US3782328A - Squeegee /shield - Google Patents

Squeegee /shield Download PDF

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US3782328A
US3782328A US00324730A US3782328DA US3782328A US 3782328 A US3782328 A US 3782328A US 00324730 A US00324730 A US 00324730A US 3782328D A US3782328D A US 3782328DA US 3782328 A US3782328 A US 3782328A
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squeegee
article
spray
applying
path
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US00324730A
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H Franz
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PPG Industries Inc
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PPG Industries Inc
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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B05SPRAYING OR ATOMISING IN GENERAL; APPLYING FLUENT MATERIALS TO SURFACES, IN GENERAL
    • B05DPROCESSES FOR APPLYING FLUENT MATERIALS TO SURFACES, IN GENERAL
    • B05D1/00Processes for applying liquids or other fluent materials
    • B05D1/32Processes for applying liquids or other fluent materials using means for protecting parts of a surface not to be coated, e.g. using stencils, resists
    • CCHEMISTRY; METALLURGY
    • C03GLASS; MINERAL OR SLAG WOOL
    • C03CCHEMICAL COMPOSITION OF GLASSES, GLAZES OR VITREOUS ENAMELS; SURFACE TREATMENT OF GLASS; SURFACE TREATMENT OF FIBRES OR FILAMENTS MADE FROM GLASS, MINERALS OR SLAGS; JOINING GLASS TO GLASS OR OTHER MATERIALS
    • C03C17/00Surface treatment of glass, not in the form of fibres or filaments, by coating
    • CCHEMISTRY; METALLURGY
    • C23COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
    • C23CCOATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; SURFACE TREATMENT OF METALLIC MATERIAL BY DIFFUSION INTO THE SURFACE, BY CHEMICAL CONVERSION OR SUBSTITUTION; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL
    • C23C18/00Chemical coating by decomposition of either liquid compounds or solutions of the coating forming compounds, without leaving reaction products of surface material in the coating; Contact plating
    • C23C18/16Chemical coating by decomposition of either liquid compounds or solutions of the coating forming compounds, without leaving reaction products of surface material in the coating; Contact plating by reduction or substitution, e.g. electroless plating
    • C23C18/1601Process or apparatus
    • C23C18/1619Apparatus for electroless plating
    • C23C18/1632Features specific for the apparatus, e.g. layout of cells and of its equipment, multiple cells
    • CCHEMISTRY; METALLURGY
    • C23COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
    • C23CCOATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; SURFACE TREATMENT OF METALLIC MATERIAL BY DIFFUSION INTO THE SURFACE, BY CHEMICAL CONVERSION OR SUBSTITUTION; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL
    • C23C18/00Chemical coating by decomposition of either liquid compounds or solutions of the coating forming compounds, without leaving reaction products of surface material in the coating; Contact plating
    • C23C18/16Chemical coating by decomposition of either liquid compounds or solutions of the coating forming compounds, without leaving reaction products of surface material in the coating; Contact plating by reduction or substitution, e.g. electroless plating
    • C23C18/1601Process or apparatus
    • C23C18/1633Process of electroless plating
    • C23C18/1675Process conditions
    • C23C18/1683Control of electrolyte composition, e.g. measurement, adjustment
    • HELECTRICITY
    • H05ELECTRIC TECHNIQUES NOT OTHERWISE PROVIDED FOR
    • H05KPRINTED CIRCUITS; CASINGS OR CONSTRUCTIONAL DETAILS OF ELECTRIC APPARATUS; MANUFACTURE OF ASSEMBLAGES OF ELECTRICAL COMPONENTS
    • H05K3/00Apparatus or processes for manufacturing printed circuits
    • H05K3/0085Apparatus for treatments of printed circuits with liquids not provided for in groups H05K3/02 - H05K3/46; conveyors and holding means therefor
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B05SPRAYING OR ATOMISING IN GENERAL; APPLYING FLUENT MATERIALS TO SURFACES, IN GENERAL
    • B05DPROCESSES FOR APPLYING FLUENT MATERIALS TO SURFACES, IN GENERAL
    • B05D1/00Processes for applying liquids or other fluent materials
    • B05D1/02Processes for applying liquids or other fluent materials performed by spraying

Definitions

  • ABSTRACT A transparent substrate to be spray coated passes beneath a squeegee/shield apparatus to avoid formation of finger-like fronts or puddles in the spray area and to prevent splashing of the spray medium onto the substrate surface.
  • the squeegee/shield element functions to doctor a prior applied coating while intercepting of portion of the subsequent spray stream.
  • This invention relates to an apparatus for providing non-conductive transparent substrates with transparent coatings having optical properties of good uniformity, and particularly relates to a squeegee/shield apparatus that avoids sources of non-uniformity of said optical properties.
  • These techniques generally involve the immersion of a metallic article or a sensitized non-metallic article into a suitable electroless plating bath comprising an aqueous medium having dissolved therein a metal salt and an appropriate reducing agent, whereupon a metal film is deposited upon the immersed article by an autocatalytic mechanism.
  • the electroless process is an old and established one.
  • Brenner and Riddell disclosed in 1944 that an opaque coating of nickel could be autocatalytically deposited upon metallic substrates by immersing the substrates into a nickel salt solution containing sodium hypophosphite.
  • U.S. Pat. Nos. 2,532,283 and 2,532,284 were issued to Brenner and Riddell upon their discoveries.
  • the use of sodium hypophosphite as the reducing agent results in deposits which are not pure metal, but which contain about 2 to 10 percent elemental phosphorous by weight.
  • the application further states that coatings of the best uniformity may be obtained even with large plates having four or more square feet of surface when the coating is applied by separately spraying a solution of reducing agent and a solution of the reducible metal salt on the glass plate preferably while the major surfaces thereof are in a horizontal or substantially horizontal plane.
  • the process has been found to be effective over a broad temperature range for coating any of the so-cnlled catalytic metal substrates or non-catalytic substrates sensitized in a conventional manner to promote deposition of continuous, adherent transparent metal films.
