EP2791397A1 - Beschichtungsanlage und verfahren zum beschichten von werkstücken - Google Patents
Beschichtungsanlage und verfahren zum beschichten von werkstückenInfo
- Publication number
- EP2791397A1 EP2791397A1 EP12795435.2A EP12795435A EP2791397A1 EP 2791397 A1 EP2791397 A1 EP 2791397A1 EP 12795435 A EP12795435 A EP 12795435A EP 2791397 A1 EP2791397 A1 EP 2791397A1
- Authority
- EP
- European Patent Office
- Prior art keywords
- coating
- electrode
- power conversion
- workpieces
- current
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Granted
Links
- 238000000576 coating method Methods 0.000 title claims abstract description 128
- 239000011248 coating agent Substances 0.000 title claims abstract description 124
- 238000000034 method Methods 0.000 title claims description 10
- 238000006243 chemical reaction Methods 0.000 claims abstract description 129
- 238000000502 dialysis Methods 0.000 claims description 48
- 238000002955 isolation Methods 0.000 claims description 23
- 238000009434 installation Methods 0.000 claims description 17
- 238000009499 grossing Methods 0.000 claims description 10
- 230000001105 regulatory effect Effects 0.000 claims description 6
- 230000001276 controlling effect Effects 0.000 claims description 4
- 230000001788 irregular Effects 0.000 claims description 4
- 238000007654 immersion Methods 0.000 description 11
- 230000002349 favourable effect Effects 0.000 description 3
- 239000000463 material Substances 0.000 description 2
- 238000010276 construction Methods 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 230000002950 deficient Effects 0.000 description 1
- 238000007598 dipping method Methods 0.000 description 1
- 230000005684 electric field Effects 0.000 description 1
- 238000004070 electrodeposition Methods 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 239000003973 paint Substances 0.000 description 1
- 238000010422 painting Methods 0.000 description 1
- 239000004065 semiconductor Substances 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25D—PROCESSES FOR THE ELECTROLYTIC OR ELECTROPHORETIC PRODUCTION OF COATINGS; ELECTROFORMING; APPARATUS THEREFOR
- C25D5/00—Electroplating characterised by the process; Pretreatment or after-treatment of workpieces
- C25D5/18—Electroplating using modulated, pulsed or reversing current
-
- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25D—PROCESSES FOR THE ELECTROLYTIC OR ELECTROPHORETIC PRODUCTION OF COATINGS; ELECTROFORMING; APPARATUS THEREFOR
- C25D13/00—Electrophoretic coating characterised by the process
- C25D13/22—Servicing or operating apparatus or multistep processes
-
- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25D—PROCESSES FOR THE ELECTROLYTIC OR ELECTROPHORETIC PRODUCTION OF COATINGS; ELECTROFORMING; APPARATUS THEREFOR
- C25D17/00—Constructional parts, or assemblies thereof, of cells for electrolytic coating
-
- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25D—PROCESSES FOR THE ELECTROLYTIC OR ELECTROPHORETIC PRODUCTION OF COATINGS; ELECTROFORMING; APPARATUS THEREFOR
- C25D21/00—Processes for servicing or operating cells for electrolytic coating
- C25D21/12—Process control or regulation
Definitions
- the present invention relates to a coating machine for coating workpieces, which comprises a dip tank into which the workpieces for coating the same can be introduced, a power conversion system for providing a coating current which is passable for coating the workpieces through the dip tank, and an electrode which is in the immersion basin is arrangeable and which is electrically connected to the power conversion system comprises.
- Such a coating system is for example from the
- the present invention has for its object to provide a coating system which is flexible and reliable operable.
- the power conversion system comprises a power conversion unit comprising a power switch and an isolating transformer, the circuit breaker on the input side connected to a supply current source and the output side connected to the isolation transformer and wherein the isolation transformer on the input side with the circuit breaker and the output side an electrode is connected.
- the power conversion system includes a power conversion unit that includes a power switch and an isolation transformer
- the power conversion system is flexible in use.
- a plurality of power conversion units are provided, each comprising a power switch and an input side connected to the power switch isolation transformer.
- current in this specification and the appended claims is meant an electric current.
- connection means both direct and indirect electrical connection. It may be provided in an indirect connection, that between two interconnected or connectable elements or components, further elements or components are arranged.
- Circuit breaker from a supply current of the supply current source, a predeterminable coating flow for supplying to an electrode can be generated.
