JP2007196111A - Rotary atomization type coating apparatus and coating method using the same - Google Patents

Abstract

<P>PROBLEM TO BE SOLVED: To provide a coating method in which a preheating step after a coating step can be omitted in the case of applying a water-based coating liquid. <P>SOLUTION: This invention relates to the coating method for applying the water-based coating material to the object to be coated by using a rotary atomization type coating apparatus, wherein coating is performed by rotating a bell cup of the rotary atomization type coating apparatus at such a circumferential speed that the coating solid content of the water-based coating material becomes a predetermined value or more. <P>COPYRIGHT: (C)2007,JPO&INPIT

Description

  TECHNICAL FIELD The present invention relates to a coating method and a rotary atomizing coating apparatus for spraying a paint onto an object such as an automobile body using a rotary atomizing coating apparatus, and in particular, a preferred rotation applied when spraying a water-based paint onto an automobile body. The present invention relates to a coating method using an atomizing coating apparatus and a rotary atomizing coating apparatus.

  General automobile body coatings are mainly composed of undercoating for the purpose of rust prevention, intermediate coating for the purpose of rust prevention and improvement of finish finish, and top coating for the purpose of appearance finish. It is carried out by the 3-coat 3-bake method.

  Among these, in intermediate coating and top coating (especially 2-coat 1-bake top coating), water dilution type is used instead of conventional organic solvent dilution type thermosetting coating (hereinafter also simply referred to as organic solvent type coating). By using a thermosetting paint (hereinafter also simply referred to as a water-based paint), improvement of the painting work environment and reduction of the wastewater treatment load are achieved.

  These water-based paints, like the organic solvent-based paints, are applied in a diluted state with water in order to lower the viscosity and enhance the coating workability. However, the evaporation rate of the solvent water is higher than that of the organic solvent-based paints. Since it is slow, it is possible to install a preheat zone for forcibly evaporating water in the flash-off process between the coating process and the drying process or between the top coat base coating process and the top coat clear coating process. 1 and so on.

However, the method disclosed in Patent Document 1 requires a space and equipment for the preheating process in the painting booth, which increases the painting booth length and increases the capital investment cost and running cost. There was a problem.
JP 2005-177632 A

  An object of this invention is to provide the coating method and coating apparatus which can abbreviate | omit the preheating process after a coating in painting a water-system coating material.

  In order to achieve the above object, a coating method of the present invention is a method of applying a water-based paint to an object to be coated using a rotary atomizing coating apparatus, and the solid content of the water-based paint is a predetermined value or more. The bell cup of the rotary atomizing coating apparatus is rotated at a peripheral speed to be painted.

  The rotary atomizing coating apparatus of the present invention includes a bell cup that discharges at least a water-based paint onto an object to be coated, and a control unit that controls a peripheral speed of the bell cup, The bell cup is rotated at a peripheral speed at which the solid content of the water-based paint is equal to or greater than a predetermined value.

  Increasing the peripheral speed of the bell cup of the rotary atomizing coating device reduces the coating particle size to be discharged and increases the surface area per unit volume of the paint, thus increasing the contact area with the surrounding air. Evaporation of water, which is a solvent, is promoted during discharge from the substrate and applied to an object. As a result, the solid coating content can be controlled to a predetermined value or more.

  In the present invention, since the bell cup is rotated at a peripheral speed at which the solid content of the water-based paint is equal to or higher than the predetermined value, the pre-heating step after painting may be omitted even for a water-based paint having a low evaporation rate. it can.