  • An advantage of the process is that it will deposit highly uniform transparent films when performed at about room temperature, i.e., from about 20C. to about 30C.
  • the application further states that in order to insure that each of a plurality of substrates is provided with a coating that exhibits substantially the same physical and chemical characteristics, it is advantageous that the process temperature be held constant to within about :t 1C., for example, over 100 substrates or over 1,000 square feet of substrates, or the like. Best uniformity and appearance of transparent films is achieved when films are deposited to a thickness having a luminous transmission of about 35 to 40 percent or less, and when the films comprise nickel-boron, cobalt-boron, iron-boron, and the like. Films comprising mixtures of boron and nickel, cobalt and/or iron may also be provided.
  • the boron is present in a minor amount (rarely exceeding about percent by weight and normally between about 2 and 7 percent by weight) while the metal (nickel, cobalt and/or iron) is present in preponderant amounts (rarely less than 85 percent by weight and normally between about 93 and 98 percent by weight).
  • the transparent substrates obtained in accordance with the last-mentioned process may be employed, for example, as transparent windows or outside walls in a building such as a skyscraper or other multistory structure. These substrates may be especially advantageously employed as one of the plates which make up multiglazed units as described in the previously mentioned U.S. patent application Ser. No. 57,575, now abandoned. It will be understood that uniformity of coating in such uses is especially important because otherwise the reflected color of portions of the building differs sharply from that of other portions, thus distracting from its appearance.
  • the prior art teaches a process whereby glass plates are conveyed along an article movement path through a sequence of rinse and spray stations. After a plate leaves a rince station, it is normally covered with a layer of water. When the plate enters a spray station, this layer of water is normally pushed toward the trailing edge of the plate and tends to accumulate toward the trailing edge. As more water accumulates at the trailing edge, the water tends to flow back into the spray zone. The problem is especially severe at the trailing edge where water is retained by the edge of the plate. After reaching equilibrium thickness at the trailing edge, some of the water flows back into the spraying zone so that the glass plate is sprayed while it is covered with a thin film of water of non-uniform thickness.
  • finger-like waves of sprayed-0n solution form immediately downstream and immediately upstream of each spray station.
  • the deposition of solution begins prematurely in those areas of the sensitized sur- A the final coating.
  • the prior art recognized the existence of the problem of non-uniformity of coating, but failed to recognize the cause and therefore the solution.
  • a squeegee/- shield apparatus is installed immediately downstream of the first spray station. This apparatus prevents the formation of rear waves rearward of the apparatus and prohibits splashing of the solution onto the sensitized surface rearward of the apparatus, thereby eliminating any accumulation of solution at the trailing edge. In addition, it only permits a thin, uniform film of rinsing medium to pass beneath the spray station.
  • the location of the squeegee/shield apparatus relative to the surface to be coated and to the cone of dispensed rinsing medium is an important part of the present invention.
  • the squeegee must touch the sensitized glass surface so that no dispensed solution passes rear ward of the squeegee and only a thin, uniform layer of rinsing medium reaches the spray area. It must also cut off a portion of the spray fan to insure that initial contact with the glass surface is by fresh solution.
  • the squeegee should be placed so that it touches the tip of the spray fan, but since it is very impractical to maintain an exact relative positioning, the squeegee generally is positioned initially to overlap the spray fan by about one-fourth of an inch. If there is a gap between the spray fan and the squeegee, spent solution may contact the glass surface before fresh solution in random areas, causing coating defects. If the squeegee cuts off, for example, about 2 inches of the spray fan, too much spray solution drips down onto the sensitized surface from the squeegee, instead of being sprayed onto the surface.
  • the shield is above the squeegee to prevent splashing of the spray solution rearward onto the sensitized area before the sensitized surface reaches the dispensing station.
  • the squeegee may be made in the form of a lip seal of any soft, elastomeric material, such as natural rubber, neoprene, silicone rubber, and some plastic materials such as polyvinyl chloride. It is important to note that the material have a durometer of between about 50 and about 90, and preferably about 70. Certain plastics, such as polytetrafluoroethylene, have been proven to be too hard, therefore damaging the surface.
  • the squeegee is made in the form of a roller rather than a lip seal as previously described.
  • the roller can be, for example, 1 /2 inches in diameter and driven by friction at the sensitized surface.
  • the roller can be made of any soft, elastomeric material, however, a closed cell foam rubber over a steel tube has proved very desirable.
  • Coated glass made in accordance with the present invention, is capable of inhibiting transfer of radiant heat such as that from the suns rays by the light reflectance and absorption of the film and the fact that it permits transmittance of less than 35 to 40 percent of visible light from sunlight.
  • Panels having light transmittance of 5 to 25 percent are especially useful in warm to temperate climates such as the United States. In other climates such as Northern Europe, panels of greater transmittance are preferred.
  • the color of the panels is dependent upon the amount and composition of metal which is reduced.
  • Especially attractive nickel-boron and like metal-boron coatings which have a neutral color reflecting and passing essentially white light are provided according to the invention.
  • Cobalt coatings are blue while iron coatings are brown. Other colors can be obtained by producing mixtures of these coatings.
  • the nickel-boron and metal-boron compounds herein contemplated are usually electroconductive.
  • these films may be used as heating elements.
  • one such panel may be coated on its interior side by the process of this invention. By applying an electromotive force across this coating, heat may be generated in the panel, thus minimizing or preventing substantial heat loss from the interior of the building in which such windows are mounted.
  • Coatings having one or more of the desirable properties set forth above are effectively produced according to this invention by spraying, as hereinafter disclosed in greater detail.
  • Such a process is especially valuable in producing uniform coatings on large articles such as plates of glass or other substrates having one dimension in excess of 3 feet, with the other being in excess of 1.5 feet, for example, panels of 3 feet by 6 feet or larger.
