|Publication number||US3200057 A|
|Publication date||Aug 10, 1965|
|Filing date||Dec 27, 1960|
|Priority date||Dec 27, 1960|
|Publication number||US 3200057 A, US 3200057A, US-A-3200057, US3200057 A, US3200057A|
|Inventors||Brewer George E F, Burnside Gilbert L|
|Original Assignee||Ford Motor Co|
|Export Citation||BiBTeX, EndNote, RefMan|
|Patent Citations (4), Referenced by (25), Classifications (6)|
|External Links: USPTO, USPTO Assignment, Espacenet|
Aug. 10, 1965 BURNSIDE EIAL 3,200,057
ELECTROPHORETIC COATING PROCESS Filed Dec. 27, 1960 2 Sheets-Sheet 1 POWER SOURCE I- 1 I7 I II II I II II I POWER SOURCE POWER SOURCE I I I I I 11/' E El? REWER 5%7 L. UR/VS/DE F/G' 2 INVENTORS BY efiazv 10,1955 6. 1.. BURNSIDE ET'AL 3,200,057
ELECTROPHORETIC COATING PROCESS Filed Dec. 27, 1960 2 Sheets-Sheet 2 POWER SOURCE GEORGE EEBREWER G/LBER T L. BURNS/DE INVENTORS ATTORNEYS to be coated serves as one electrode.
057 ELECTRUPHORET C COATING PROCESS Gilbert L. Burnside, Oak Park, and George E. F. Brewer,
Wolverine Lake, Mich., assiguors to Ford Motor Company, Dearborn, Mich, a corporation of Delaware Filed Dec. 27, 196i Ser. No. 73,684 4 Qlairns. (Cl. 2tl4-18l) This invention relates to the formation of electrophoretic coatings and more particularly to an improved method of coating conducting surfaces of articles by electrophoretic techniques.
Present methods of painting articles having extended and irregular shaped surfaces include hand or automatic spray painting, electrostatic painting, brushing, or dipping. Electrophoretic techniques have been applied for coating articles having a relatively small surface area but these techniques have been restricted to the applicabution of paint or due to surface blemishes.
In the past, it has also been rather difficult to obtain a relatively uniform film of paint over the entire surface of an article. Surfaces which are not readily accessible to the application of paint have not been satisfactorily coated. Recessed areas, such as rocker panels of automobiles, have only been coated at a great expense due to the requirements of special painting techniques or special hand labor operations to obtain a minimal protective coating against corrosion.' Dipping the article in a paint bath to obtain a coating of its recessed surfaces has not proven satisfactory since the evaporation of solvents from the paint film with subsequent refluxing has resulted in washing off a portion of the adhered paint coating. 7
This invention pertains to an improved method of electrophoretically coating articles which will provide a uniform coat of paint on all its surfaces.
Electrophoresis has been defined as the motion of charged particles through a suspending medium under the influence of an applied electrical field. Electrophoretic coating may be carried out in any conventional electrolytic cell. The conducting surface of the article When the article to be coated is submerged in an electrolytic solution, an electrical circuit is completed to a second electrode to initiate deposition of emulsified colloidal particles suspended in the electrolytic solution. In an electrical field, these colloidal particles in suspension move either toward the negative or the positive electrode showing that the dispersed particles carry either a positive or a negative charge. Upon contact with an electrode, the colloidal particles lose their electrical charges, thereby breaking the emulsion and depositing as a coating on the electrode.
Electrophoretic deposition of composition coatings is old in the art.
by submerging it in a bath of finely divided insulating organic particles in a liquid medium. When a potential is applied between the anode and a cathode, which is United States Patent 2,307,018 discloses one method of forming an insulating coating on an anode 3,29%,057 Patented Aug. 10, .1965
ishing Magazine, volume 42, page 313 by Edward J. Roehl in an article entitled A Discussion on Electrophoretic Finishing.
The electrolyte solution utilized in the electrophoretic coating process of this invention comprises emulsified paint particles in a colloidal state dispersed in a suspended conducting liquid medium.
