The present invention relates to a surface treatment apparatus.
A conventional surface treatment apparatus includes e.g. a positive electrode member to be electrically connected to a treatment-object article made of metal and having a circumferential groove as an annular treatment-object area in the outer circumferential face thereof, a frame member having an inner circumferential face opposed with a gap relative to the outer circumferential face and the circumferential groove, a non-conductive elastic seal member capable of forming an electrolysis solution path along the annular treatment-object area by sealing the gaps between portions of the outer circumferential face opposed to each other across the annular treatment-object area and the inner circumferential face, a negative electrode member provided in the electrolysis solution path, and an electrolysis solution circulating means for circulating an amount of electrolysis solution along the electrolysis solution path.
With the above-described surface treatment apparatus in operation, as an electrolysis solution path is formed along the annular treatment-object area provided in the outer circumferential face of the treatment-object article and an amount of electrolysis solution is circulated along this electrolysis solution path, a surface treatment such as anodization treatment can be done on the annular treatment-object area in an efficient manner.
In the case of the conventional surface treatment apparatus described above, the frame member is made of a conductive material and this frame member constitutes a negative electrode member having an annular inner circumferential face opposed to the outer circumferential face of the treatment-object article and the annular treatment-object area (circumferential groove) with a gap relative thereto respectively (see, e.g. Patent Document 1).
With the surface treatment apparatus described above, with supply of electricity between and across the positive electrode member and the negative electrode member at the time of a surface treatment, a metal component such as copper dissolved in the electrolysis solution that can easily changed into positive ion tends to deposit and then adhere and accumulate on the surface of the negative electrode member.
Further, with the conventional surface treatment apparatus, because of the provision of the negative electrode member having an annular inner circumferential face, there tends to occur uniform adhesion/accumulation of the deposited metal along the entire inner circumferential face of the negative electrode member. The accumulated deposited metal results not only in decrease in the path cross section area of the electrolysis solution path, but also in hindrance of smooth circulation of the electrolysis solution.
Incidentally, in case the frame member constitutes a positive electrode member having an annular inner circumferential face opposed to the outer circumferential face and the annular treatment-object area of the treatment-object article with a gap relative thereto respectively, a non-metal component such as a chloride or a sulfide dissolved in the electrolysis solution that can easily be changed into negative ion tends to deposit and then adhere/accumulate on the surface of the positive electrode member. Hence, a similar phenomenon tends to occur.
The temperature of the electrolysis solution becomes higher in the vicinity of the surface of the annular treatment-object area due to the heat generated in association with the electrode reaction. And, if smooth circulation of the electrolysis solution is hindered, increase in the temperature of the electrolysis solution tends to occur.
Such increase in the temperature of the electrolysis solution tends to result in burning of coating in the surface treatment when a coating such as an alumite coating is formed in the annular treatment-object area. More particularly, at the time of anodizing treatment, there occurs non-uniformity of electric current distribution or excess of current density, which causes a burning-like outer appearance and may pose difficulty in effecting a plurality of cycles of surface treatment operations with high voltage in repetition with high efficiency.
The present invention has been made in view of the above-described state of the art and its object is to provide a surface treatment apparatus which allows a plurality of cycles of surface treatment operations with high voltage to be effected in repetition with high efficiency.
According to a first characterizing feature of a surface treatment apparatus relating to the present invention, the surface treatment apparatus comprises:
one of a positive electrode member and a negative electrode member to be electrically connected to a treatment-object article made of metal and having an annular treatment-object area in an outer circumferential face thereof;
a frame member having a non-conductive inner circumferential face opposed with a gap to the outer circumferential face and to the annular treatment-object area;
a non-conductive elastic seal member capable of forming an electrolysis solution path along the annular treatment-object area by sealing the gaps between portions of the outer circumferential face opposed to each other across the annular treatment-object area and the inner circumferential face;
the other one of the positive electrode member and the negative electrode member having a bar-like shape with a leading end portion that protrudes into the electrolysis solution path toward the treatment-object article; and
an electrolysis solution circulating means for circulating an amount of electrolysis solution along the electrolysis solution path.
With the above-described arrangement, since the frame member has a non-conductive inner circumferential face that is opposed with a gap to the outer circumferential face and to the annular treatment-object area, there occurs no deposition of a metal component or a non-metal component on the inner circumferential face of the frame member at the time of surface treatment.
Further, since the other one of the positive electrode member and the negative electrode member having a bar-like shape protrudes, the other one of the positive electrode member and the negative electrode member can have a smaller surface area as compared with the convention, so that the adhesion area for a deposited component such as a metal component or a non-metal component to the other one of the positive electrode member and the negative electrode member can be small, and the adhesion strength of the deposited component to the other of the positive electrode component and the negative electrode component can be small.