- a current strength of the coating current can be set by means of the circuit breaker.
- the circuit breaker may be galvanically isolated from the electrode.
- the supply current source is galvanically isolated from the electrode by means of the isolation transformer.
- the power switch comprises a power semiconductor.
- Insulated Gate Bi-polar transistor includes. This allows a particularly reliable and low-loss operation of the circuit breaker and thus the power conversion system.
- the current conversion unit preferably comprises a rectification device and / or smoothing device, which can be connected on the input side to the supply current source and connected on the output side to the power switch. In this way, the power conversion unit AC power can be supplied, which can be converted by means of the rectification device and / or smoothing device for providing the same to the power switch in a DC current.
- the current conversion unit comprises a rectification device and / or smoothing device, which is connected on the input side to the isolating transformer and on the output side to an electrode.
- the high-frequency square wave signal generated by means of the circuit breaker can be smoothed particularly easily for a uniform application of coating current to the electrode.
- the current conversion unit comprises a rectification device and / or smoothing device, by means of which a three-phase alternating current of the supply current source for generating a direct current with low ripple is convertible.
- the power conversion system comprises at least two substantially identically designed power conversion units.
- the power conversion units are designed as modules and are thus in particular self-contained, interchangeable and / or functionally independent functional units of the power conversion system. It may be advantageous if the coating system comprises at least two current conversion units, which are electrically connected to one electrode.
- the coating system comprises at least two current conversion units, which are assigned to each other different electrode groups.
- at least two electrode groups can be controlled and / or regulated independently of one another by means of two different current conversion units.
- each electrode is assigned a separate power conversion unit. In this way, a particularly flexible control of the electrodes can be carried out in the dip tank.
- a plurality of coating areas are preferably formed.
- a plurality of coating regions are arranged one above the other in the vertical direction.
- a plurality of coating regions are arranged one behind the other in a conveying direction of the workpieces.
- Each coating area is preferably assigned an electrode, in particular an electrode group.
- An electrode group may include one or more electrodes.
- an electrode is designed as a dialysis cell.
- an electrode is substantially plate-shaped, cylindrical or semi-cylindrical.
- an electrode as a flat, for example, plate-shaped, a semicircular, for example, half-cylindrical shell-shaped, or as a round, for example cylindrical, dialysis cell is formed.
- the coating system preferably comprises a control device for controlling and / or regulating the power conversion system.
- control device for controlling and / or regulating a plurality of power conversion units of the
- control device By means of the control device are preferably a plurality of power conversion units, which are assigned to each other different electrode groups, substantially independently controllable and / or controllable.
- a targeted spatial power distribution in the dip tank can be realized.
- a plurality of current conversion units which are assigned to different electrode groups, can be coordinated with one another such that the current intensity and / or a spatial distribution of the coating current to adapt it to the geometry of the workpieces and / or to a conveying path Workpieces and / or to compensate for an irregular function of a power conversion unit are selectively influenced.
- an “irregular function" of a power conversion unit is in particular a defect or a total failure of the power conversion unit to understand. Furthermore, an “irregular function” is present if a coating current provided by means of a current conversion unit falls below a predetermined value, in particular a predetermined current intensity. It can be advantageous if an electrode, which is electrically connected to the current conversion unit, is an anode. The workpieces then preferably form cathodes.
- the electrode which is electrically connected to the power conversion unit, is in particular a stationary, spatially fixedly arranged in the dip tank electrode, in particular anode.
- all electrodes which are electrically connected to power conversion units are electrically connected to power conversion units, stationary electrodes, in particular anodes.
- the electrode which is electrically connected to a current conversion unit, is a cathode.
- the cathode may then be a stationary electrode in the dip tank or a workpiece.
- the coating system according to the invention is particularly suitable for use in a combination of a supply current source and a coating system.
- the present invention therefore also relates to a combination of a supply current source and a coating system.
- the circuit breaker of a power conversion unit of the coating system is connected or connected on the input side to the supply current source without galvanic isolation.
- the power switch of the power conversion unit by means of an electrical line directly to a three-phase AC supply line of the supply current source is connectable.
- the necessary electrical isolation between the supply current source and an electrode is then preferably only by the isolation transformer, which is connected on the input side to the circuit breaker and the output side to an electrode.
