INSTALLATION AND METHOD FOR COATING OBJECTS

Abstract

An installation for coating objects, in particular vehicle wheels, has a dipping trough which is filled with a coating liquid into which the objects can be dipped. In order to reduce the complexity of the piping, there is provided a combined recirculation and filtration circuit for recirculating and filtering the coating liquid, wherein the recirculation and filtration circuit includes a pump, at least one recirculation outlet, arranged in the dipping trough, for the coating liquid, and a filtration device having a residue connection and a filtrate connection, wherein the residue connection is connected to the at least one recirculation outlet in the dipping trough.

Claims

1. A method for coating objects, comprising the steps of: a) immersing objects in a dip tank which is filled with a coating fluid, b) circulating and filtering the coating fluid in the dip tank by removing at least a portion of the coating fluid from the dip tank; filtering the coating fluid which has been removed from the dip tank in a filtration device having a retentate connection and a filtrate connection, whereby retentate and filtrate are separated in the filtering device and the retentate accumulates at the retentate connection and the filtrate accumulates at the filtrate connection; connecting the retentate connection to all of one or more circulation outlets arranged in the dip tank; returning the retentate to the dip tank through all of the one or more circulation outlets arranged in the dip tank; and generating a circulation flow within the coating fluid in the dip tank by returning the retentate to the dip tank from the retentate connection through the one or more circulation outlets.

2. The method of claim 1, wherein the coating fluid is maintained in a homogenous state by the circulation flow formed by the returning of retentate and circulating of the coating fluid by the one or more circulation outlets.

3. The method of claim 1, further comprising the step of connecting the filtrate connection to a cleaning tank to provide the filtrate to the cleaning tank, the objects being cleaned in the cleaning tank after being immersed in the dip tank.

4. The method of claim 1, further comprising the step of controlling the temperature of the portion of the coating fluid removed from the dip tank.

5. The method of claim 1, further comprising the steps of: surrounding one or more electrodes used to generate a voltage in the dip tank with one or more exchange diaphragms, and providing dialysis fluid to the dip tank in order to reduce the acid content of the coating fluid in the dip tank.

6. The method of claim 1, wherein the portion of the coating fluid removed from the dip tank is removed by overflowing from the dip tank into an overflow tank, wherein the coating fluid which overflows into the overflow tank is pumped from the overflow tank to the filtration device.

7. The method of claim 1, further comprising the step of pre-filtering the portion of the coating fluid removed from the dip tank, wherein the coating fluid is separated into the retentate and the filtrated in an ultra-filtration module after being pre-filtered.

8. The method of claim 1, wherein the one or more circulation outlets each comprise an injector nozzle.

9. The method of claim 1, wherein the objects are vehicle wheels.

10. A method for coating objects, comprising the steps of: a) immersing objects in a dip tank which is filled with a coating fluid, b) circulating and filtering the coating fluid in the dip tank by removing at least a portion of the coating fluid from the dip tank; separating retentate and filtrate from the portion of the coating fluid removed from the dip tank; accumulating the retentate at a retentate connection; connecting the retentate connection to all of one or more circulation outlets arranged in the dip tank; returning the retentate to the dip tank through all of the one or more circulation outlets arranged in the dip tank; and generating a circulation flow within the coating fluid in the dip tank by returning the retentate to the dip tank from the retentate connection through the one or more circulation outlets.

11. The method of claim 10, wherein the coating fluid is maintained in a homogenous state by the circulation flow formed by the returning of retentate and circulating of the coating fluid by the one or more circulation outlets.

12. The method of claim 10, further comprising the steps of: accumulating filtrate at a filtrate connection; and connecting the filtrate connection to a cleaning tank to provide the filtrate to the cleaning tank, the objects being cleaned in the cleaning tank after being immersed in the dip tank.

13. The method of claim 10, further comprising the step of controlling the temperature of the portion of the coating fluid removed from the dip tank.

14. The method of claim 10, further comprising the steps of: surrounding one or more electrodes used to generate a voltage in the dip tank with one or more exchange diaphragms, and providing dialysis fluid to the dip tank in order to reduce the acid content of the coating fluid in the dip tank.