  • Immersion processes have serious disadvantages. These disadvantages are especially acute where transparent coatings are desired since, for example, the composition of the plating bath changes during use, thereby requiring frequent chemical analysis and addition of materials to maintain a constant bath composition. If a constant bath composition is not maintained, the metal films formed thereon will not be uniform. In this latter connection, it should be appreciated that contamination of a bath composition, which may be caused, for example by an inadvertent admixture therewith of the solutions employed to activate the glass being coated, may necessitate a complete shut down of the process and a renewal of the bath. Furthermore, immersion processes are not especially adoptable to forming transparent films inasmuch as the rate of deposition is difficult to control. Thus, it is relatively common for a heavier coating to be deposited on that portion of the substrate which is first to enter and last to leave the plating bath.
  • Spraying a coating avoided the tapered coating thickness associated with dip coating in a plating bath.
  • the non-uniformity of appearance of transparent coatings in some frequency made it necessary to improve the coating operation.
  • FIG. I is a diagrammatic top plan view, with portions removed for the sake of clarity, of an apparatus suitable for carrying out the process of the present invention on a continual basis;
  • FIG. 2 is a diagrammatic front elevation of the apparatus of FIG. ll;
  • FIG. 3 is a diagrammatic partial perspective view of a glass loading and cleaning section of the apparatus of FIG. 1;
  • FIG. 4 is a diagrammatic partial perspective view of a sensitizing and activating section of the apparatus of FIG. 1;
  • FIG. 5 is a diagrammatic partial perspective view of a metal-boron deposition section of the apparatus of FIG. 1;
  • FIG. 6 is a diagrammatic partial perspective view of a drying section in the apparatus of FIG. 1;
  • FIG. 7 is a diagrammatic partial perspective view of a film density measuring and unloading section included in the apparatus of FIG. 1;
  • FIG. 8 is a diagrammatic top plan view of a metal solution-reducing solution dispensing spray gun set of a metal-boron deposition coating of the apparatus of FIG. 1, illustrating the disposition of spray guns in said set relative to each other and to an advancing glass substrate, and illustrating a fan-shaped pattern assumed by the respective solutions being sprayed;
  • FIG. 9 is a diagrammatic side elevational view of the coating apparatus illustrated in FIG. 8.
  • FIG. 10 is a diagrammatic front elevational view of the apparatus illustrated in FIG. 8;
  • FIG. llll is a diagrammatic perspective view of a metal-boron spray gun set without a squeegee/shield apparatus
  • FIG. 12 is a diagrammatic side cross-sectional view showing the details of a squeegee/shield apparatus made in accordance with a first embodiment of the present invention together with a spray gun;
  • FIG. 13 is a diagrammatic side cross-sectional view showing the details of a squeegee/shield apparatus made in accordance with a second embodiment of the present invention together with a spray gun;
  • FIG. I4 is a diagrammatic side cross-sectional view showing the details of a squeegee/shield apparatus made in accordance with a third embodiment of the present invention together with a spray gun;
  • FIG. 15 is a diagrammatic side cross-sectional view showing the details of a squeegee/shield apparatus made in accordance with a fourth embodiment of the present invention together with a spray gun.
  • the apparatus comprises five basic units or sections, which are designated a glass loading and cleaning section (section 100), a glass sensitizing and activating section (section 200), a metalboron coating composition deposition section (section 300), a glass drying section (section 400) and a film density measuring and glass unloading section (section 500).
  • the apparatus also comprises a conveyor means including a plurality of belts 1 in section 100 and rollers 2 in sections 200, 300, 400 and 500 for carrying and advancing glass plates 3 (FIGS. 1 to 7) past the various sections 100 to 500 along an article movement path in the direction of the arrows Y.
  • the belts 1 and the rollers 2 are rotated by conventional means (not shown) so as to advance the plates 3 at a rate of from about 0.5 to about 7 feet per minute, and preferably from about 3 to about 6 feet per minute.
  • a plurality of glass plates 3 are loaded onto the belts 1, so that the belts advance the plates into and through section 100 of the apparatus.
  • a plurality of rotating discs or blocks 101 gently abrade the uppermost surface of each plate, preferably with a mixture of cerium oxide or red rouge and water, to loosen and remove any dirt therefrom.
  • This blocking operation is preferably carried out with cattle hair felt blocks having a diameter of from about 4 to about 12 inches.
  • Each of the blocks is mounted on a shaft 102 which is rotated by a suitable motor 103 and gear means (not shown) at a rate of from about 200 to about 600 revolutions per minute.
  • the blocks are rotated at about 300 to about 500 revolutions per minute and are oscillated, for example, a distance of about 2 to 4 inches in a direction transverse to the direction Y of the advancing plate to insure that the entire uppermost surface of the plate is blocked.
  • each plate advances beneath a plurality of rotary cup brushes 104 that wash the surface of the plate with tap water.
  • the brushes 104 which may have nylon bristles or the like, are generally rotated at the same rate as the blocks 101, and are preferably oscillated in the same manner as well.
  • Each plate finally advances beneath a rotary cylinder brush 105 disposed across the advancing plate.
  • the brush 105 may comprise nylon bristles or the like which contact the plate and complete the cleaning thereof.
  • the brush is generally rotated at about 300 to about 400 revolutions per minute.
  • Both the rotary cup brushes 104 and the rotary cylinder brush 105 may be driven by conventional means such as motors (not shown) that may be similar to motors 103.
  • Each plate 3 then enters into and passes through section 200 of the apparatus, wherein the surface thereof is sensitized and then activated (super-sensitized).
  • the plate is subjected to a first rinse, preferably with demineralized water, as it enters section 200 to remove any traces of cerium oxide, red rouge, tap water or any other undesirable matter carried over from section 100.
  • the first rinse may be performed in any conventional manner.
  • the plate may be rinsed by reciprocating a single water spray apparatus transversely of the advancing plate, (i.e., in the direction of arrow X) while the plate advances in the direction indicated by arrow Y.
  • the rinse is preferably performed by employing a cross-fire technique.
  • a mutually opposed pair of pipes 201 and 202 are supported from a carriage 203 that reciprocates along the X axis on a track 204 at a rate of between about 25 and about single passes per minute, and preferably between about 45 and about 60 single passes per minute.