- the combination of a supply current source and a coating system preferably also has the features and / or advantages described above in connection with the coating system according to the invention.
- the present invention has the further object of providing a method for coating workpieces, which can be carried out flexibly and reliably, in particular by means of the coating system according to the invention and / or the combination of a coating system and a supply current source according to the invention.
- the power switch is connected on the input side to a supply current source and on the output side to the isolating transformer, and
- the isolating transformer being connected on the input side to the power switch and on the output side to an electrode arranged in the dip tank;
- the method according to the invention for coating workpieces preferably has the features and / or advantages described above in connection with the coating system according to the invention and / or with the combination of a supply current source and a coating system according to the invention.
- the current intensity of the coating current is adjusted by means of the circuit breaker of the power conversion unit.
- the coating current is then supplied by means of the isolation transformer to the power conversion unit of an electrode arranged in the dip tank.
- the coating installation according to the invention the combination of a coating installation and a supply current source according to the invention and / or the method according to the invention for coating workpieces may have the features and / or advantages described below:
- adjacent power conversion units may preferably additionally apply the coating current provided by a failed power conversion unit.
- a corresponding control and / or regulation of the power conversion units of the power conversion system is preferably carried out by means of the control device.
- the total coating energy required that is, the total coating current required
- the total coating energy required is distributed among a plurality of power conversion units of the power conversion system.
- several voltage potentials for coating the workpieces can be provided, whereby a coating result can be improved.
- these can preferably be fully self-contained current-controlled or voltage-controlled.
- the electrodes are connected in pairs to one power conversion unit each.
- split electrodes in particular dialysis cells
- a current conversion unit which supplies a part of the electrode, in particular the dialysis cell, with coating current
- At least one electrode in particular at least one dialysis cell, in particular in the vertical direction, is divided into at least two parts such that a ratio, in particular a height ratio and / or an area ratio, which can assume at least two parts of any value ,
- the ratio in particular the height ratio and / or the area ratio of the two or more parts at least one electrode, in particular dialysis cell, about 1: 1, 3/4: 1/4, 1/4: 3/4 , Vs: 7s, 7s: 2/3, 7s: 7s: 7s, 7 4: 7 4: 2/4, 7, 4: 2/4: 4 or 7 2/4: 7 4: 7. 4
- split electrodes in particular divided dialysis cells, that is, multi-part electrodes or dialysis cells, preferably allows the reduction in delivery and
- flat cells, half-round cells and / or round cells are suitable for the entire electrode, in particular the entire dialysis cell, and / or individual or several parts of the electrode or dialysis cell.
- a separate power conversion unit is provided for each part of an electrode, in particular for each part of a dialysis cell.
- Each part of a dialysis cell preferably forms an electrode portion of an electrode.
- each electrode section of an electrode is assigned a separate power conversion unit.
- At least one electrode is divided into at least two electrode sections or parts and / or comprises two or more electrode sections or parts which are independent of each other, wherein each electrode section or part of the electrode is associated with a separate power conversion unit.
- Current conversion unit is preferably a coating stream supplied to the respective electrode portion or part controllable and / or regulated, in particular independent of the coating currents for further electrode sections or parts.
- asymmetrical workpieces can also be optimally coated.
- a non-symmetrical, non-linear course of a conveying path, along which the workpieces are conveyed through the dip tank, are controlled.
- the necessary galvanic separation preferably does not occur
- the frequency f p is preferably about 20 kHz.
- the power conversion units may preferably be connected directly to the normal power network.
- the coating of the workpiece to be coated is preferably taken over by one of the other power conversion units via the electrode assigned to this other power conversion unit.
- the coating system according to the invention can preferably be used to save energy, since hardly any reactive power is required (cos ⁇ > 0.97 over the entire voltage range from 0 V to approximately 400 V).
- the isolation transformer is preferably designed so that the apparent power at least approximately corresponds to the active power.
- the feed can preferably be made from the normal hall network.
- an improved coating quality is preferably obtained. Furthermore, the coating quality can preferably be optimized by a uniform current-guided driving style.
- a consumption of coating material can preferably be reduced. Furthermore, a wear of the current collector and the electrodes, in particular the anodes, can be reduced by a uniform current-guided driving.
- the coating system can be extended without much effort if necessary.
- the coating system according to the invention is suitable for use in all areas in which an electrochemical coating process, in particular paint coating process, is to be carried out.
- the coating system is preferably an electrodeposition coating system.
