming equipment 1 of the present embodiment, it is possible to efficiently form a coated film having substantially the same quality as that coated under the coating conditions of an actual coating step by controlling the particle diameter, concentration and velocity of atomized particles in the spray pattern of coating material sprayed from the spray gun 30, and the relative shift of the spray gun 30 to the object 50.
A method for controlling the particle diameter, concentration and velocity of atomized particles in the spray pattern of coating material sprayed from the spray gun 30 is explained below. The atomized particle diameter is the average particle diameter of the particle swarm of atomized particles of coating material which have been atomized by a spray gun 30 measured at the point of reaching the object 50. The particle diameter can be measured by a laser diffraction particle size analyzer, etc. The atomized particle concentration is the total volume of particles passing through a unit area of the spray pattern. As a simplified method, the atomized particle concentration may be taken to be an average atomized particle concentration calculated from the flow rate of the coating material divided by the area of the sprayed pattern. The pattern area can be easily obtained by spraying the spray pattern onto a plate, etc. The atomized particle velocity is an average particle velocity of the particle swarm in the object 50 direction at the points the atomized particles reach the object 50. The atomized particle velocity can be measured by, for example, a laser Doppler velocimeter, etc.
When a rotational bell-type atomization coating device is used as a spray gun 30, the particle diameter can be easily set by suitably selecting the bellcup diameter of the rotational bell-type atomization coating device, the rotational speed of the bell, and flow rate of the coating material, etc., so that the particle diameter is substantially the same as that in the actual coating operation. The rotational speed of the bell can be controlled, for example, by varying the air pressure for rotating the bell of the rotational bell-type atomization coating device 30. The flow rate of the coating material can be controlled by varying the flow rate of the coating material supplier. Usually, a rotational bell-type atomization coating device used in an actual coating operation has a bellcup diameter of about 60 mmφ to 70 mmφ, its rotational rate is 20000-30000 rpm, and flow rate is 200 to 300 cm3/min; however, when a small bellcup is used in the present embodiment, a particle diameter substantially the same as that in the actual coating operation can be obtained at a flow rate as small as about 20 to 30 cm3/min and a rotational rate of about 10000 rpm.
When an air-atomizing type coating equipment is used as the spray gun 30, the particle diameter can be easily set so as to be substantially the same as that in the actual coating operation by suitably selecting the atomized air flow rate, flow rate of the coating material, etc. The atomized air flow rate can be controlled by reducing the volume of discharged air, etc.
The atomized particle concentration can be easily calculated based on the flow rate of the coating material relative to the pattern area formed on the object 50 by the spray pattern sprayed from the spray gun 30. Therefore, an atomized particle concentration that is substantially the same as that in the actual coating operation can be easily obtained by controlling the flow rate of the coating material. For example, when the width of the coating pattern in an actual operation is to be 30 cm and the flow rate is to be 200 cm3/min, if the width of the coating pattern in the present embodiment is set at 10 cm, the ratio of pattern area of the present embodiment/the actual operation is 1/9. Therefore, the same atomized particle concentration can be obtained by setting the flow rate at 22.2 cm3/min (200×(1/9)). Note that the width of the spray pattern can be easily changed by controlling the angle of the shaping air emitted from the rotational bell-type atomization coating device, and the flow rate thereof.
When a rotational bell-type atomization coating device is used as the spray gun 30, the atomized particle velocity can be easily made substantially the same as that in the actual coating operation by suitably selecting the flow rate of shaping air of the rotational bell-type atomization coating device, the coating distance, etc. Note that when air-atomizing type coating equipment is used as the spray gun 30, by suitably selecting the atomized air flow rate and the coating distance, the atomized particle velocity can be easily made substantially the same as that in the actual coating operation.
As described above, by controlling the flow rate of the coating material of the spray gun 30, coating distance, etc., it is possible to make the atomizing conditions of the coating material (particle diameter, concentration, and velocity of the atomized particles) substantially the same as those of the coating material deposited on an object 50 in an actual coating operation.
A method for controlling the relative movement of the spray gun 30 and the object 50 is explained below. Specifically, the relative movement of the spray gun 30 and the object 50 is controlled based on a coated film formation profile in an actual coating operation determined by the relationship between changes in the coated film formation time and the thickness of the resulting coated film.
The coated film formation profile in an actual coating operation is explained below with reference to
In
The floating time (TF) of the atomized particles as the spray gun 100 passes the micro-area portion 103 a single time can be calculated by dividing the passing length of the micro-area portion 103 L1 by the reciprocating speed. The spray gun 100 is also reciprocated in those portions other than the micro-area portion 103. The duration of the time in which the rotational bell-type atomization coating device 100 passes those portions other than the micro-area portion 103, i.e., the interval TI after the completion of a coating pass in the micro-area portion 103 to the subsequent coating pass, can be calculated by the expression TI=(Reciprocating width L2−Passing distance of the micro-area portion 103 L1)/Reciprocating speed. Therefore, a coated film formation profile as shown in
The controller regulates the object conveyor 41 so as to produce a coated film formation profile determined by the relationship between changes in the coated film formation time and the thickness of the resulting coated film. In other words, the object conveyor 41 is controlled depending on the duration of the object 50's passings, number of times the object 50 passes, and the interval TI between the completion of one coating pass and the start of the subsequent coating pass in the spray pattern of the coating material sprayed from the spray gun 30 so that these agree with those of the coated film formation profile in an actual coating operation. Note that the object conveyor 41 is controlled so that the atomized particles of coating material do not deposit on the object 50 during the interval TI by having the object 50 stand still in or by moving the object 50 to a region in the coating booth where the atomized particles of coating material do not deposit.
This allows the deposition of the atomized particles of the coating material sprayed from the spray gun 30 on the object 50 (film deposition behavior) to be made substantially the same as in an actual coating.
When the actual coating operation is to be conducted by 2-stage coating, i.e., the object is overcoated after previously conducting coating, as shown in the coated film formation profile of
In multi-stage coating wherein the object is coated with a coating material three or more times, it is possible to make the deposition behavior substantially the same as in the actual coating operation by suitably setting the intervals T1 in such a manner that they correspond to the plurality of flash times.
As described above, the film forming equipment 1 of the present embodiment can reproduce coating conditions in an actual coating operation by controlling the temperature and humidity of the air in the coating booth 22, controlling the particle diameter, concentration, and velocity of atomized particles of a coating material spayed from a spray gun 30, and controlling the deposition behavior of the atomized particles deposited on an object 50 so that they are substantially the same as in an actual coating operation. Therefore, a coated film having a finished quality substantially the same as one obtained in an actual coating operation can be formed.
Number | Date | Country | Kind |
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2005-093791 | Mar 2005 | JP | national |
Filing Document | Filing Date | Country | Kind | 371c Date |
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PCT/JP06/05472 | 3/14/2006 | WO | 00 | 8/31/2007 |