Electrostatic coater
09943864 ยท 2018-04-17
Assignee
Inventors
Cpc classification
B05B5/0407
PERFORMING OPERATIONS; TRANSPORTING
B05B5/0426
PERFORMING OPERATIONS; TRANSPORTING
B05B5/03
PERFORMING OPERATIONS; TRANSPORTING
International classification
B05B3/10
PERFORMING OPERATIONS; TRANSPORTING
B05B5/04
PERFORMING OPERATIONS; TRANSPORTING
Abstract
An electrostatic coater capable of realizing high-level coating quality is provided. Shaping air SA, discharged from an air port, is directed radially outward. An elevation angle thereof preferably ranges from 10 to 20 degrees. Further, the shaping air SA is a flow in a state of being twisted in a direction opposite to the rotation direction R of a bell cup. The twisting angle about the axis O of the bell cup preferably ranges from 38 to 60 degrees. A liquid thread of paint extends radially outward from the outer peripheral edge of the bell cup, and the paint separated from the tip end thereof becomes a particle. It is preferable that the shaping air SA collides with the paint particle at a point P where the momentum of the paint particle is decreased of the paint particle is decreased.
Claims
1. An electrostatic coater comprising: a rotary atomizing head configured to rotate in a first direction and scatter paint radially outward to atomize the paint; and air ports positioned behind an outer peripheral edge of the rotary atomizing head, the air ports being configured to discharge shaping air to a front, wherein the air ports consist of only a plurality of air ports arranged at equal intervals on a single circumference coaxial with a rotational center axis of the rotary atomizing head; wherein the air ports direct the shaping air radially outward, the shaping air is directed such that part of secondary-dispersed air of the shaping air becomes air accompanying a liquid thread of paint extending from the rotary atomizing head, and that the shaping air collides with a paint particle separated from the liquid thread of the paint extending radially outward from the rotary atomizing head; wherein the shaping air collides with the paint particle at a point apart radially outward from a tip end of the liquid thread of paint; wherein the shaping air collides with the paint particle at a vertical separation distance between 5.6 mm and 43.2 mm from the outer peripheral edge of the rotary atomizing head; wherein the shaping air discharged from the air ports is twisted in a second direction opposite the first direction of the rotary atomizing head.
2. The electrostatic coater according to claim 1, wherein an elevation angle of the shaping air directed radially outward ranges from 10 to 20 degrees, and wherein the elevation angle is configured to direct the shaping air to collide with the paint particle after the paint particle separates from a liquid thread of paint.
3. The electrostatic coater according to claim 2, wherein a twisted angle of the shaping air about the rotational center axis of the rotary atomizing head ranges from 38 to 60 degrees.
4. The electrostatic coater according to claim 1, wherein the electrostatic coater is applicable to metallic coating.
5. The electrostatic coater according to claim 1, wherein the shaping air from neighboring air ports is configured to overlap while spraying.
Description
BRIEF DESCRIPTION OF THE DRAWINGS
(1)
(2)
(3)
(4)
(5)
(6)
(7)
(8)
(9)
(10)
(11)
(12)
(13)
DETAILED DESCRIPTION OF THE PRESENT INVENTION
Embodiments
(14) Hereinafter, preferred embodiments of the present invention will be described based on the accompanying drawings.
(15) Referring to
(16) Referring to
(17) As means for causing the shaping air SA to be in a twisted state, it is acceptable to adopt a configuration of tilting a shaping 16 communicating to the air ports 12 in a direction opposite to the rotation direction R of the bell cup 10 about the axis O of the bell cup 10 (
(18) Referring to
(19) The paint extends out as the liquid thread 20 from the outer peripheral edge 10b of the rotating bell cup 10. Then, the paint 22 separate from the tip end of the liquid thread 20. The paint particles 22, separated from the liquid thread 20, fly radially outward by the centrifugal force, but starts decelerating by the friction with the air. That is, the momentum of the paint particle 22 is decreased. Reference character A in
(20) In the electrostatic coater of the embodiment, the momentum of the paint 22 start decreasing at the starting point of the region B (
(21) In order to confirm the effect of the present invention, an experiment was carried out under the following conditions:
(22) (1) Diameter of the bell cup 10: 77 mm
(23) (2) Horizontal separation distance L(b, a) between the collision point P and the air port 12: 19.42 mm (
(24) (3) Vertical separation distance Hsa between the point P where the shaping air SA collides with the paint particle 22, and the air port 12: 14.16 mm (
(25) (4) Horizontal separation distance Lh between the outer peripheral edge 10b of the bell cup 10 and the collision point P: 9.42 mm (
(26) (5) Vertical separation distance Lv between the outer peripheral edge 10b of the bell cup 10 and the collision point P: 17 mm (
(27) (6) Outward elevation of the shaping air SA (
(28) (7) Twisted angle of the shaping air SA (
(29) (8) Pitch between adjacent air ports 12 and 12: 8.5 mm when converted into a linear distance.