  • the carriage 203 is driven by a chain or belt 205 that runs over a pair of pulleys 206 and 207 arranged at the opposite ends of the track 204.
  • a motor 208 drives the chain 205 while a connection 205A between the chain and the carriage slides up and down in a vertical groove 2058 in the carriage 203 as the connection moves around the pulleys.
  • the drive construction is similar to that shown in Bramsen et al, US Pat. No. 2,246,502.
  • demineralized water is fed alternately to the pipes 201 and 202 in such a program that water is sprayed only from nozzles 201A, 2018 and 201C when the carriage is moving from left to right in FIG. 4, and only from nozzles 202A, 202B and 202C when the carriage is moving in the opposite direction.
  • the pipes 201 and 202 are supplied with water or other rinsing composition through lines 209 and 210, respectively, by any suitable means.
  • the pipes are advantageously operated at pressures between about 25 and about pounds per square inch, preferably between about 25 and about 45 pounds per square inch, and at flow rates of about 500 to about 600 milliliters per minute per pipe.
  • Valves V and V are illustrated as an example of suitable control means, either automatic or manual, that become apparent to one skilled in the art.
  • stannous chloride solution may comprise any of the formulations known in the art as being capable of sensitizing non-conductive substrates to metal deposition. However, a preferred formulation comprises from about 0.02 to about 1.0 gram of stannous chloride per liter of solution, together with a small amount of hydrochloride acid.
  • Such a solution may be prepared, for example, by mixing about 20 grams of stannous chloride and 2 to 3 milliliters of concentrated hydrochloric acid (12 N) in enough demineralized water to form one gallon of stock concentrate, and then diluting each part of the concentrate with about 19 parts of demineralized water.
  • about one part of the above-described concentrate is injected into a stream comprising about 19 parts of demineralized water, whereafter the combined stream is mixed with air at about 60 to about 80 pounds per square inch, and sprayed through the gun 211 in a highly atomized state at a rate of about 500 to about 700 milliliters per minute.
  • the stannous chloride composition dispensing spray gun 211 is supported from the same carriage 203 that supports the first rinse pipes 201 and 202.
  • a second set of rinse pipes 212 and 213, a palladium chloride composition dispensing spray gun 214 and a third set of rinse pipes 215 and 216 may also be supported from carriage 203.
  • the sheet 3 then passes under the gun 214 which sprays an atomized mixture of air and dilute palladium chloride on the now sensitized surface so as to activate (or super-sensitize) the surface for the ensuing metalboron deposition.
  • the palladium chloride may comprise any of the well-known formulations that are suitable for activating a previously sensitized substrate. However, a formulation comprising from about 0.005 to about 1.0 gram of palladium chloride per liter of solution, together with a small amount of hydrochloride acid, is preferred.
  • One such formulation may be prepared by mixing about 2 grams of palladium chloride and 2 to 3 milliliters of concentrated hydrochloric acid with a sufficient amount of demineralized water to form one gallon of concentrated stock solution, and then diluting each part of the stock solution with 19 parts of demineralized water.
  • the diluted palladium chloride is preferably mixed with air at a pressure of about 60 to about 80 pounds per square inch and sprayed onto the glass at a rate of about 500 to about 700 milliliters per minute.
  • the plate 3 After passing spray gun 214 and before leaving section 200 of the apparatus, the plate 3 undergoes a third demineralized water rinse. This rinse is carried out in the same manner as the first and second rinses, and is designed to remove any excess palladium chloride from the advancing plate before it reaches the metal-boron coating composition deposition section.
  • the spacing between the respective guns in section 200 of the apparatus may vary within wide limits depending, for example, upon the rate at which the plate 3 is advancing, the dimensions of the fan-shaped spray pattern generated by each gun, the rate of traverse of each gun, and the like. However, it is preferred to arrange the various guns in section 200 such that the time required for the leading edge of the given plate 3 to advance from each gun or set of guns to the next successive gun or sets of guns is from about to about 90 seconds.
  • the plate then passes from section 200 of the apparatus to section 300 thereof, wherein a metal and boron-containing coating, preferably nickelboron, cobalt-boron, iron-boron or a mixture of at least two of said metal-boron coatings is deposited on the now activated surface thereof.
  • a metal and boron-containing coating preferably nickelboron, cobalt-boron, iron-boron or a mixture of at least two of said metal-boron coatings is deposited on the now activated surface thereof.
  • the deposition is preferably accomplished by simultaneously spraying a metalcontaining solution and a boron-containing reducing solution from separate spray nozzles and intermixing said solutions onto the activated surface such that the metal ions present in the contemplated metal solution become reduced to a transparent boron-containing metal film which tenaciously adheres to the activated surface.
  • the spacing of the guns which spray the metal solution and the boron-containing reducing solution, and the rate at which they are reciprocated are determined generally by the rate at which the plate advances, the temperature, pH, and concentration of the intermixed film forming composition and the like, and primarily by the time required for the film forming composition to be substantially depleted in its film forming capacity, and the desired thickness and transparency of the deposited film. The importance of these latter two parameters will become more apparent in view of the illustrative example set forth below.
  • section 300 is shown in FIGS. 1, 2 and 5 as having two reciprocating spray gun sets 302 and 303, each comprising a first nozzle for dispensing a metal-containing solution, 302A and 303A, respectively, and an opposed second nozzle, 3028 and 30313, respectively, for dispensing a reducing solution.
  • Section 300 also includes a mutually opposed pair of reciprocating water pipes 304 and 305 arranged for cross-fire rinsing.
  • spray gun sets 302 and 303 are supported for transverse reciprocating movement, for example, in the manner described for reciprocating spray guns 211 and 2M in connection with FIG. 4.
  • the gun set in section 300 must reciprocate much faster than those in section 200 or than those employed in conventional spray techniques for depositing silver, for example.
  • uniformly and controllably transparent metal-boron coatings can best be made in accordance with the present invention only when the gun sets in section 300 are reciprocated at a rate of at least about 60 to about 65 single passes per minute, and preferably from about 72 to about 76 single passes per minute, when the plates being coated are about 4 feet wide and are advanced at a rate of from about 3 to about 6 feet per minute.