- the coating stream is preferably a painting stream.
- the workpieces are preferably paintable by means of the coating system.
- Fig. 1 is a schematic representation of a combination of a coating system and a supply current source
- Fig. 2 is a schematic representation of a power conversion unit of a
- Fig. 3 is a schematic representation of the coating system of FIG. 1 with a first embodiment of an electrode arrangement in which each electrode group is associated with a power conversion unit of the power conversion system of the coating system each consisting of two electrodes;
- each electrode is assigned a separate current conversion unit and the electrodes are designed as semi-cylindrical dialysis cells;
- FIG. 5 shows a schematic illustration corresponding to FIG. 4 of a third embodiment of an electrode arrangement in which divided, flat dialysis cells are provided in the vertical direction, wherein a separate current conversion unit is provided for each partial dialysis cell;
- FIG. 6 is a schematic illustration, corresponding to FIG. 4, of a fourth embodiment of an electrode arrangement in which a cylindrical dialysis cell is provided, which is arranged in an upper region of a dip tank of the coating installation and aligned parallel to a conveying direction of a conveying device of the coating installation;
- FIG. 7 shows a schematic representation corresponding to FIG. 6 of a fifth embodiment of an electrode arrangement, wherein the cylindrical dialysis cell is arranged in a lower region of the dip tank;
- FIG. 8 is a schematic illustration, corresponding to FIG. 7, of a sixth embodiment of an electrode arrangement in which a semi-cylindrical dialysis cell is provided, which extends transversely to the conveying direction of the conveying device of the coating installation; and 9 shows a schematic representation corresponding to FIG. 4 of a seventh embodiment of an electrode arrangement in which two flat dialysis cells and two cylindrical dialysis cells arranged in a lower region of the dip tank are provided.
- 100 includes a dip tank 102 filled with an immersion bath 104 of coating liquid and a power conversion system 106 by which power from a supply power source 108 for a plurality of electrodes 110 of FIG Coating plant 100 can be provided.
- workpieces 112 for example vehicle bodies 114
- the electrodes 110 are used to supply the current to the immersion bath 104 in the immersion basin 102, wherein the workpieces 112 form cathodes 120 and wherein electrodes 110 arranged stationarily in the immersion basin 102 form anodes 122.
- the anodes 122 are distributed uniformly or non-uniformly in the immersion basin 102 in different embodiments and electrically connected to a respective current conversion unit 124 of the power conversion system 106. To operate the coating system 100, power is required, which can be provided by means of the supply current source 108.
- a supply current in particular a three-phase current, provided. Since this three-phase current can not be applied directly to the electrodes 110, but must be converted into direct current in order to perform a coating operation, the supply current is converted by means of the current conversion system 106. In particular, by means of the current conversion system 106, a direct current, which is also referred to below as the coating current, is generated.
- the conveying device 116 By means of the conveying device 116, workpieces 112, in particular vehicle bodies 114, are introduced into the immersion bath 104 in the immersion basin 102 and guided along the conveying direction 118 through the immersion basin 102.
- the coating current which is generated from the supply current by means of the current conversion system 106 is applied to the electrodes 110.
- An electric current flow from the anodes 122 to the cathodes 120 formed by the workpieces 112 causes coating material to deposit on the workpieces 112 and thus be coated.
- each current conversion unit 124 comprises an input 130, with which the current conversion unit 124 can be connected to the supply current source 108.
- the power conversion unit 124 includes a rectifying device 132 for generating a direct current from the three-phase rotating current of the supply power source 108 and supplying the direct current to a power switch 134 of the power conversion unit 124.
- the power switch 134 is formed as an insulated gate bi-polar transistor (IGBT) 136 and serves to adjust an electric power transmitted by the power conversion unit 124.
- IGBT insulated gate bi-polar transistor
- the power switch 134 is connected on the input side to the rectification device 132 and thus on the input side to the supply current source 108.
- the power switch 134 On the output side, the power switch 134 is connected to an isolating transformer 138 of the power conversion unit 124.
- the isolation transformer 138 of the power conversion unit 124 serves to electrically isolate the electrode 110 connected to the power conversion unit 124 from the supply power source 108.