The paint emulsion particles are prepared so that each dispersed paint droplet when suspended in an aqueous bath is uniform in composition and consists of all film forming materials that are required for a practical paint coating. Each emulsion paint droplet is charged with either a positive or negative electrical charge so that they will migrate in an electrical field that is deposited on an electrode. An example illustrating the formulation and preparation of one paint composition to be utilized for electrophoretic coating is hereinafter described.
Current electrophoretic coatings of paint film have not proven satisfactory due to the nature of the electrophoretic coating process. Charged colloidal particles suspended in the electrolyte solution migrate towards the article being coated if the surface of the article has an electrical charge opposite in polarity .to the charge of the colloidal material. When the charged particles come into contact with the oppositely charged surface, they lose their electrical charge and deposit as a coating. The deposition of this coating is irreversible in the sense that the deposited particles lose their tendency to return into colloidal dispersion. Since some of the dispersed colloidal materials in the solution have migrated towards the article being coated while an electrical field is applied, a relatively high concentration of such colloidal particles is present near the surface of the submerged article being coated. Upon the removal of the article from the solution, many of the colloidalparticles, which have not been deposited but remain in the vicinity of the submerged article, adhere to the already deposited film. Upon the drying or curing of the deposited paint film, the nondeposited colloidal material adhering to the surface will bring about an uneven coating which is very unsightly.
Rin sing of the excess undeposited colloidal material has resulted in damaging the deposited paint film and therefore, has not proven satisfactory for removing the excess colloidal material. Also, during the rinsing operation large amounts of the undeposited colloidal materials are washed away with the rinsing solution.
The improvement of the electrophoretic coating process of this invention comprises the reversal of the direction of the electrical field after an article is electrophoretically coated by changing the polarity of the electrical charge applied to the electrolytic cell during the electrophoretic coating process, i.e. changing the direction of flow of direct electrical current between the electrodes of such cell. Upon reversal of the electrical field, the colloidal material which has been previously migrating towards the surface of the article now migrates away from the surface of the article. After a reverse field is applied for a limited time, the depletion of the colloidal material in the solution in the immediate vicinity of the submerged article is achieved. The article can then be removed from the solution without having an undeposited colloidal material adhering to its coated surface.
In US. Patent 1,769,659 it has been disclosed that in the elect-rophoretic coating process the direction of the current maybe reversed after each complete deposition to prevent pitting of the electrodes. In this patent, the potential applied during the deposition and reversal is limited to a value below the decomposition potential of tap water, which ranges between 1.2 and 1.9 volts, to prevent the formation of hydrogen and oxygen at the electrodes.
The electrical potential applied in the process of this force the migration of colloidal particles away from the vicinity of the submerged article is considerably less than the potential required to deposit a coating on the article.
Experimentally, voltages ranging between 50 volts to 1,000 volts have proven very satisfactory at a current density of .1 ampere per square foot to amperes per .square foot to electrophoretically deposit a paint coating. Voltages of 5 volts to 1,000 volts have been effective in depleting the colloidal particles in the immediate vicinity of the submerged article to prevent the adherence of colloidal particles to the deposited paint coat. The current density to be selected for the electrophoretic coating process will depend on various parameters such as the The rinse solution may be mixed with a detergent, such as soap, to reduce its surface tension in order to avoid any damage to the deposited paint film.' Very little or no agitation is required since no mechanical action is necessary to remove the undepositcd excess colloidal material.
In a second embodiment of our invention, an article 11 is electrophoretically coated in the coating bath 12 contained in the tank 13 similar to the first embodiment as illustrated in FIGURE 2a. After the article 11 is coated, it is not lifted from. the bath 12 but remains submerged in the same tank 13 while the direction of the electrical field between the article 11 and the electrode 14 is reversed as selected voltage and the desired thickness of the coating, i
the conductivityand composition of the coating bath and the time allotted for the formation of the desired coating, and the distance between the electrodes. Gaseous products given =ofi at the electrodes are of no serious concern in the process of electrophoretic coating of paint films of this invention since the paint composition is formulated to effect a continuous film when polymerized.
An object of this invention is to provide for an improved electrophoretic coating process which will result in an even and unblemished paint film, thereby, improving the surface finish of the article being coated.