And, since the other one of the bar-like positive or negative electrode member has its leading end portion that protrudes into the electrolysis solution path toward the treatment-object article, any deposited component of weak adhesion strength which may have adhered and accumulated on the other one of the positive electrode member and the negative electrode member can be gushed away by the impetus of the amount of electrolysis solution that circulates along the electrolysis solution path, thus being removed from the other one of the positive electrode member and the negative electrode member. Hence, there will hardly occur growth of any deposited component accumulated on the other one of the bar-like positive or negative electrode member.
Therefore, smooth circulation of the electrolysis solution in the electrolysis solution path can be maintained for an extended period of time, whereby undesirable increase in the temperature in the vicinity of the surface of the annular treatment-object area can be restricted for an extended period of time, also.
Consequently, the inventive surface treatment apparatus makes it possible to effect a plurality of cycles of surface treatment with high voltage repeatedly in an efficient manner.
According to a second characterizing feature of the present invention, the apparatus comprises a plurality of the other one of the positive electrode members and the negative electrode members having the bar-like shape disposed in distribution along the circumferential direction of the electrolysis solution path.
With the above-described arrangement, as the intensify the electric field generated between the other one of the bar-like positive or negative electrode member and the annular treatment-object area is dispersed along the annular treatment-object area, it becomes easier to form a uniform coating.
According to a third characterizing feature of the present invention, the other one of the positive electrode member and the negative electrode member having the bar-like shape is disposed to protrude, with its longitudinal direction being the direction perpendicular to the outer circumferential face.
With the above-described arrangement, an electric field can be generated in right/left symmetry between the other positive electrode member and the negative electrode member having the bar-like shape and the annular treatment-object area located on the opposed right and left sides relative thereto, so that a uniform coating can be formed easily.
According to a fourth characterizing feature of the present invention, the other one of the positive electrode member and the negative electrode member having the bar-like shape has an outer circumferential face which is formed as a concave/convex face.
With the above-described arrangement, the other bar-like one of the positive electrode member and the negative electrode member can have a large surface area for allowing conduction of a large current therethrough, so that a coating of a desired thickness can be readily formed in an efficient manner in a short time.
According to a fifth characterizing feature of the present invention, the other one of the positive electrode member and the negative electrode member having the bar-like shape has a leading end portion whose shape is a convex face.
With the above-described arrangement, occurrence of electric current concentration at the leading end portion near the treatment-object article can be restricted, so that a spark will hardly occur, and a unifomi coating can be formed easily.
Next, embodiments of the present invention will be described with reference to the accompanying drawings.
More particularly, of three piston ring grooves A1, A2, A3 formed from the top to the skirt portion of the cylindrical piston A, an anodization treatment is effected on an outer circumferential face (“piston outer circumferential face” hereinafter) B of the top side piston ring (compression ring) groove A1.
Hence, the piston ring groove A1 corresponds to “a circumferential groove” as “an annular treatment-object area” included in the piston outer circumferential face B.
The anodization treatment apparatus includes, as shown in
The electrolysis solution tank 1 is made of vinyl chloride or stainless steel and provided in the form of a top end open vessel. And, the tank 1 is configured to receive and collect therein an amount of electrolysis solution that has passed the oxidization treatment section 3 and includes a reflux path 5 for refluxing the solution to the electrolysis solution feeding section 2.
The electrolysis solution feeding section 2 includes a cooling tank 6 for cooling the electrolysis solution refluxed from the electrolysis solution tank 1, a feeding path 7 for feeding an amount of electrolysis solution in the cooling tank 6 to the oxidization treatment section 3, a feeding pump 8 incorporated in the feeding path 7, and a feeding control section 9 for controlling the operation of the feeding pump 8 so that an amount of the electrolysis solution may be fed to the oxidization treatment section 3 at a predetermined timing.
The cooling tank 6 includes a cooler 10 for cooling the collected electrolysis solution, and a cooling control section 12 for controlling the operation of the cooler 10 based on detection information of the electrolysis solution temperature obtained by a temperature sensor 11 so that the electrolysis solution may be cooled to a predetermined temperature.
The electric conduction section 4 is provided for conducting electricity to the oxidization treatment section 3. Preferably, this electric conduction section 4 is provided with a current controlling means so as to be capable of adjusting the electric current density. As such current controlling means, a device comprised of an ammeter, a voltmeter, a rectifier, or the like known in the art can be suitably employed.