BEST MODE FOR CARRYING OUT THE INVENTION

Hereinafter, embodiments of the present invention will be described with reference to the drawings.
First, the outline of the car body painting line will be explained. The white body assembled in the car body line is first carried into the undercoating process. In this undercoating process, the oil and iron powder adhering to the white body are washed, and then surface adjustment and chemical conversion film treatment such as zinc phosphate are applied (the above is the cleaning and pretreatment process), and the undercoating film is further formed Electrodeposition coating is performed. A body coated with an electrodeposition coating material having an epoxy resin such as polyamine resin as a base resin is carried into an electrodeposition drying furnace and baked at, for example, 160 to 180 ° C. for 15 to 30 minutes. An electrodeposition coating film having a thickness of 10 μm to 35 μm is formed on the plate and the bag structure (electrodeposition process).

  The body on which the electrodeposition coating has been formed is sent to the sealing process (including the undercoat process and the stone guard coat process), and vinyl chloride is used for the purpose of rust prevention or sealing at the steel plate joints and steel plate edges. A resin-based sealing material is applied. In the undercoat process, a vinyl chloride resin-based chipping-resistant material is applied to the tire house and the back of the floor, and in the stone guard coat process, a polyester-based or polyurethane-based resin-resistant chipping is applied to the lower part of the body outer plate such as a sill or fender. The material is applied. In addition, these sealing materials and chipping-resistant materials are cured in a dedicated drying furnace or an intermediate coating drying furnace described below.

  The body on which the sealing material and the chipping-resistant material are applied and the electrodeposition coating film is formed on the inner and outer plates is then carried into the intermediate coating process. The intermediate coating process has an intermediate coating booth and an intermediate coating drying furnace. In the intermediate coating booth, an inner panel coating paint corresponding to the outer panel color of the vehicle is applied to the inner panel of the body, and then wet. An intermediate coating is applied to the outer plate part on wet. This body is conveyed to an intermediate coating drying furnace, and an intermediate coating film having a film thickness of 15 μm to 35 μm is formed on the outer plate by passing through the intermediate coating drying furnace at 130 to 150 ° C. for 15 to 30 minutes, for example. A coating film for inner plate coating having a film thickness of 15 μm to 30 μm is formed on the inner plate portion. The inner coating paint and the intermediate coating paint are paints using an acrylic resin, alkyd resin, polyester resin, or the like as a base resin.

  After finishing the intermediate coating, the body is sanded as necessary and then transported to the top coating process. When the outer color is metallic, the top coating base paint and clear paint are applied wet-on-wet. Is done. In the case of a solid-type outer plate color, a top-coated solid paint is applied in the clear coating process. The topcoat base paint, clear paint, and topcoat solid paint are paints that use acrylic resin, alkyd resin, polyester resin, or the like as a base resin.

  Then, the body to which the top coat is applied is conveyed to a top coat drying furnace, where it is baked at, for example, 130 to 150 ° C. for 15 to 30 minutes, thereby forming a top coat film. The film thickness of the top coat base coating film is, for example, 10 μm to 20 μm, the film thickness of the clear coating film is, for example, 15 μm to 30 μm, and the film thickness of the top coating solid coating film is, for example, 15 μm to 35 μm. Finally, the coated body is subjected to an inspection and rework process, and then conveyed to an assembly line on which automobile parts are assembled.

  The above is the outline of the painting line of the automobile body. FIG. 1 shows an example in which the painting method and the painting apparatus of the present invention are applied to the overcoating step 1 among them.

  As shown in the figure, the top-coating step 1 of this example is a preparatory step 11 for removing dust on the inner and outer plates of the body B using a waste cloth or the like, and a top-coating base coating (hereinafter also simply referred to as a base coating). Top coating base coating step 12 for coating, flash-off step 13 for spontaneously evaporating the solvent of the base coating, clear coating step 14 for coating the clear coating, a setting step 15 for standing to evaporate the solvent of the base coating and the clear coating, and And a top coating drying step 16 for simultaneously drying the base coating and the clear coating.

  For the automobile body B in which the top coat is a solid paint, the top coat base coating process is passed as it is, and the top coat solid paint is applied to the inner and outer plates of the car body B in the clear coating process.