- the isolation transformer 138 On the input side, the isolation transformer 138 is connected to the power switch 134. On the output side, the isolating transformer 138 is connected to an electrode 110, in particular an anode 122. Since only alternating current can be transmitted by means of the isolation transformer 138, but DC must be applied to the anodes 122, a rectification device 140 and a smoothing device 142 are provided between the isolation transformer 138 and the anode 122. By means of the rectification device 140, the AC current transmitted by the isolation transformer 138 can be rectified. Subsequently, this current can be smoothed by means of the smoothing device 142, which is formed, for example, as a filter 144, so that the coating flow to be supplied to the anode 122 has the lowest possible waviness.
- the rectification device 140 is connected on the input side to the isolating transformer 138 and on the output side to the smoothing device 142.
- the smoothing device 142 is connected on the input side to the rectification device 140 and on the output side to an output 146 of the current conversion unit 124.
- the output 146 of the current conversion unit 124 is connected to an electrode 110, in particular anode 122.
- the coating installation 100 comprises a control device 148.
- the control device 148 may be provided centrally for all power conversion units 124.
- each power conversion unit 124 is provided with a separate control device 148.
- each power conversion unit 124 is then further associated with an interface 150, so that the control devices 148 of the various power conversion units 124 can communicate with each other directly and / or via a higher-level (not shown) control device.
- the three-phase rotation current provided by the supply current source 108 which can be applied to the input 130 of the current conversion unit 124, can be converted into a direct current that can be supplied to the anode 122 and can be provided at the output 146 of the current conversion unit 124.
- FIG 3 shows a first embodiment of an electrode arrangement 149, in which two rows 151 of anodes 122, which are parallel to the conveying direction 118 of the conveying device 116 and run parallel to one another, are provided.
- Each anode 122 is designed as a flat, plate-shaped dialysis cell 152.
- Each dialysis cell 152 is multiply divided in the vertical direction, for example, in two parts, wherein preferably both parts 154 of the dialysis cell 152 are connected to a common current conversion unit 124.
- the two rows 151 of anodes 122 are arranged in a horizontal direction on both sides (right and left) of a conveying path of the workpieces 112.
- One in Fig. 4 illustrated second embodiment of an electrode assembly 149 differs from that shown in FIG. 3 essentially in that the anodes 122 are designed as semicircular, non-divided dialysis cells 152, which are aligned in the vertical direction, wherein each dialysis cell 152 is assigned a separate current conversion unit 124.
- the dialysis cells 152 are essentially semicylindrical shell-shaped.
- the in Fig. 4 illustrated second embodiment of an electrode assembly 149 in terms of structure and function with the in FIG. 3, so that reference is made to the above description thereof in this regard.
- FIG. 5 illustrated third embodiment of an electrode assembly 149 differs from that shown in FIG. 3 substantially by the fact that a separate power conversion unit 124 is provided for each part 154 of a dialysis cell 152.
- the third embodiment of an electrode arrangement 149 shown in FIG. 5 is identical in construction and function to the one shown in FIG. 3, so that reference is made to the above description thereof in this regard.
- a fourth embodiment of an electrode arrangement 149 illustrated in FIG. 6 differs from the second embodiment illustrated in FIG. 4 essentially in that the anode 122 is designed as a round dialysis cell 152.
- a round dialysis cell 152 is in particular a substantially cylindrical dialysis cell 152.
- the dialysis cell 152 is in accordance with the in Fig. 6 illustrated fourth embodiment of the electrode assembly 149 disposed in an upper portion 156 of the dip tank 102 and extends substantially parallel to the conveying direction 118th
- FIG. 6 illustrated fourth embodiment of an electrode assembly 149 in terms of structure and function with the in FIG. 4, so that reference is made to the above description in this respect.
- a fifth embodiment of an electrode arrangement 149 illustrated in FIG. 7 differs from the fourth embodiment illustrated in FIG. 6 essentially in that the dialysis cell 152 is arranged in a lower region 158 of the immersion basin 102.
- the fifth embodiment of the electrode assembly 149 shown in FIG. 7 is identical in structure and function to the fourth embodiment shown in FIG. 6, so that reference is made to the above description thereof.
- a sixth embodiment of an electrode arrangement 149 shown in FIG. 8 differs from that shown in FIG. 7, essentially in that the dialysis cell 152 is designed as a half-cylinder shell-shaped dialysis cell 152.
- dialysis cell 152 is shown in FIG. 8 illustrated sixth embodiment of the electrode assembly 149 not parallel, but aligned transversely to the conveying direction 118.