A further object of this invention is the elimination of the rinsing operation which may be required after an article is electrophoretically coated.
A further object of this invention is the reduction of wastage of paint since the undepo'sited colloidal material will substantially remain in the aqueous coating bath where it can be used further for the coating of additional articles.
Other objects and advantages of this invention will become more apparent from the following description to be read in conjunction with the accompanying drawings in which:
FIGURE 1 is a schematic drawing depicting the apparatus of the first embodiment of this invention;
FIGURE 2a is :a schematic diagram showing the first phase of electrophoret-ically coating an article utilizing the equipment of the second embodiment of this invention;
FIGURE 21) is a schematic diagram illustrating the rinsing operation which is the second phase of the second embodiment of this invention;
FIGURE 3 is a schematic drawing of the third embodiment of this invention illustrating the electrophoretic coating of articles suspended from a conveyor; and,
FIGURE 4 is a schematic drawing depicting the fourth embodiment of this invention showing a modified apparatus of the third embodiment illustrated in FIGURE 3.
In the first embodiment of our invention, an electrically grounded article 11 is electrophoretically coated by submerging it in a coating bath 12 contained in an insulated tank 13, followed by the application of a negative electrical charge to an electrode 141 which is also submerged in the coating bath 12. After the article 11 is electro phoretica'lly coated, it is removed tfrom the coating bath 12 and submerged in a rinse solution 15 contained in a second tank 16 which is grounded.
During the eleotrophoretic coating operation, the negative electrical charge is applied to the electrode 14 from the negative terminal of a power source 17. During the rinsing operation, the negative electrical charge is directly applied to the article 11. When the electrical charge is applied to the article 11 while it is submerged in the rinse solution 15, undeposited excessive colloidal material which has been adhering to the deposited film coat migrates away from the immediate vicinity of the submerged article 11.
shown in FIGURE 2b. The reversal of the electrical field is achieved by connecting the article 11 to the negative terminal of the power source 17 and electrically grounding the electrode. This reversal of the electrical field will suit in the migration of the undeposited colloidal material in the immediate vicinity of the submerged article 11 away from its coated surface. The article 11 is then lifted from the coating bath 12-the resulting surface film being uniform and relatively free from undeposited material.
In a third embodiment of this invention, .as illustrated in FIGURE 3, the articles 11 to be coated are transported by a conveyor 18 to an insulated tank 13 containing the electrophoretic coating bath 12. The articles 11 are hung from the conveyor 18 by a paint hook 19 which has an electrically insulated portion 20 to isolate the article'11 from ground. A contact plate 21 is attached to the paint book 19 below its insulated portion 20. Article 11a, about to be coated, is grounded when the contact plate 21 makes an electrical connection with a grounded bus bar 22. Article 11b, already coated, after having been su'bmerged in the coating bath 12, becomes negatively charged when the contact plate 21 contacts a second bus-bar 23 which is connected to the negative terminalof the power source 17.
Colloidal paint particles in the coating bath 12 are repelled from the. vicinity of the article 11b which serves as a cathode of the electrolytic cell. The chalged particles are propelled towards the article 11a which is grounded and are irreversibly deposited on its surface. Articles 11a and 11b remain submerged in the coating bath 12 until a sufficient paint film is deposited on the surface of article 11a. Article 11b becomes a cathodeafter being coated by being electrically connected to the negative terminal of the power soure 17 through the contact plate 21 and the bus bar 23. The uncoated article 11a, which is conveyed to the tank 13, becomes submerged in the coating bath 12 where it is grounded by the bus bar 22 to become the anode of the electrolytic cell.