  A water-based paint (water dilution type thermosetting paint) is used for the base paint of this example. After this water-based paint is applied wet-on-wet to the inner plate part and outer plate part of the body B in the top coat base coating process 12, water in the solvent contained in this coating film is naturally evaporated in the flash-off process 13. The base coating film is wet-on-wet, and after the clear paint is applied in the overcoat clear coating process 14, the body B is transferred to the overcoat drying process 16 through the setting process 15, and the base paint and the clear paint are baked at the same time.

  In order to carry out the above-described overcoating process 1, in order to carry out the setting process 15 and the overcoating booth 110 for carrying out the preparation process 11, the overcoating base process 12, the flash-off process 13, and the clear coating process 14 as the coating equipment Are provided with a setting chamber 150 and a top coat drying furnace 160 for carrying out the top coat drying step 16.

  The top coat booth 110 is provided with an air conditioner (supply / exhaust device) having a temperature control function and a humidity control function (not shown), and the temperature-controlled air of constant temperature and humidity is constant from the ceiling surface to the floor surface inside the booth. It is supplied by the air volume, prevents paint dust from scattering and stabilizes the coating conditions by making the ambient temperature and humidity constant. The actual temperature and humidity of the coating booth 110 are detected by the sensor 111 and sent to the control device 112 of the rotary atomizing coating apparatus described later.

  In the top coating base coating process 12 in the top coating booth 110, four coating robots 121 to 128 each having a rotary atomizing coating gun (not shown) attached to the hand are arranged on each of the left and right sides, and four coating machines on the entrance side are coated. The base paint is mainly applied to the inner plate portion of the body B, for example, the door opening, by the robots 121 to 124, and the base paint is mainly applied to the outer plate portion of the body B by the four painting robots 125 to 128 on the exit side. The

  The number of painting robots arranged in the top coat base painting step 12 and the work sharing are not limited to this example, and may be set as appropriate according to the work load of the automobile body B that is the object to be coated.

  In particular, in the rotary atomizing coating gun of the coating robots 121 to 128 arranged in the top coating base coating process 12 of this example, the coating solid content immediately after the base coating is applied to the body B is not less than a predetermined value, for example, 70 weights. The peripheral speed of the bell cup is set high so as to be at least%, preferably at least 80% by weight. This will be described later. It should be noted that the peripheral speed of the bell cup is set to be high for a painting gun for painting at least the outer plate of the automobile body B, and the painting gun for painting the inner plate may be set to a high speed as necessary.

  After the top coat base coating step 12, a flash-off step 13 for spontaneously evaporating water contained in the base coating film is provided. The flash-off process 13 in this example is an air conditioner provided in the painting booth 110 while the automobile body B is conveyed by the conveyor, specifically, between the base paint being applied and the clear paint being applied. The water contained in the base coating film is evaporated only by the environmental temperature and humidity (including the ventilation in the painting booth). It is not a process of performing special forced heating or forced air blowing. The passing time of the flash-off process 13 is, for example, 3 to 5 minutes.

  After the flash-off step 13, a clear coating step 14 is provided as shown in FIG. 1, and two right and left coating robots 141 to 144 each having a rotary atomizing type coating gun attached to the hand are provided here. Is arranged. As for these painting robots 141 to 144, the two coating robots 141 and 142 on the entrance side mainly paint the clear paint on the inner plate portion of the body B, for example, the door opening, and the two painting robots on the exit side. The clear paint is mainly applied to the outer plate portion of the body B by 143 and 144. However, the number of coating robots arranged in the clear coating process 14 and the work sharing are not limited to this example, and may be set as appropriate depending on the work load of the automobile body B that is the object to be coated.

  Even if the clear paint to be applied here is a water-based paint, the applied solid content when applied to the body B in the same manner as the base paint described above is, for example, 70% by weight or more, preferably 80% by weight or more. As such, the peripheral speed of the bell cup may be set high, but it is not always necessary to do so.