  • a spray gun set reciprocating at 74 single passes per minute will complete about 1.75 single passes over each inch segment of the advancing plate.
  • each inch segment of the plate will receive from about 17.5 to about 21.1 applications of solution per gun set.
  • the required number of passes per minute will vary somewhat in accordance with changes in magnitude of the various parameters discussed herein. For example, the required number of passes would increase when the plate being coated or advanced more rapidly than approximately 3 to approximately 6 feet per minute.
  • Spray guns of each set 302 and 303 are connected through respective supply lines (not shown) to air under pressure at about 20 to about 60 pounds per square inch.
  • the respective supply lines are in fluid communication with prepared metal and reducing solutions stored in separate solution tanks or containers (not shown), preferably of such size to hold a reasonable supply of fluid, such that when the prepared solutions are injected into the supply lines by any conventional means (not shown), the solutions are fed through the lines and aprayed from the guns in a fan-shaped pattern.
  • the magnitude of air pressure required for a satisfactory spray varies considerably with the design of the guns of the various parameters of the solutions employed. In this connection, satisfactory results have been obtained with pressures as low as about 20 pounds per square inch and as high as about 55 pounds per square inch. Pressures in the range of about 25 to about 40 pounds per square inch are preferred.
  • the rates at which the respective prepared solutions are sprayed from each gun may vary, but it is preferred that the rates of flow be maintained at about 300 to about 2,000 millimeters per minute per gun.
  • each of the nozzles 302A and 302B in the metal depositing spray gun set 302 is preferably designed to provide a substantially fan-shaped stream which opens only a few degrees in the direction transverse to the advancing plate, and which opens in the direction of travel of the plate such that the stream contacts the advancing plate in an elliptical pattern having a major diameter of from about 8 inches to about 14 inches, and preferably from about l inches to about 12 inches in length (FIG. 8).
  • Spray gun set 303 functions in the same manner.
  • each metal salt-reducing solution set are arranged to have an included angle of from about 80 to about 120 between the streams of composition they dispense.
  • each of the metal salt solution dispensing guns is inclined obliquely from the vertical about 40 to about 60 toward a mutually opposed reducing solution dispensing gun, and vise versa in a vertical plane common to the dispensing guns of the set (FIG. 10). This arrangement is desirable so that the metal and reducing solutions are effectively and thoroughly mixed as they approach and strike the surface of the activated glass plate.
  • FIG. 11 shows a metal-boron composition dispensing spray gun set 302 reciprocating along the X axis and applying solution to the transparent sheet 3 as said sheet travels along its article movement path Y.
  • set 302 produces a rear wave 306 and a front wave 307 on the surface of the glass sheet 3.
  • the rear wave comprises a mixture of fresh solution and spent solution containing precipitated nickel, decomposed reactants, rinsing medium and gas bubbles. This mixture reaches and covers the sensitized surface of the glass sheet 3 before the sheet reaches a position where its upper surface is sprayed with fresh solution from gun set 302.
  • the resultant coating does not possess uniform optical properties.
  • the boundary 308 of rear wave 306 does not extend across the sheet in a straight line. Rather, it extends transversely of article movement path Y in a finger-like pattern, causing non-uniform surface coverage and, therefore, streaks in the final coating.
  • the amount of old solution per unit area of glass sheet covered and the age of the old solution is not uniform for all portions of the rear wave 306. This non-uniformity of amount and age of coating manifests itself in inhomogeneities in the resulting film.
  • Front wave 307 is principally composed of spent so lution and rinsing medium. In the case of any front wave, spent solution is contacting the surface of a substrate after fresh solution has been applied. Since spent solution does not adhere as readily to a metal surface as it does to a glass surface, front wave 307 does not affect the unifonnity of the finished coating to the extent that rear wave 306 affects it.
  • front and rear refer to the direction of movement of glass sheets along the article movement path as defined by the direction of arrow Y.
  • upstream and downstream to define the direction of glass sheets along the article movement path. The sheets are presumed to travel in a downstream direction.
  • rear wave 306 has been completely eliminated and front wave 307 has been reduced in size by the use of a stationary squeegee/shield apparatus 301 immediately upstream of the first spray gun set 302, as shown in FIG. 5.
  • the squeegee/shield apparatus 301 extends in direction X that is transverse to the article movement path Y, and it functions to control the thickness of rinse water remaining on the surface of sheet 3 from rinse pipes 215 and 216 to form a water film of uniform thickness on the glass surface when said sheet 3 and said spray gun set 302 are in alignment, while avoiding the formation of finger-like waves of solution upstream of said spray gun set.
  • the squeegee/shield apparatus is stationary and does not reciprocate along the X axis.
  • Squeegee/shield 301A includes a splash shield 310 and a squeegee 312 mounted beneath splash shield 310.
  • Squeegee 312 comprises, for example, a loop made of soft rubber approximately 0.0l0 inch thick. The loop forms a lip portion 314 that engages the coated upper sensitized surface of each moving sheet of glass 3 that enters a spraying station.
  • Squeegee 312 is held in place beneath shield 310 by any suitable means, such as, for example, an angular plate 316 which is bolted to a flange 318.
  • the squeegee is made of an elastomeric material having a durometer hardness of from about 50 to about 90, and preferably about 70. Examples of suitable materials are: natural rubber, neoprene, silicone rubber and plasticized polyvinyl chloride. Stiff plastics such as Teflon, Mylar, Lexan and many polycarbonates tend to scratch the sensitized surface.
  • Shield 310 and squeegee 312 prevent the spray-fan M from gun set 302 from splashing onto the galss surface and congragating in an upstream area 320 of set 302. Squeegee 312 prevents any of the spray M from flowing beneath shield 310 to upstream area 320. Together, the shield 310 and the squeegee 312 eliminate the rear wave and its assoiated problems.
  • Shield 310 may be constructed of any material that is capable of adding structural integrity to the apparatus 301 and is not attacked by the spray-fan M.