(30) Here, the diameter of the air port 12 is 0.8 mm and the number of air ports 12 is thirty (30).
(31) It should be noted that a virtual line in
(32) As a comparative example, experimental results were collected using a conventional electrostatic coater of a rotary atomization type. The coating conditions using a conventional electrostatic coater were as follows:
(33) (1) Diameter of a bell cup: 77 mm;
(34) (2) Horizontal separation distance L(b, a) between the outer peripheral edge of the bell cup and an air port: 11 mm;
(35) (3) Shaping air was a flow parallel to the axis of the bell cup when viewed laterally;
(36) (4) Shaping air was directed to a point which is 2 mm radially outward from the outer peripheral edge of the bell cup;
(37) (5) Shaping air was a flow in a twisted state in a direction opposite to the rotation direction of the bell cup about the axis of the bell cup;
(38) (6) Twisted angle of the shaping air: 40.
(39) Metallic coating was carried out using the conventional electrostatic coater and the electrostatic coater of the embodiment. The experimental results were as shown below.
(40) TABLE-US-00001 TABLE 1 Metallic coating Separation distance Rotating Paint Flow rate between speed of discharge of shaping workpiece Coating bell cup amount air (Nl/ and coater efficiency (rpm) (cc/min.) min.) (mm) (%) Conven- 40,000 150 600 250 86.10 tional example embodiment 40,000 150 400 200 89.70
(41) From the above-described experimental results, it was found that the coating efficiency of the embodiment was improved. Further, regarding the coating NV value (%), a good result was obtained that it was 33.5% in the case of using the electrostatic coater of the embodiment, while it was 25.8% in the case of using the conventional electrostatic coater. Regarding evaluation of the coating NV value (%), Patent Literature 6 should be referred to.
(42)
(43) Considering the grounds thereof, it can be said as follows when the conventional example and the embodiment are compared.
(44) As is well known, coating is performed while moving the electrostatic coater. The moving direction is shown by the arrows in
(45) As metallic chips (aluminum flakes) in the metallic paint have larger mass than that of a resin component, a collision speed of the metallic chip to the workpiece surface is relatively fast. On the workpiece surface, the surfaces around aluminum flakes are covered with the relatively large paint particles 22b due to the phenomenon described with reference to
(46)
(47) The airflow of the secondary-dispersed shaping air SA becomes a state accompanying the liquid thread 20 extending radially outward from the outer peripheral edge 10b of the bell cup 10. It can be expected that the airflow of the secondary-dispersed shaping air SA acts on the liquid thread 20 extending radially outward so as to allow the liquid thread 20 to further extend radially outward. As the length of the liquid thread 20 becomes longer, the cross-sectional area of the tip end portion thereof becomes smaller. Consequently, the paint particle 22, generated by separating from the tip end of the liquid thread 20, becomes smaller. This means that further micronization of the paint is realized by the airflow of the secondary-dispersed shaping air SA.
(48) Referring to
(49) This is also clear from the photograph of
(50) As other embodiments, modifications of the above-described embodiment were experimentally produced and tested. As a result, substantially the same effects as those of the above-described embodiment could be obtained. The specifications of the other embodiment s are as described below.