  The setting chamber 150 in which the setting step 15 is performed has a housing that surrounds the body so that dust does not adhere to the passing body. This setting chamber 150 is a stationary process for evaporating the solvent content of the clear paint and base paint applied in the previous process and preventing the occurrence of cracking problems in the top coat drying process 16. Is not particularly required. However, it is desirable to provide an exhaust device for exhausting the evaporated solvent.

  The topcoat drying furnace 160 for performing the topcoat drying step 16 has a burner for heating the outside air taken up to a predetermined temperature, and a fan and a duct for guiding this hot air to a blower outlet provided in the furnace body (all are The base paint and clear paint are simultaneously baked and cured by this hot air. Generally, a radiation zone using radiant heat is provided on the inlet side to prevent dust and the like from adhering to the undried coating film, and a convection zone for directly blowing hot air from the intermediate area to the outlet side. Is provided.

Next, the coating conditions in the top coat base coating step 12 will be described.
In the 2-coat 1-bake system topcoat, the solid content of the base coating (also referred to as coating NV) immediately after the base coating is applied and immediately before the clear coating is applied is more preferably 70% by weight or more. Is preferably 80% by weight or more from the viewpoint of prevention of cracking defects, suppression of color variation due to poor alignment of the glittering material, or smoothness of the coating film. On the other hand, if the body temperature is too high when spraying the paint, the finished appearance of the coating film such as smoothness will be adversely affected, so the body temperature immediately before the clear paint is applied is about 35 ° C. or less. Is preferred.

  However, in the case of a base paint composed of a water-based paint, the amount of water that evaporates from the wet paint film is applied to the base paint composed of an organic solvent-based paint after the base paint is applied until the clear paint is applied. Compared to less.

  In order to solve this problem, the flash-off time when applying the water-based base paint may be longer than the organic solvent-based base paint or preheat treatment, but the flash-off time may be changed depending on the paint type. The line configuration is extremely complicated and not realistic. Further, when the preheating treatment is added, in addition to the above-described problems, there is a possibility that the body temperature at the time of applying the clear paint becomes high and the smoothness is adversely affected.

  Therefore, in order to satisfy these conditions at the same time, in this example, even when an aqueous base paint having a low solvent evaporation rate is applied, the flash-off process 13 between the top coat base coating process 12 and the clear coating process 14 is not yet performed. The preheat treatment for heating or blowing the dried base coating film is not performed, and moisture is naturally evaporated from the undried base coating film only by the environmental temperature and the environmental air volume of the coating booth 110. Of course, when an organic solvent base paint is applied, the flashoff is also caused by natural evaporation.

  By not forcibly heating the undried base coating film, the body temperature at the time of applying the clear paint can be maintained at an appropriate temperature of around 35 ° C., so that a decrease in smoothness can be suppressed.

  In this example, instead of performing the preheating process in the flash-off process 13, the particle size of the paint when applying the base paint is reduced, and the area in contact with the ambient air is increased while the paint particles are flying. This increases the solid content immediately after the base paint is applied to the body. When this coating solid content becomes high, moisture passes through the flash-off step 13 and water gradually evaporates without performing preheating treatment. The value can be 80% by weight or more.

  Fig. 3 shows changes in solid content of the base coating film (dotted line) when water-based base paint is applied by the conventional method and pre-heat treatment is performed in the flash-off process, and water-based base by the method of this example. It is the graph which compared with the fluctuation | variation (solid line) of the coating-coated solid content of a base coating film, when paint is highly atomized and it paints naturally without performing a preheating process in a flash-off process.

  In the conventional method, the coating NV immediately after applying the water-based base paint is about 40% by weight, and the pre-heating treatment increases the coating NV immediately before applying the clear paint to 80% by weight or more. In the method of this example, the coating NV is increased to nearly 80 wt% by making the water-based base paint highly atomized, and thereafter, only the increase in solid content due to natural evaporation can be handled.