  • Stainless steel is an example of a meterial suitable for use with a nickel-boron spray.
  • the squeegee could be extended upward to replace the shield and perform its splash prevention function, as long as some measure is taken to add structural integrity to the apparatus. This could be done by, for example, reinforcing the upper portion of the squeegee or varying its thickness so that is is is thicker, and therefore stronger, at its upper portion.
  • the squeegee 312 and particularly lip portion 314 performs two additional functions. Some of the rinse water from pipes 215 and 216 remains on the glass sheet 3 in a random manner as it approaches gun set 302 along the article movement path Y. If this rinse water is allowed to sit on the glass surface beneath gun set 302, there will be a non-uniform dilution of the spray solution and a coating with inferior optical properties will result.
  • Lip portion 314 acts as a wiper to insure that no puddles of rinse water pass beneath gun set 302. It allows only a thin uniform rinsing fllm of from about 0.03 inch to about 0.10 inch, and preferably about 0.05 inch, to sit on the glass beneath the coating station.
  • lip 314 is positioned so that it slightly overlaps the side edge 309 of spray-fan M by about one-eighth or about one-fourth of an inch at the upper glass surface to intercept a portion of spray M.
  • the tip of lip 314 should just touch the side edge of spray-fan M to insure that fresh spray solution contacts the glass surface first, but it is impractical to maintain this relationship with precision. If the squeegee is positioned so that lip 314 does not either touch the side edge or intercept a portion of spray-fan M, spent solution may contact the glass surface in random areas before fresh solution contacts the surface in those areas and a coating having non-uniform optical properties may result.
  • FIG. 13 shows a squeegee/shield 3013 including a squeegee 322 comprising a thin plastic reinforcement 324 enclosed within a looped elastomeric covering 326.
  • the covering 326 may be made, for example, of soft material, similar to the ones described in connection with squeegee 312.
  • the reinforcement 324 can be made, for example, of polyvinyl butyral, approximately 0.030 inch thick.
  • the squeegee comprises a curtain 322 approximately three-fourths of an inch to 1 inches long and approximately 0.007 to approximately 0.040 inch thick, hanging freely from splash shield 310.
  • the curtain 332 may be made of any of the suitable materials descirbed above in connection with squeegee 312.
  • the squeegee is in the form of a roller 340, driven by friction at the sensitized surface. It is possible to drive roller 340, but this is unnecessary and can lead to complications if roller 340 is not driven at the exact speed as the rollers 2 beneath the glass sheet 3.
  • the roller may be made of any of the abovementioned squeegee materials, but is preferably made of closed cell foam rubber. Enclosed within the foam rubber is a metallic tube 342.
  • Shield 3344 includes a sheet 346 and rods 348 with ribs 350 connecting the sheet to the rods.
  • Axle 352 is rotatably connected to the base of rods 348and roller 340 rotates about axle 352.
  • the squeegee operates to perform the functions described in connection with the embodiment of FIG. 12.
  • a subsequent spray gun set appears to be able to sweep the spent solution from the surface of substrate 3 without damaging the prior coating. This can be explained by the fact that the spent solution does not adhere as readily to the fresh coating as it does to sensitized glass. Therefore, the use of squeegee/shield apparatus after the first spray gun set is unnecessary and even undesirable.
  • the shields 310 and 344 have been illustrated as being oriented at an angle of about 30 with the verti cal, but this angle is not critical. Actually, the shield may even lie within a vertically extending plane. By tilting the shield to an angle of from about 15 to about 50 with the vertical, the top portion of the shield is spaced from gun set 302 to make gun set 302 more accessible.
  • the intermixed film forming composition which is uniformly distributed on the surface of the plate is permitted to rest relatively quietly.
  • This quiescent period or period of minimum turbulence is highly desirable since it enables the film forming composition to deposit a transparent coating which is substantially free from visual defects normally attributed to turbulence or agitation of the filming composition during deposition.
  • the intermixed filming compositions comtemplated herein undergo a change in their capacity for depositing a film such that the rate of film deposition, which is initially relatively rapid, decreases and then effectively completely ceases while the deposited film is still transparent.
  • a filming composition comprising equal amounts of the nickel acetate solution and borohydride reducing solution, illustrated respectively in Tables I and II of US. Pat. application Ser. No. 57,451, will normally undergo a substantial decrease in its filming capacity within from about 10 seconds to a few minutes, e.g., 5 minutes.
  • a glass plate that is coated with a metal and boron-containing film at room temperature by a single 15; second spray application of the above illustrated intermixing filming composition will normally have a luminous transmission of from about 30 to about 40 percent when the filming capacity of the composition has depleted and filming has effectively ceased.
  • the film forming composition may be removed from the plate by any convenient means without affecting the thickness, and thus the transparency of the film. It will also be appreciated tha the lowest degree of transparency obtainable will depend primarily upon the amount of film that will deposit from a given film forming composition before it becomes dead, the number of gun sets in section 300, and the distance between each gun set. The effect of these variables on the thickness, uniformity and transparency of the metal-boron films formed in accordance with this invention will be more fully appreciated in light of the example recited hereinbelow.
  • the plate After undergoing the quiescent period after its exposure to the mixed composition dispensed by spray gun set 303, the plate has a luminous transmittance of about 15 to 25 percent. If a third apray gun set is used (not illustrated), a luminous transmittance of as little as 10 percent may be obtained. Each additional gun provide a quiescent period designed to allow the partially formed metal-boron film to increase in thickness uniformly in the substantial absence of adverse effects caused by turbulence.
  • this period is designed to allow sufficient time for the film forming composition on the surface of the plate to become substantially depleted of its film-forming capacity so that the rate of deposition of the metal-boron film will have materially slowed down, and preferably effectively ceased, before the plate is rinsed under pipes 304 and 305.
  • the necessary distance between pipes 304 and 305 and the last metal depositing gun set 303 is related to the rate at which the plate is advanced.