The oxidization treatment section 3 includes a first electrode (positive electrode) section 13 and a second electrode (negative electrode) section 14.
The first electrode section 13 includes a positive electrode member 15 made of metal such as copper, stainless steel, etc. having conductivity and a lift device 16 for lifting up/down the positive electrode member 15 relative to the second electrode section 14.
The positive electrode member 15 functions also as a “holder” for holding the piston A, so that the positive electrode member 15 is electrically connected to a positive electrode terminal 4a of the electric conduction section 4, thus being electrically connected to the piston 4 by holding this piston 4.
The holder (positive electrode member) 15 includes, at the lower end thereof, a retention pawl (not shown) engageable/disengageable with/from the inner circumferential face of the piston A. As this engaging pawl is retained to the inner circumferential face of the piston A, the holder 15 holds the piston A under a condition of its axis being aligned along the perpendicular direction and electrically connected.
The second electrode section 14, as shown in
The second electrode section 14, as shown in
The number of the negative electrode members 41 to be provided ranges, preferably, from 4 to 20. In the instant embodiment, fourteen negative electrode members 41 are disposed in distribution along the circumferential direction of the frame member 17.
The frame member 17, the fixing plates 18, 19 and the support base 20 are all formed of non-conductive material (insulating material) such as vinyl chloride resin.
The frame member 17, as shown in
The frame member 17, as shown in
As shown in
The inner side of the inner circumferential face of each flange plate portion 29, 30 (“frame plate inner circumferential face” hereinafter) is formed as the piston insertion hole 25.
Therefore, the frame member 17 includes a frame plate inner circumferential face 31 formed as a “non-conductive annular inner circumferential face” opposed to the piston outer circumferential face B and the piston ring groove A1 along the entire circumferences thereof with a predetermined gap relative thereto respectively.
As shown in
Along the lower fixing plate 19 and the support base 20, there are formed a connecting flow path 33 connected to the feeding path 7 for the electrolysis solution and a discharge hole 34 for discharging an amount of electrolysis solution accumulated within the circular concave face portion 32 to the electrolysis solution tank 1 by natural (gravity) falling.
Therefore, as shown in
On the frame plate inner circumferential face 31 side of the frame member 17, as shown in
Each elastic seal member 40 is formed as an annular shaped non-conductive material (insulating material) such as rubber. As shown in
Each elastic seal member 40 defines a concave portion 42 open toward its outer circumference side and continuously along the entire circumference and has a horizontally oriented U-shaped cross section including upper and lower lateral wall portions 43 and the leading end portion 44 which is brought into the pressed contact against the piston outer circumferential face B.
As shown in
The pressurization mechanism 51 includes an air feeding/discharging device 52 capable of feeding and discharging of pressurized air, a feeding/discharging control section 53 for controlling air feeding/discharging operations of the air feeding/discharging device 52, air feeding/discharging paths 54 communicated to the respective concave portions 42 of the elastic seal members 40 and a pipe joint 56 for joining an air feeding/discharging pipe 55 of the air feeding/discharging device 52 to the air feeding/discharging path 54.
The air feeding/discharging paths 54 are provided at three circumferential portions of the second electrode section 14, and to each air feeding/discharging path 54, the air feeding/discharging pipe 55 is connected, so that for the concave portion 42 of each elastic seal member 40, pressurized air can be fed/discharged to/from the three circumferential positions.
Next, the operations of the pressurization mechanism 51 will be explained.
As shown in
Upon feeding of the pressurized air into the concave portion 42 of the elastic seal member 40, this elastic seal member 40 is elastically extended toward the piston outer circumferential face B and also the leading end portion 44 is elastically bulged and displaced toward the piston outer circumferential face B, whereby this leading end portion 44 is pressed against the piston outer circumferential face B, as shown in
Upon establishment of this pressed contact of the leading end portion 44 of the elastic seal member 40 against the piston outer circumferential face B as shown in
As shown in
The leading end portion 46a of the electrode shaft portion 46 is formed as a convex curved shape having no corners.
Preferably, the plurality of negative electrode members 41 are disposed such that the longitudinal directions (axial directions) thereof be same as the direction perpendicular to the piston outer circumferential face B or be inclined within an angle range of 75 degrees relative to the perpendicular direction.
In the instant embodiment, as shown in
In each negative electrode member 41, the fixing shaft portion 47 is clamped and fixed between the first frame plate 23 and the second frame plate 24, such that the electrode shaft portion 46 protrudes toward the piston A in an electrolysis solution discharge path 38 to be described later as shown in
The connecting shaft portion 48 of each negative electrode member 41, as shown in
The connecting terminal plate 49 is formed as a round annular shape and each connecting shaft portion 48 is electrically connected thereto, as being clamped between the connecting terminal plate 49 and a receiving plate 50 bolt-fixed to the connecting terminal plate 49.