  In order to make the base paint highly fine in the top coat base coating process 12, the peripheral speed of the bell cup of the rotary atomizing type coating apparatus is increased. The paint supplied to the bell cup travels along the inner surface of the bell cup and jumps out of the edge. The coating particle size at this time correlates with the peripheral speed of the bell cup, and the larger the peripheral speed, the more the atomization is promoted. The Since the peripheral speed V of the bell cup is uniquely determined by the rotation speed A and the diameter D of the bell cup (V = ADπ), it can be said that the coating particle diameter correlates with the rotation speed and the diameter of the bell cup. And it has been found that when atomization is promoted by the present inventors, the solid content of coating increases. FIG. 2 is a graph showing a result of verifying the relationship between the peripheral speed of the bell cup and the coating NV of the base coating film immediately before the clear coating under a certain coating booth condition. The peripheral speed of the bell cup is 130 to 270 m / second. It can be seen that the coating NV is strongly correlated in the second range.

  However, the coating conditions of the base paint in the above-described top coat base coating process depend on the material of the base paint and clear paint used, the temperature and humidity in the flash-off process, the transit time, etc. Do.

  That is, if the peripheral speed of the bell cup is set so that the solid content of the base coating immediately before the clear coating is applied is 75 to 90% by weight, both the armpit and smoothness can be obtained without preheating treatment. The quality can be satisfied. Therefore, the natural evaporation characteristics of the flash-off process 13 in the environmental conditions such as the temperature and humidity of the coating booth 110 to be applied are verified, and the bell cup in which the coating NV is within the above appropriate range immediately before the application of the clear paint after the flash-off. Set the peripheral speed.

  Normally, control is performed such that the lower the temperature detected by the temperature / humidity sensor 111 of the painting booth and the higher the humidity, the higher the peripheral speed of the bell cup. The data may be stored in the control device 112 and controlled so that the set value is changed at predetermined intervals such as every day or every several hours.

  As described above, according to the present embodiment, it is possible to suppress the occurrence of wrinkles, color fluctuations, and a decrease in smoothness without performing preheating treatment on the water-based paint.

  It should be noted that the rotation speed of the bell cup can be controlled according to the type of paint so that it is possible to cope with a mixture of a water-based paint vehicle and an organic solvent-based paint vehicle. For example, the control device 112 of the rotary atomizing coating device shown in FIG. 1 takes in data relating to vehicle specifications from a line management device or the like, and the vehicle seated in the top coat base coating process 12 is a water-based paint specification vehicle or an organic solvent-based paint. After determining whether the vehicle is a specification vehicle, for example, in the case of a water-based paint specification vehicle, the rotation speed (circumferential speed) of the bell cup is controlled as described above, and in the case of an organic solvent-based paint specification vehicle, the rotation speed of the bell cup (circumferential speed). ) Can be controlled to be lower than that. In this case, it is desirable to further control the rotation speed of the bell cup in consideration of the temperature and humidity of the coating booth 110.

  Moreover, although embodiment mentioned above is an example which applied the coating method and rotary atomization type coating apparatus which concern on this invention to 2 coat 1 bake coating type topcoat base coating material, the coating method and rotary atomization which concern on this invention are applied. The type coating apparatus can also be applied to the case where an intermediate coating, a top coating solid coating, or a clear coating is used as a water-based coating.

  That is, when a water-based intermediate coating is used, a rotary atomizing coating apparatus is applied to the intermediate coating process, and when applying the water-based intermediate coating, the coating NV is 75% by weight or more, preferably 80%. Set the rotation speed (peripheral speed) of the bell cup so that it becomes more than% by weight. Thereby, even if it does not provide a preheating process between an intermediate-coat coating process and an intermediate-coat drying process, generation | occurrence | production of a crack and a smooth fall can be suppressed simultaneously.