- the in Fig. 8 illustrated sixth embodiment of the electrode assembly 149 in structure and function with the in FIG. 7, so that reference is made to the above description thereof in this regard.
- a seventh embodiment of an electrode arrangement 149 illustrated in FIG. 9 differs from that shown in FIG. 3, essentially in that both two flat, plate-shaped dialysis cells 152 and two cylindrical dialysis cells 152 are provided, wherein the cylindrical dialysis cells 152 are arranged underneath the plate-shaped dialysis cells 152 and wherein each dialysis cell 152 is assigned to a separate current conversion unit 124.
- the flat, plate-shaped dialysis cells 152 are arranged adjacent to one another with respect to the conveying direction 118.
- the round dialysis cells 152 are arranged offset to one another in the vertical direction and are aligned parallel to one another and parallel to the conveying direction 118.
- the dialysis cells 152 are not arranged one behind the other in the conveying direction 118, but extend at least in sections next to one another parallel to the conveying direction 118.
- FIG. 9 illustrated seventh embodiment of an electrode assembly 149 in structure and function with the in FIG. 3, so that reference is made to the above description thereof in this regard.
- round or semicircular dialysis cells 152 can be used to optimize the coating process in addition to flat dialysis cells 152.
- the current intensity of the coating current and the electric field in the immersion bath 104 can be specifically influenced in order to obtain an optimum coating result. Furthermore, by providing independent current conversion units 124, each with a separate isolation transformer 138, a failure of a defective power conversion unit 124 can be compensated for by amplifying a coating current delivered to an adjacent anode 122 by means of a further current conversion unit 124.
- the coating system 100 shown in FIGS. 1 to 9 is thus flexible and reliable operable.
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- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Electrochemistry (AREA)
- Materials Engineering (AREA)
- Metallurgy (AREA)
- Organic Chemistry (AREA)
- Automation & Control Theory (AREA)
- Coating Apparatus (AREA)
- Electrostatic Spraying Apparatus (AREA)
- Battery Electrode And Active Subsutance (AREA)
- Water Treatment By Electricity Or Magnetism (AREA)
Abstract
Description
Claims
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE102011056496A DE102011056496A1 (de) | 2011-12-15 | 2011-12-15 | Beschichtungsanlage und Verfahren zum Beschichten von Werkstücken |
PCT/EP2012/074363 WO2013087455A1 (de) | 2011-12-15 | 2012-12-04 | Beschichtungsanlage und verfahren zum beschichten von werkstücken |
Publications (2)
Publication Number | Publication Date |
---|---|
EP2791397A1 true EP2791397A1 (de) | 2014-10-22 |
EP2791397B1 EP2791397B1 (de) | 2017-02-08 |
Family
ID=47290979
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP12795435.2A Active EP2791397B1 (de) | 2011-12-15 | 2012-12-04 | Beschichtungsanlage und verfahren zum beschichten von werkstücken |
Country Status (12)
Country | Link |
---|---|
US (1) | US9988729B2 (de) |
EP (1) | EP2791397B1 (de) |
JP (1) | JP2015500401A (de) |
KR (1) | KR20140102209A (de) |
CN (1) | CN103987880A (de) |
BR (1) | BR112014013903A2 (de) |
CA (1) | CA2858237A1 (de) |
DE (1) | DE102011056496A1 (de) |
MX (1) | MX2014006932A (de) |
RU (1) | RU2014122745A (de) |
WO (1) | WO2013087455A1 (de) |
ZA (1) | ZA201403941B (de) |
Families Citing this family (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR102066166B1 (ko) * | 2017-12-26 | 2020-01-14 | (주)제이앤디 | 효율성을 증대시킨 전착 도장 시스템 |