15. The method of claim 10, wherein the portion of the coating fluid removed from the dip tank is removed by overflowing from the dip tank into an overflow tank, wherein the coating fluid which overflows into the overflow tank is pumped from the overflow tank to the filtration device.

16. The method of claim 10, wherein the one or more circulation outlets each comprise an injector nozzle.

17. An installation for coating objects comprising: a) a dip tank which is filled with a coating fluid in which objects can be dipped, wherein b) a filtration device for filtering at least a portion of the coating fluid which is removed from the dip tank, wherein the filtration device comprises a pump having a pump inlet and a pump outlet, wherein the pump inlet is at least indirectly connected to the dip tank, a retentate connection where retentate is accumulated, a filtrate connection where filtrate is accumulated c) one or more circulation outlets arranged in the dip tank for the coating fluid, wherein the retentate connection is connected to all of the one or more circulation outlets in the dip tank and the retentate is returned to the dip tank from the retentate connection through all of the one or more circulation outlets.

18. The installation according to claim 17, wherein the one or more circulation outlets each comprise an injector nozzle, wherein the one or more circulation outlets and injector nozzles generate a circulation flow in the dip tank, the circulation flow maintaining the coating fluid in the dip tank in a homogenous state.

19. The installation according to claim 17, further comprising a heat exchanger, the heat exchanger controlling the temperature of the portion of the coating fluid removed from the dip tank.

20. The installation according to claim 17, wherein the filtrate connection of the filtration device is at least indirectly connected to a cleaning tank, in which the objects are cleaned after the coating operation, the filtrate being provided to the cleaning tank.

Description

BRIEF DESCRIPTION OF THE DRAWINGS

[0028] The invention is explained below with reference to two embodiments and with reference to the appended drawings, in which:

[0029] FIG. 1 is a schematic illustration of an installation for dip coating vehicle wheels;

[0030] FIG. 2 is a schematic illustration of a modified installation having a buffer container for cleaning water.

DETAILED DESCRIPTION OF PREFERRED EMBODIMENTS

[0031] While this invention is susceptible of embodiment in many different forms, there is shown in the drawings and will herein be described in detail one or more embodiments with the understanding that the present disclosure is to be considered as an exemplification of the principles of the invention and is not intended to limit the invention to the embodiments illustrated.

[0032] FIG. 1 shows an installation which is generally designated 10 for cataphoretic dip coating of vehicle wheels 12.

[0033] The installation 10 comprises a dip tank 14 which is filled with an electrodeposition paint 16 as a coating fluid. The vehicle wheels 12 which are intended to be painted are lowered into the dip tank 14 using a conveying device 18 which is only partially shown and thereby partially or completely immersed in the electrodeposition paint 16 which is substantially composed of deionized water, binding agent and paint pigments and other known additives. By applying a voltage between the vehicle wheels 12 and electrodes 20 which are also arranged in the dip tank 14, the coating process is started.

[0034] In addition to the dip tank 14, there is provided in this instance in the form of a channel which extends along the dip tank 14 an overflow tank 22 into which excess electrodeposition paint 16, as indicated by the flow arrow 24, can overflow. In this instance, conversion products of the electrodeposition paint 16 which occur during the coating process and other impurities are carried along, whereby a crest of foam 26 is formed in the overflow tank 22 above the electrodeposition paint 16.

[0035] In order to prevent solid components of the electrodeposition paint 16, for example, the paint pigments, from being deposited in the dip tank 14 and agglomerating in this case and in order to ensure that the physical and chemical parameters of the electrodeposition paint 16 are distributed in the dip tank 14 in a homogeneous manner, a circulation flow 32 is produced in the dip tank 14 using a combined circulation and filtration circuit 30.

[0036] The circulation and filtration circuit 30 comprises to this end firstly a pump which is constructed in this instance as a submersible pump 34 which is arranged in the overflow tank 22 and which has an inlet 35. From the outlet 37 thereof a line 36 leads to the primary side of a heat exchanger 38 whose secondary side is connected to a cooling system which is not shown by means of lines 40, 42.