  In addition, when a water-based top-coating solid paint or a water-based clear paint is used, a rotary atomizing coating apparatus is applied to the coating robots 141 to 144 shown in FIG. 1 to apply the water-based top-coating solid paint or water-based clear paint. The rotation speed (peripheral speed) of the bell cup is set so that the coating NV is 70% by weight or more, preferably 80% by weight or more. Thereby, even if it does not provide a preheating process between a top coat coating process and a top coat drying process, generation | occurrence | production of a bran and a fall of smoothness can be suppressed simultaneously.

  The embodiment described above is described in order to facilitate understanding of the present invention, and is not described in order to limit the present invention. Therefore, each element disclosed in the above embodiment is intended to include all design changes and equivalents belonging to the technical scope of the present invention.

  Hereinafter, the present invention will be described based on more specific examples.

Example 1
A test piece with electrodeposition and intermediate coating applied to a steel plate, using an EcoBell M (externally applied bell-type electrostatic coating gun, bell cup diameter 65 mm), a rotating atomizing coating device, and water-based The top coat base paint (Aqua BC-3 manufactured by Nippon Oil & Fats BASF Coatings Co., Ltd., silver color, paint solid content 25% by weight) was applied so that the film thickness was 10 to 15 μm.

  At this time, the paint discharge rate is 100 ml / min, the linear velocity of the gun is 30 m / min, the gun distance is 200 mm, the applied voltage is -80 kV, the displacement width (pitch) during reciprocating coating is 200 mm, and it is repeated twice. The flow rate was 200 liters / minute, the rotation speed of the bell cup was 80000 rpm, and the temperature and humidity of the coating booth were 24 ° C. and 73% RH.

  After the above base paint is applied, the test piece is allowed to stand in the painting booth for 6 minutes, and then an organic solvent-based clear paint (Bellcoat No. 7300 manufactured by Nippon Oil & Fats Co., Ltd.) is made to have a film thickness of 35 ± 5 μm. Painted on. The test piece was allowed to stand in the painting booth for 10 minutes and then placed in an electric furnace at 140 ° C. for 20 minutes to simultaneously cure the base coating and the clear coating.

  The sharpness (PGD value) of the obtained test piece was measured with a sharpness measuring device manufactured by Nissan Motor Co., Ltd., and the color difference ΔE when Comparative Example 1 described above was used as a standard coated plate was measured with a color difference meter manufactured by Nissan Motor Co., Ltd. It was measured. In addition, the solid content of coating after 2 minutes from the application of the base paint in parallel with the production of the test piece and the solid content of the coating film 6 minutes later (immediately before the application of the clear paint) were measured. These results are shown in Table 1.

Example 2
A test piece was prepared and evaluated under the same conditions as in Example 1 except that the rotation speed of the bell cup when applying the water-based base paint was 85000 rpm and the temperature and humidity of the coating booth were 23 ° C. and 80% RH.

<< Comparative Example 1 >>
To the test piece subjected to the same intermediate coating as in Example 1, using the Acumbel 605 manufactured by Sames, which is a rotary atomizing coating device (internally applied bell type electrostatic coating gun, bell cup diameter 70 mm), An aqueous overcoat base paint (Aqua BC-3, silver color, 25% by weight of solid content of paint manufactured by Nippon Oil & Fats BASF Coatings Co., Ltd.) was applied so that the film thickness was 10 to 15 μm.

  The paint discharge rate at this time is 120 ml / min, the linear velocity of the gun is 60 m / min, the gun distance is 200 mm, the applied voltage is -70 kV, the displacement width (pitch) during reciprocating coating is 100 mm, and it is repeated twice. The flow rate was 400 liters / minute for the first time, 600 liters / minute for the second time, the rotation speed of the bell cup was 40000 rpm, and the temperature and humidity of the coating booth were 24 ° C. and 73% RH.