Upon the removal of the coated article 11b from the coating bath 12, substantially no excess undeposited material will adhere to its coated surface due to the depletion of the colloidal material in the vicinity of the submerged coated article 11b during the coating of article 11a. The coated article 1112 is then conveyed to an oven 24 to cure the deposited paint film. To keep the colloidal material uniformly dispersed in the coating bath 12, a mixer 25 is placed into the tank 13 to slightly agitate the coating bath 12. V g
This embodiment of our invention readily lends itself to a continuous high volume coating of articles by electrophoretic means which will result in a high quality paint film without requiring a rinsing operation. I
A further embodiment of this invention is illustrated in FIGURE 4. A second electrode 26 having a large surface area is placed into the coating bath 12 contained in the tank 13 and is then electrically connected to the negative terminal of the power source 17. Upon the application of the electrical field, charged paint particles will migrate from the vicinity of the coated article 11b and from the electrode 26 to deposit a film on the electrically grounded article 11a.
The potential required to sufficiently propel particles away from the coated surface 1112 does not have to be as great as that required to deposit charged particles on an uncoated surface 11a. By utilizing the second electrode 26 as a cathode, the required total potential between the coated article 11b and the uncoated article 11a may be reduced since the coated article 11b, serving as the only cathode in the embodiment illustrated in FIGURE 3, has a relatively high resistance due to its built up insulating paint coat. Otherwise, a relatively high potential would be necessary to deposit the paint particles on the uncoated article 11a. I
It is to be understood that for certain formulations of the coating bath, in which the dispersed colloidal materials are positivelycharged, deposition can also be initiated on the surface of an article when the article serves as a cathode of the electrolytic cell.
One red primer which may be electrophoretically deposited as a prime coating on an electrically grounded steel panel is formulated as follows:
A film forming material consisting of a styrene-allyl alcohol copolymer 63 percent by Weight is mixed with linseed fatty acid 37 percent by weight. This mixture is esterified at 500 F. to an Acid Number of 5 and a maximum viscosity of 2.5 poises measured when the copolymer is reduced to 60 percent nonvolatile with xylene. A portion of this film forming mixture 51 percent by weight is intimately blended in a roller mill with red oxide pigment 45 percent by Weight and linseed fatty acid 4 percent by weight. This blend 38 percent by weight is then let down by further blending it with an additional portion of the film forming material of the above composition 50 percent by weight, malamine formaldehyde 11.8 percent by weight, and cobalt naphthanate .2 percent by weight.
This pain-t mixture is then emulsified by the addition of an emulsifying agent which consists of chemically pure concentrated ammonium hydroxide (28 percent strength) 3.5 percent by weight and demineralized water 96.5 percent by weight. This diluted ammonium hydroxide solution is gradually added until the so-called inversion point is reached at which time the viscosity of the paint mixture drops suddenly after reaching a high point. The balance of the diluted ammonium hydroxide is then added. The resulting emulsion is then further refined in a colloid mill until a more stable emulsion is reached.
The paint composition of the above example is then utilized to prepare an aqueous coating bath for electrophoretically coating a metallic article. One example of the electrophoretic coating process utilizing this paint composition is as follows:
Example 1 Two parts of the automotive primer paint composition described above is thoroughly mixed with 6 parts of water and A; part of concentrated ammonia to form a colloidal dispersion to be used as a coating bath. This coating bath has a specific resistance of approximately 5.0 10 ohm centimeter.
The metallic article to be coated is immersed in the bath and electrically grounded. A negative charge is applied to an electrode also immersed in the bath as described in the second embodiment of this invention illustrated in FIGURE 2a. This negative charge is gradually increased until the potential difference between the electrode and the article reaches 150 volts in an approximately 20 second time period. The electrical potential is then maintained at 150 volts for an additional 40 seconds in order to obtain a uniform paint film of approximately 1 mil thickness on the surface of the article after the paint film is cured. The specific resistivity of the uncured deposited paint film is approximately 30x10 ohm centimeter, and the final current density measures approximately 1.7 amperes per square foot.
After the desired film thickness is achieved, the article is lifted from the electrophoretic coating bath and immersed in a conductive rinse bath containing a grounded electrode as illustrated in FIGURE 2b. While the article is being rinsed, an electrical potential of approximately 45 volts at a current density of /2 ampere per square foot is applied directly to the coated article for about a 30 second period. After the rinsing operation, the article is removed from the bath and baked in an oven at a temperature of approximately 350 F. for 10 minutes to cure the electrophoretically deposited prime coating.