  • the distance between the final rinse pipes 304 and 305 and the last spray gun set 303 should be at least about 30 inches, and preferably at least about 35 to 40 inches to provide a final film thickness corresponding to a luminous transmittance of about 20 percent.
  • the plate 3 After undergoing a final water rinse under rinse pipes 304 and 305, the plate 3 advances into section 400 of the coating apparatus where it is dried by means of a suitable air knife 401 (FIG. 6).
  • the air knife 401 may comprise any conventional blow-off device, but it is preferred to employ a high volume-low pressure knife to avoid disturbing the quality of the metal-boron film. For example, it is desirable to employ a knife that operates at a pressure of about 3 to 7 ounces per square inch, while forcing from about 300 to about 400 cubic feet of air per minute against the metal-boron coated glass plate.
  • the completed metal-boron coated plate After passing beneath the air knife, the completed metal-boron coated plate passes into section 500 where the thickness of the deposited film is measured by a conventional measuring device 501. Thereafter, the transparent glass plate is removed from the rollers 2 and is ready for use.
  • the present invention is applicable in forming transparent metal-boron films on clear plastic (e.g. polymethyl methacrylate) and glasses, especially soda-limesilica glasses, but can be used to film a wide variety of glass, ceramic, glass-ceramic, siliceous and calcareous based compositions.
  • this invention can be used to provide metal-boron and particularly nickelboron films on the following types of glasses: soda-limesilica glasses; alkali-alumina-silica glasses, such as those containing lithia as a component alkali; aIkali-zirconiasilica glasses; alkali-alumina-zirconia-silica glasses; brosilicate glasses, etc.
  • soda-limesilica glasses alkali-alumina-silica glasses, such as those containing lithia as a component alkali
  • aIkali-zirconiasilica glasses alkali-alumina-zirconia-silica glasses
  • brosilicate glasses etc.
  • the soda-lime-silica glass to be treated can be a clear glass or it can be a colored glass tinted by the introduction or various conventional materials into the glass forming batch. These latter glasses are often referred to as heat absorbing glasses especially when they contain iron oxide.
  • Representative soda-lime-silica glass bases which can be treated in accordance with this invention usually contain 65 to 75 percent by weight SiO 10 to l8 percent by weight Na O, 5 to percent by weight CaO, l to 5 percent by weight MgO, 0 to 1.0 percent by weight Na SO 0 to 5 percent by weight aluminum oxide (M 0 0 to 8 percent by weight K 0, 0 to 8 percent by weight B O O to 1 percent by weight iron oxide (Fe o and 0 to 0.7 percent by weight of NaCl, S0 A5 0 BaO, NiO, C00 and Se and combinations thereof.
  • compositions for sode-limesilica glasses are listed as follows (wherein the given amounts of metals listed are determined as their oxides, except as otherwise noted):
  • EXAMPLE A 40 inch X 70 inch X A commercial soda-lime-silica glass plate is coated with a nickel-boron film with the apparatus illustrated schematically in FIG. 1.
  • Four blockers are used, each comprising a 3-inch thick cattle hair felt disc of 8-inch diameter.
  • the blockers are arranged at l2-inch centers in the direction parallel to the rollers, hereafter referred to as the transverse direction, and are rotated at about 350 revolutions per minute.
  • the blockers are oscillated about 4 inches in the transverse direction at a frequency of about 15 cycles per minute.
  • Four 6-inch diameter rotary cup brushes are arranged at 12-inch centers in a transverse direction such that the longitudinal distance between the blockers argthe rotary cup brushes is about 9 inches.
  • the rotary cup brushes are equipped with No.
  • the rotary cylinder brush has a 6-inch diameter, comprising No. 12 nylon bristles, and has its axis disposed 8 inches from the rotary cup brushes.
  • the first, second and third rinse sets, as well as the tin composition dispensing gun and the palladium composition dispensing gun, i.e., all of the rinse sets and the guns in section 200, are mounted from a single boom that reciprocates in a transverse direction at a rate of about 45 single passes per minute.
  • Each of the rinse nozzles comprises a single UniJet-T8002 spray noule (manufactured by Spraying Systems Company, Dellwood, Ill.) and is operated at a pressure of about 40 pounds per square inch, at an average flow rate of about 0.2 gallon of demineralized water per minute.
  • Each of the tin and palladium composition dispensing guns comprises a single, type C, spray gun equipped with a Paasche U2, F2-8 nozzle, manufactured by Paasche Air Brush Company, Chicago, Ill., and operated at an air pressure of about 70 pounds per square inch and a flow rate of about 500 milliliters of the solution described below per minute.
  • the distance between the rotary cylinder brush and the first rinse pipes 201 and 202 is about 30 feet, while the distance from each gun to the next successive gun is about feet.
  • the gun sets in section 300 of the apparatus are spaced apart from those in section 200 such that the distance between rinse pipes 215 and 216 and gun set 302 is about feet.
  • gun set 302 is spaced about 3 feet from gun set 303.
  • the distance between the tip of the gun dispensing nickel solution and the tip of the gun dispensing reducing solution in each respective set is about 10 inches.
  • All of the guns in section 300 employlaasche U2, F2-8 nozzles, which are arranged so that the tip of each nozzle is about 7 inches above the surface of the glass being coated, and so that each respective gun set generates a fan-shaped stream of intermixed film forming solution that contacts the glass surface in a generally elliptical pattern having a major diameter of about 1 1 inches extending in a longitudinal direction. All of the rinse sets and the spray guns in section 300 are mounted from a single boom that reciprocates in the transverse direction at a rate of about 72 passes per minute which is equal to 36 round trips per minute.
  • each of the metal deposition gun sets in section 300 is maintained at a pressure of about 40 pounds per square inch and a flow rate of about 800 milliliters of solution per minute, while the final cross-fire rinse pipes 304 and 305 are operated at a pressure of about 40 pounds per square inch at an average flow rate of about 0.2 gallon of demineralized water per minute per nozzle.
  • the distance between rinse pipes 304 and 305 and the last metal depositing gun set 303 is about 70 inches.
  • the air knife 401 comprises an elongated metal housing having a 0.002-inch wide delivery slot extending along the length of its bottom wall.