  After applying the above-mentioned base paint, put it in an electric furnace at 70 ° C. and a wind speed of 5 m / sec for 3 minutes, preheat it, remove it from the electric furnace, and leave the test piece in the painting booth for 3 minutes. After that, an organic solvent-based clear paint (Bellcoat No. 7300 manufactured by Nippon Oil & Fats Co., Ltd.) was applied so that the film thickness was 35 ± 5 μm. The test piece was allowed to stand in the painting booth for 10 minutes and then placed in an electric furnace at 140 ° C. for 20 minutes to simultaneously cure the base coating and the clear coating. The obtained test piece was evaluated.

<< Comparative Example 2 >>
A test piece was prepared and evaluated under the same conditions as in Example 1 except that the number of rotations of the bell cup when applying the aqueous base paint was 60000 rpm.

<< Comparative Example 3 >>
A test piece was prepared and evaluated under the same conditions as in Example 1 except that the temperature and humidity of the coating booth when applying the aqueous base paint was 23 ° C. and 80% RH.

<Discussion>
From the results of Example 1 and Comparative Examples 1 and 2, the coating NV immediately before clear coating was subjected to preheating treatment by increasing the rotation speed of the bell cup to 80000 rotations without performing preheating treatment. The content rose to 82% by weight, almost the same as in Example 1, and both the color difference and the sharpness were good.

  In contrast to Example 1, when the temperature and humidity of the coating booth are low and high, the coating NV just before clear coating is not sufficiently high at the same bell cup rotation speed (80000 rpm) as in Comparative Example 3, and the color difference. However, as shown in Example 2, when the rotation speed of the bell cup was increased to 85000 rpm, good results in both color difference and sharpness were obtained.

Example 3
Water-based intermediate coating material (externally applied bell-type electrostatic coating gun, bell cup diameter 65 mm) is applied to a test piece obtained by electrodeposition coating on a steel plate using Dubell's EcoBell M, which is a rotary atomizing coating device. Nippon Oil & Fats BASF Coatings Aqua GX Sealer, paint solid content 50 wt%) was applied to a film thickness of 30 ± 5 μm.

  At this time, the paint discharge rate is 200 ml / min, the linear velocity of the gun is 25 m / min, the gun distance is 200 mm, the applied voltage is -80 kV, the displacement width (pitch) during reciprocating coating is 150 mm, and the shaping air flow rate is 200 liters / min. The rotation speed of the bell cup was 70000 rpm, and the temperature and humidity of the coating booth were 24 ° C. and 73% RH.

  The test piece was allowed to stand in the painting booth for 10 minutes after the intermediate coating was applied, and then placed in an electric furnace at 150 ° C. for 20 minutes to cure the intermediate coating film.

  The sharpness (PGD value) of the obtained test piece was measured with a sharpness measuring device manufactured by Nissan Motor Co., Ltd. In addition, the coating solid content after 2 minutes passed and the coating film solid content after 10 minutes (immediately before putting into an electric furnace) was measured in parallel with preparation of a test piece. These results are shown in Table 2.

<< Comparative Example 4 >>
A test piece subjected to the same electrodeposition treatment as that of Example 3 was subjected to a water atomization using an Accubell 605 (internally applied bell type electrostatic coating gun, bell cup diameter 70 mm) manufactured by Sames, which is a rotary atomizing type coating device. A coating material (Aqua GX sealer manufactured by NOF BASF Coatings Co., Ltd., solid content of paint 50% by weight) was applied so that the film thickness was 30 ± 5 μm.

  At this time, the paint discharge rate is 250 ml / min, the linear velocity of the gun is 40 m / min, the gun distance is 200 mm, the applied voltage is -70 kV, the displacement width (pitch) during reciprocating coating is 200 mm, and the shaping air flow rate is 300 liters / min The rotation speed of the bell cup was 40,000 rpm, and the temperature and humidity of the coating booth were 24 ° C. and 73% RH.