Example 2 One part of the automotive primer paint composition heretofore described is mixed with 6 parts of water and part of concentrated ammonia and V part of a soap detergent to form a colloidal dispersion to beused as a coating bath. The'specific resistance of this coating bath is approximately 1.0 10 ohm centimeter. The metallic article to be prime coated is immersed in the coating bath and electrically grounded. An electrode, which is also immersed in the bath, has an electrical charge applied which is gradually increased to 200 volts in 30. seconds; This potential is maintained between the electrode and the article for approximately an additional 60 seconds in order to obtain a paint film of approximately 1 mil thickness on the surface of the article after the film is cured. The specific resistivity of this paint film on the coated article measures approximately 2.1 X 10" ohm centimeter, and the final current density measures approximately 3.5 amperes per square foot.
After the desired film thick-ness is achieved, the electrode is grounded and an electrical potential of 200 volts is applied directly to the coated article for 20 seconds to remove the excess colloidal material from the vicinity of the immersed coated article. The article is then removed from the bath and baked in an oven at an approximate temperature of 375 F. for about 10 minutes to cure the deposited prime paint coating on the surface of the metallic article.
The power source 17 utilized in Examples 1 and 2 is a rectifier having a range of 0 and 1,000 volts and 0 and amperes.
1. In a method of applying a coating to a conducting surface of an article comprising the steps of causing the surface of said article to contact an aqueous bath having organic film-forming material dispersed therein, said article serving as a first electrode, causing a second electrode to contact said aqueous bath, and causing a direct electric current to flow between said first and second electrodes and through said aqueous bath at an electrical potential substantially above the value at which the electrolysis of water occurs until a coating of said film-forming material is electrically deposited upon said article from said aqueous bath, the step of causing the direction of flow of the direct electric current between said article and said bath to be reversed for a time sufiicient to remove from the surface of said electrically deposited coating film-forming material from said bath that has not been electrically deposited.
2. In a method of applying a coating to a metallic article comprising the steps of immersing said article in an aqueous bath having charged particles of organic coating material dispersed therein, said article serving as a first electrode, causing a second electrode to contact said aqueous bath, and causing a direct electric current to flow between said first and second electrodes and through said aqueous bath at an electric potential of between 50 and 1000 volts until a Water insoluble coating of said coating material is electrophoretically deposited upon said article from said aqueous bath, the step of causing the direction of fiow of direct electric current between said article and said bath to be reversed for a time sufiicient to remove charged particles of coating material from said water insoluble coating.
3. In a method of applying paint to a metallic article comprising the" steps of causing the surface of-said article to be immersed in an aqueous bath having a paint formulation comprising a film-forming organic resin dispersed therein, said article serving as a first electrode, causing a second electrode to contact said aqueous bath, and cansing a direct electric current to flow between'said first and said second electrodes and through said aqueous bath at an electric potential substantially above the value at which the electrolysis of water occurs until a water-insoluble film of paint is'electrically deposited upon said article from said aqueous bath, the steps of causing the direction of -flow of direct electric current between said article and said bath. to be reversed for a timesufficient to remove adhered paint particles from the electrically deposited paint film.
.4. In a method of applying paint to a metallic article comprising the steps of causing the surface of said article to be immersed in an aqueous bath having charged parti cles ofa paint formulation comprising a film-forming organic resin dispersed ther'ein, said article serving as a first electrode, causing a secondselectrode to contact said aqueous bath, and causing a direct electric current to fiow between said first and said second electrodes and through said aqueous bath at an electric potential in'the range of about 50 to about 1000 volts until a water insoluble film of paint is electrophoretically deposited upon said article from said aqueous bath, the step of causing the direction of flow of direct electric current between said article and said bath to be reversed for a time sufiicient to remove charged paint particles from the electrophoretically deposited paint-film at a voltage in the range of about 5 to about 1000 volts. i
References Cited by the Examiner UNITED STATES PATENTS WINSTON A. DOUGLAS, Primary Examiner. JOHN R. SPECK, MURRAY TILLMAN, Examiners.
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|U.S. Classification||204/507, 26/18.6|
|International Classification||C25D13/18, C25D13/00|