Therefore, for replacement of the negative electrode member 41, the connection between the connecting shaft portion 48 and the connecting terminal plate 49 will be released and then the negative electrode member 41 to be replaced will be withdrawn from between the first frame plate 23 and the second frame plate 24. Thereafter, a new negative electrode member 41 will be inserted between the first frame member 23 and the second frame plate 24 and connected to the connecting terminal plate 49. In this way, the replacement can be carried out easily.
As shown in
The electrolysis solution feeding nozzles 36 are preferably provided in the same number as the number of the negative electrode members 41. In the instant embodiment, fourteen (14) of them are provided as the same number as the negative electrode members 41.
As shown in
Preferably, the electrolysis solution feeding nozzle 36, as shown in
As shown in
Each electrolysis solution feeding nozzle 36 is disposed so as to be capable of feeding the electrolysis solution to the electrolysis solution path 45 along a direction inclined relative to the tangent of the frame plate inner circumferential face 31 such that the electrolysis solution may flow along the electrolysis solution path 45.
Therefore, as the electrolysis solution feeding section 2 having these electrolysis solution feeding nozzles 36 is provided as an “electrolysis solution circulating means” for circulating an amount of electrolysis solution along the electrolysis solution path 45. Hence, as the electrolysis solution is caused to circulate around the surface of the electrode shaft portion 46 as indicated by the arrow (a) in
Since the deposited metal accumulated on the electrode shaft portion 46 can be readily removed, there will hardly occur spark due to contact between the accumulated deposited metal and the piston outer circumferential face B or the circumferential groove A1. Hence, the possibility of melting of formed alumite coating by sparking and resultant deterioration in the treatment quality is lessened.
As shown in
With the anodization treatment apparatus according to the instant embodiment, deposited metal accumulated on the negative electrode member 41 will hardly grow. Hence, the electrode use period until the deposition thickness of deposited metal increases to a thickness requiring replacement of the negative electrode member 41 has become approximately twice as large as that of the conventional anodization treatment apparatus having a negative electrode member having an annular circumferential face opposed with a gap to the outer circumferential face B and the circumferential groove A1 of the piston A.
Further, as shown in Table 1 below, in the case of forming an alumite coating having a coating thickness of 15 μm, in comparison with the conventional anodization treatment apparatus disclosed in Patent Document 1, it was found that the burning voltage becomes 50V or more higher, and by setting the voltage by 30V or more, it became possible to reduce the treatment period by 30% or more.
In the instant embodiment, for providing the electrode shaft portion 46 with a greater surface area, in its outer circumferential face, there is formed a concave/convex face 57 having convex faces and concave faces alternately along the axial direction. The convex faces and the concave faces are formed spirally along the axis of the electrode shaft portion 46.
1. The surface treatment apparatus according to the present invention may be configured to effect surface treatment on a convex (ridge-like) or planar annular treatment-object area included in the outer circumferential face of the treatment-object article.
2. The surface treatment apparatus according to the present invention may include a negative electrode member electrically connected to a metal treatment-object article and a bar-like positive electrode member having a leading end portion protruding toward the treatment-object article into the electrolysis solution path.
3. The surface treatment apparatus according to the present invention may include the other one of the positive electrode member and the negative electrode member which is in the form of a bar having an oval or polygonal cross sectional shape.
4. The surface treatment apparatus according to the present invention may include a single other one of the positive electrode member and the negative electrode member in the form of a bar.
5. In the surface treatment apparatus according to the present invention, the other one of the positive electrode member and the negative electrode member having the bar-like shape may protrude with its longitudinal direction being an oblique direction relative to the outer circumferential face of the treatment-object article.
6. In the surface treatment apparatus according to the present invention, the other one of the positive electrode member and the negative electrode member having the bar-like shape may protrude with its longitudinal direction being an oblique direction toward the upstream side in the flow direction of the electrolysis solution in the electrolysis solution path or being an oblique direction toward the downstream side in the flow direction of the electrolysis solution in the electrolysis solution path.
7. The surface treatment apparatus according to the present invention may be an electroplating treatment apparatus for effecting electroplating treatment as a surface treatment.
Number | Date | Country | Kind |
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2010-121414 | May 2010 | JP | national |
Filing Document | Filing Date | Country | Kind | 371c Date |
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PCT/JP11/54920 | 3/3/2011 | WO | 00 | 9/10/2012 |