  5 minutes after applying the above-mentioned intermediate coating, put it in an electric furnace at 70 ° C. and a wind speed of 5 m / sec for preheating treatment, and then remove the test piece from the electric furnace for 3 minutes in the painting booth. After placing, it was placed in an electric furnace at 150 ° C. for 20 minutes to cure the intermediate coating film. The obtained test piece was evaluated.

<< Comparative Example 5 >>
A test piece was prepared and evaluated under the same conditions as in Example 3 except that the rotation speed of the bell cup when applying the water-based intermediate coating was changed to 60000 rpm.

<< Comparative Example 6 >>
A test piece was prepared and evaluated under the same conditions as in Example 3 except that the number of rotations of the bell cup when applying the water-based intermediate coating was 80000 rpm.

<Discussion>
From the results of Example 3 and Comparative Examples 4 and 5, the intermediate coat NV immediately before baking was preheated by increasing the rotation speed of the bell cup to 70000 rotations without performing preheat treatment. It rose to 76% by weight, which was almost similar to that of Comparative Example 4, and the sharpness was good.

  Further, it was found that when the rotation speed of the bell cup was made too high as in Comparative Example 6 as compared with Example 3, the coating NV was too large and the sharpness (smoothness) was lowered.

It is process drawing which shows an example of the coating line to which the coating method and rotary atomization type coating apparatus which concern on this invention are applied. It is a graph which shows the relationship between the rotation speed of a bell cup, and coating solid content. It is a graph which shows the fluctuation | variation of the coating solid content with respect to the time passage after coating.

Explanation of symbols

DESCRIPTION OF SYMBOLS 1 ... Top coat process 11 ... Preparatory process 12 ... Top coat base coating process 13 ... Flash off process 14 ... Clear coating process 15 ... Setting process 16 ... Top coat drying process

Claims (11)

A method for applying a water-based paint to an object to be coated using a rotary atomizing coating device, wherein the bell cup of the rotary atomizing-type coating device at a peripheral speed at which the solid content of the water-based paint is equal to or higher than a predetermined value. A painting method characterized by rotating and painting. The coating method according to claim 1, wherein no forced preheating treatment is performed in a flash-off process or a setting process after the water-based paint is applied. The coating method according to claim 1 or 2, wherein the peripheral speed of the bell cup is controlled in accordance with at least one of temperature and humidity of an environment in which the object is coated. The coating method according to claim 1, wherein a peripheral speed of the bell cup is 200 m / sec or more. The water-based paint is a topcoat base paint, and after applying the topcoat base paint, a clear paint is applied wet-on-wet, and then the topcoat base paint and the clear paint are simultaneously baked and cured. 4. The coating method according to any one of 4. The water-based paint is an intermediate paint or a top coat solid paint, and after the intermediate paint or the top coat solid paint is applied, the intermediate paint or the top coat solid paint is baked and cured. The coating method of crab. A bell cup that discharges at least the water-based paint to the object to be coated; and a control unit that controls the peripheral speed of the bell cup, wherein the control unit has a solid content of the water-based paint of a predetermined value or more. A rotary atomizing coating apparatus, wherein the bell cup is rotated at a peripheral speed. And a means for detecting at least one of a temperature and a humidity of an environment in which the article is coated, and the control means is configured to detect the circumference of the bell cup according to at least one of the temperature or the humidity detected by the detection means. 8. The rotary atomizing coating apparatus according to claim 7, wherein the speed is controlled. The rotary atomizing coating apparatus according to claim 7 or 8, wherein the control means controls the peripheral speed of the bell cup to 200 m / sec or more. The rotary atomizing coating apparatus according to claim 7, wherein the water-based paint is a top coat base paint, an intermediate coat paint, or a top coat solid paint. A means for detecting whether a paint to be applied to the object is a water-based paint or a paint other than a water-based paint, and the control means is configured to detect the paint according to the type of paint detected by the detection means. The rotary atomizing coating apparatus according to any one of claims 7 to 10, wherein the peripheral speed of the bell cup is controlled.

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