[0037] In the continuation of the flow path of the electrodeposition paint 16, a line 44 leads from the primary side of the heat exchanger 38 to a filter device 46, more specifically to a pre-filter 48 of the filter device 46. From this pre-filter 48, another line 50 leads to an ultra-filtration module 52 of the filter device 46 which has a retentate connection 54 and a filtrate connection 56 as outlets of the filter device 46.

[0038] The retentate connection 54 of the filter device 46 at which a retentate which is enriched with solid components is discharged is connected by means of a line 58 to one or more circulation outlets 60 which are arranged in the dip tank 14 and which are each provided with an injector nozzle 62. The circulation outlets 60 are in this instance arranged and sized in such a manner that, with corresponding sizing of the retentate throughput (which is substantially controlled by means of the conveying power of the submersible pump 34), an adequate circulation flow 32 is produced in the dip tank 14 in order to prevent settlement of solid components and to achieve homogenization of the electrodeposition paint 16.

[0039] However, the filtrate connection 56 of the filter device 46, at which the aqueous components of the electrodeposition paint 16 are substantially discharged as filtrate, is connected to a cleaning tank 66 by means of a line 64. In this cleaning tank 66, the vehicle wheels 12 are cleaned after the coating process in order, for example, to remove non-adhesive, excess paint. The cleaning water 68 which is then partially enriched again with paint pigments (contaminated filtrate) is circulated in the cleaning tank 66 via an additional submersible pump 70 which is arranged in the cleaning tank 66 and associated circulating outlets 60. Furthermore, from an overflow outlet 72 which is arranged in the upper region of the cleaning tank 66, a line 74 leads to the overflow tank 22 of the dip tank 14 in order to return excess cleaning water 68 into the circulation and filtration circuit 30 of the dip tank 14.

[0040] In order to introduce fresh electrodeposition paint 16 with precisely defined chemical and physical parameters into the installation 10, it comprises a supply line 75 into the dip tank 14 which is connected to a paint supply device which is not shown.

[0041] Since the acid content of the electrodeposition paint 16 increases during the coating process, a dialysis circuit 76 which cooperates with the electrodes 20 (and which is only partially illustrated) is further provided. This comprises tubular exchange diaphragms 78 which coaxially surround the mostly rod-like electrodes 20. The inner space of the exchange diaphragms 78 is then flushed with dialysis fluid during the coating process in order to reduce the acid content.

[0042] Finally, the dip tank 14 is connected by means of a counter-container circuit 80 to a counter-container 82 which can receive all the electrodeposition paint 16 from the dip tank 14 and thus enables the dip tank 14 to be completely emptied for maintenance purposes or the like without having to dispose of the electrodeposition paint 16. The counter-container circuit 80 comprises for this purpose a valve arrangement 84 and a diaphragm pump 86, wherein in a first position of the valve arrangement 84 the electrodeposition paint 16 can be conveyed by the diaphragm pump 86 from the dip tank 14 into the counter-container 82. In a second position of the valve arrangement, the diaphragm pump 86 together with circulation outlets 60 which are arranged in the counter-container 82 can be used to produce a circulation flow 88 in the counter-container 82 during the maintenance operations. In a third position of the valve arrangement 84, the same diaphragm pump 86 can be used to return the electrodeposition paint 16 into the dip tank 14 again.

[0043] FIG. 2 shows a slightly modified variant of the installation 10 in which the filtrate connection 56 of the filter device 46 is not directly connected to the cleaning tank 66. Instead, the line 64 extending from the filtrate connection 56 leads from that location to a buffer container 90 in which the filtrate is provided, for example, for manual cleaning purposes of the installation 10. Another line 92 on the bottom of the buffer container 92 then leads in a similar manner to the embodiment of FIG. 1 into the cleaning tank 66.

[0044] It is to be understood that additional embodiments of the present invention described herein may be contemplated by one of ordinary skill in the art and that the scope of the present invention is not limited to the embodiments disclosed. While specific embodiments of the present invention have been illustrated and described, numerous modifications come to mind without significantly departing from the spirit of the invention, and the scope of protection is only limited by the scope of the accompanying claims.