Second Embodiment
(51) (1) Diameter of the bell cup 10: 50 mm
(52) (2) Horizontal separation distance L(b, a) between the collision point P and the air port 12: 15.1 mm
(53) (3) Vertical separation distance Hsa between the point P where the shaping air SA collides with the paint particle 22, and the air port 12: 2.7 mm
(54) (4) Horizontal separation distance Lh between the outer peripheral edge 10b of the bell cup 10 and the collision point P: 5.1 mm
(55) (5) Vertical separation distance Lv between the outer peripheral edge 10b of the bell cup 10 and the collision point P: 5.6 mm
(56) (6) Outward elevation of the shaping air SA: 5
(57) (7) Twisted angle of the shaping air SA: 45
(58) (8) Pitch between adjacent air ports 12 and 12: 3.8 mm when converted into a linear distance
(59) Here, the diameter of the air port 12 is 0.8 mm and the number of air ports 12 is forty five (45).
Third Embodiment
(60) (1) Diameter of the bell cup 10: 40 mm
(61) (2) Horizontal separation distance L(b, a) between the collision point P and the air port 12: 37 mm
(62) (3) Vertical separation distance Hsa between the point P where the shaping air SA collides with the paint particle 22, and the air port 12: 40.5 mm
(63) (4) Horizontal separation distance Lh between the outer peripheral edge 10b of the bell cup 10 and the collision point P: 26 mm
(64) (5) Vertical separation distance Lv between the outer peripheral edge 10b of the bell cup 10 and the collision point P: 42.2 mm
(65) (6) Outward elevation of the shaping air SA: 15
(66) (7) Twisted angle of the shaping air SA: 55
(67) (8) Pitch between adjacent air ports 12 and 12: 3.8 mm when converted into a linear distance
(68) Here, the diameter of the air port 12 is 1 mm and the number of air ports 12 is thirty six (36).
Fourth Embodiment
(69) (1) Diameter of the bell cup 10: 40 mm
(70) (2) Horizontal separation distance L(b, a) between the collision point P and the air port 12: 37.3 mm
(71) (3) Vertical separation distance Hsa between the point P where the shaping air SA collides with the paint particle 22, and the air port 12: 40.7 mm
(72) (4) Horizontal separation distance Lh between the outer peripheral edge 10b of the bell cup 10 and the collision point P: 26.3 mm
(73) (5) Vertical separation distance Lv between the outer peripheral edge 10b of the bell cup 10 and the collision point P: 42.7 mm
(74) (6) Outward elevation of the shaping air SA: 15
(75) (7) Twisted angle of the shaping air SA: 55
(76) (8) Pitch between adjacent air ports 12 and 12: 3.8 mm when converted into a linear distance
(77) Here, the diameter of the air port 12 is 1 mm and the number of air ports 12 is thirty six (36).
Fifth Embodiment
(78) (1) Diameter of the bell cup 10: 40 mm
(79) (2) Horizontal separation distance L(b, a) between the collision point P and the air port 12: 37.6 mm
(80) (3) Vertical separation distance Hsa between the point P where the shaping air SA collides with the paint particle 22, and the air port 12: 40.7 mm
(81) (4) Horizontal separation distance Lh between the outer peripheral edge 10b of the bell cup 10 and the collision point P: 26.6 mm
(82) (5) Vertical separation distance Lv between the outer peripheral edge 10b of the bell cup 10 and the collision point P: 43.2 mm
(83) (6) Outward elevation of the shaping air SA: 15
(84) (7) Twisted angle of the shaping air SA: 55
(85) (8) Pitch between adjacent air ports 12 and 12: 3.9 mm when converted into a linear distance
(86) Here, the diameter of the air port 12 is 1 mm and the number of air ports 12 is thirty six (36).
REFERENCE SIGNS LIST
(87) 10 Rotary atomizing head included in coater of embodiment (bell cup) O Axis of bell cup 10a Recessed front surface of bell cup 10b Outer peripheral edge of bell cup 12 Air port which discharges shaping air SA Shaping air Radially outward elevation angle of shaping air Twisted angle of shaping air P Point where shaping air collides with paint particles L(b, a) Horizontal separation distance (between collision point P and air port) Hsa Vertical separation distance between air port and collision point Lh Horizontal separation distance between outer peripheral edge of bell cup and collision point Lv Vertical separation distance between outer peripheral edge of bell cup and collision point 20 Liquid thread of paint 22 Paint particle