CN114269989A (zh) * | 2019-07-24 | 2022-04-01 | 蓝信公司 | 桩及用于安装桩的方法 |
DE102020201562A1 (de) | 2020-02-07 | 2021-08-12 | Dürr Systems Ag | Stromwandlungseinheit und Beschichtungsanlage |
Family Cites Families (14)
Publication number | Priority date | Publication date | Assignee | Title |
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BE759416A (fr) * | 1969-11-25 | 1971-05-25 | Ppg Industries Inc | Procede d'echange d'ions d'un ultrafiltrat provenant d'un bain de depotelectrolytique |
JPS5836077B2 (ja) * | 1980-06-30 | 1983-08-06 | トヨタ自動車株式会社 | カチオン樹脂塗料を用いる電着塗装装置 |
GB2111080A (en) * | 1981-12-08 | 1983-06-29 | Ppg Industries Inc | Electrodeposition bath treatment |
CN2062337U (zh) * | 1989-11-20 | 1990-09-19 | 中国人民解放军装甲兵工程学院 | 摩擦电喷镀电源装置 |
DE69402939T2 (de) * | 1993-10-22 | 1997-10-23 | Renault | Anlage zur Oberflächenbehandlung von metallischer Werkstücken durch Kataphorese, insbesondere von Automobilkarosserien |
JPH1185294A (ja) * | 1997-09-12 | 1999-03-30 | Nippon Boshoku Kogyo Kk | 直流電源装置 |
US6919012B1 (en) * | 2003-03-25 | 2005-07-19 | Olimex Group, Inc. | Method of making a composite article comprising a ceramic coating |
DE10325656C5 (de) * | 2003-06-06 | 2007-12-27 | Eisenmann Anlagenbau Gmbh & Co. Kg | Elektrophoretische Tauchlackieranlage |
DE202004021146U1 (de) | 2004-12-22 | 2006-12-21 | Dürr Systems GmbH | Elektrotauchlackieranlage |
DE102005049712B3 (de) * | 2005-10-18 | 2006-10-26 | Eisenmann Maschinenbau Gmbh & Co. Kg | Elektrophoretische Tauchlackieranlage |
DE102006044050A1 (de) * | 2006-09-20 | 2008-04-03 | Eisenmann Anlagenbau Gmbh & Co. Kg | Verfahren zur elektrophoretischen Beschichtung von Werkstücken und Beschichtungsanlage |
US9611561B2 (en) * | 2007-09-10 | 2017-04-04 | Enpirion, Inc. | Electroplating cell and tool |
JP2010539334A (ja) * | 2007-09-20 | 2010-12-16 | シーメンス アクチエンゲゼルシヤフト | 電気化学コーティング設備の給電回路網の電流制御装置 |
US8313627B2 (en) * | 2008-01-24 | 2012-11-20 | GM Global Technology Operations LLC | Drag through electro-deposition system |
-
2011
- 2011-12-15 DE DE102011056496A patent/DE102011056496A1/de not_active Withdrawn
-
2012
- 2012-12-04 WO PCT/EP2012/074363 patent/WO2013087455A1/de active Application Filing
- 2012-12-04 JP JP2014546411A patent/JP2015500401A/ja active Pending
- 2012-12-04 MX MX2014006932A patent/MX2014006932A/es unknown
- 2012-12-04 RU RU2014122745A patent/RU2014122745A/ru not_active Application Discontinuation
- 2012-12-04 EP EP12795435.2A patent/EP2791397B1/de active Active
- 2012-12-04 KR KR1020147015559A patent/KR20140102209A/ko not_active Application Discontinuation
- 2012-12-04 CA CA2858237A patent/CA2858237A1/en not_active Abandoned
- 2012-12-04 CN CN201280060897.6A patent/CN103987880A/zh active Pending
- 2012-12-04 BR BR112014013903A patent/BR112014013903A2/pt not_active Application Discontinuation
-
2014
- 2014-05-29 ZA ZA2014/03941A patent/ZA201403941B/en unknown
- 2014-06-03 US US14/294,608 patent/US9988729B2/en active Active
Non-Patent Citations (1)
Title |
---|
See references of WO2013087455A1 * |
Also Published As
Publication number | Publication date |
---|---|
EP2791397B1 (de) | 2017-02-08 |
BR112014013903A8 (pt) | 2017-06-13 |
DE102011056496A1 (de) | 2013-06-20 |
KR20140102209A (ko) | 2014-08-21 |
MX2014006932A (es) | 2014-09-11 |
US9988729B2 (en) | 2018-06-05 |
CA2858237A1 (en) | 2013-06-20 |
JP2015500401A (ja) | 2015-01-05 |
RU2014122745A (ru) | 2016-02-10 |
US20140291158A1 (en) | 2014-10-02 |
WO2013087455A1 (de) | 2013-06-20 |
ZA201403941B (en) | 2015-12-23 |
CN103987880A (zh) | 2014-08-13 |
BR112014013903A2 (pt) | 2017-06-13 |
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