  • the knife 401 is disposed at a 45 angle relative to the advancing plate and had its centermost portion spaced about 8 feet from the final rinse pipes 304 and 305.
  • the air knife is operated at about 5 ounces per square inch and at a flow rate of about 350 cubic feet per minute.
  • the ambient air temperature is about 82F., while the temperature of the demineralized and tap water used throughout this example is about 63F.
  • the glass plate is advanced at a rate of about 5 feet per minute, while the slot opening of the air knife is spaced about one-half inch from the plate.
  • each of the prepared aqueous solutions employed has the following composition:
  • Ethomeen C-20* 0.06 grams Etl'iBin eQH C-ZO (trademark of Armour and Company) is a cocoamine having an average molecular weight of 645 and the following generalized formula:
  • R is derived from a cocoamine and x y 10.
  • An apparatus for coating :1 surface of an article having a liquid medium on said surface comprising:
  • An apparatus for coating a surface of an article comprising:
  • said last named means being located along the path of movement of said article toward said secondnamed means and downstream with respect to said first-named means, and being positioned so as to intercept a portion of the spray of the coating composition applied to said surface of said article.
  • said means for maintaining the thickness of said film of liquid rising medium substantially uniform comprises a squeegee disposed between said means for applying a 0.02 gram 0.04 milliliter liquid rinsing medium and said means for applying a spray of a coating composition.
  • said squeegee reinforcing means comprises a shield disposed in spaced relation above said surface and made of a material that is not attacked by said composition, said squeegee being attached thereto to extend downwardly therefrom.
  • said means for applying a spray of a coating composition to the surface of said article comprises a spray gun for applying a fan-shaped spray of said coating composition in a direction extending toward said surface and located in a position relative to said squeegee that said squeegee intercepts a portion of said fan-shaped spray directed toward said surface.
  • roller is constructed of closed cell foam rubber.
  • An apparatus for coating a surface of an article comprising:
  • a first-named means for applying a sensitizing composition to the surface of an article to be coated
  • said means for maintaining the thickness of said film of liquid rinsing medium substantially uniform comprises a squeegee disposed between said means for applying a liquid rinsing medium and said means for applying a spray of a coating composition.
  • said squeegee reinforcing means comprises a shield disposed in spaced relation above said surface and made of a material that is not attacked by said composition, said squeegee being attached thereto to extend downwardly therefrom.
  • said means for applying a spray of a coating composition to the surface of said article comprises a spray gun for applying a fan-shaped spray of said coating composition in a direction extending toward said surface and located in a position relative to said squeegee that said squeegeeintercepts a portion of said fan-shaped spray directed toward said surface.

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Abstract

A transparent substrate to be spray coated passes beneath a squeegee/shield apparatus to avoid formation of finger-like fronts or puddles in the spray area and to prevent splashing of the spray medium onto the substrate surface. The squeegee/shield element functions to doctor a prior applied coating while intercepting of portion of the subsequent spray stream.

Description

afignt 19 11] 3,782,328
Franz Jan. 11, 1974 SQUEEGEE /SHIELD 2,356,66 8/1944 Hamilton 118 117 ux 2,489,985 11 1949 Speight, Jr.. 118/117 ux [75] Inventor- Helm Franz pttsburgh 2,733,172 H1956 Brennan 118/301 x 73 Assigneez PPG Industries Inc. Pittsburgh 2,800,874 7/1957 Leslie 1 1 18/504 X 3,198,650 8/1965 St111ey et a1 118/504 x [22] Filed: Jan. 18, 1973 3,407,428 10/1968 Galassi 15/251551 [21] Appl. No.: 324,730
Related US. Application Data Division of Ser. No. 159,747, July 6, 1'971.
11.8). CI l18/118,118/123,118/301 Int. Cl. B05c 11/04 Field of Search 118/504, 505,. 301,
R, 64 C; l5/256.5256.53
References Cited UNITED STATES PATENTS 7/1934 Roberts 118/301 Primary ExaminerMorris Kaplan Attorney-E. Kears Pollock [57] ABSTRACT A transparent substrate to be spray coated passes beneath a squeegee/shield apparatus to avoid formation of finger-like fronts or puddles in the spray area and to prevent splashing of the spray medium onto the substrate surface. The squeegee/shield element functions to doctor a prior applied coating while intercepting of portion of the subsequent spray stream.
23 Claims, 15 Drawing Figures PAIENIEBJAN nm 3. 782.328
sum 2 or '4 4 I go! 028 ZOZA Y 20m Zola PAIENIE JAM H974 SHEEI 3 (If 4 FIG-l6 FIG.
1 SQUEEGEE ISHHIELD (.ROSS REFERENCES TO RHLA'II'ZD APPLICATIONS This is a division, of application Ser. No. 159,747, filed July 6, 1971.
This application is related to U.S. Pat. application Ser. No. 829,705, filed in the names of Richard G. Miller et a]. on June 2, 1969, and entitled Electroless Process for Forming Thin Metal Films", now U.S. Pat. No. 3,671,291. This application is also related to U.S. Pat. application Ser. No. 829,755, filed on June 2, 1969, in the name of Richard G. Miller, and entitled Electroless Process for Forming Thin Metal Films, now U.S. Pat. No. 3,672,939. This application is also related to U.S. Pat. applications Ser. Nos. 57,451, 57,575, which is now abandoned and 57,754, filed on July 23, 1970, in the name of Richard G. Miller, and entitled Wet Chemical Method for Producing Transparent Metal Films, now U.S. Pat. No. 3,674,517, Transparent Metal-Boron Coated Glass Articles and Solution for Depositing Transparent Metal Films, respectively, and U.S. Pat. application Ser. No. 57,527 of Charles B. Greenberg et al, filed on July 23, 1970, for Wet Chemical Method for Producing Transparent Metal Films and now U.S. Pat. No. 3,723,155. This application is also related to U.S. Pat. application Ser. No. 111,903, filed on Feb. 2, 1971, in the name of Helmut Franz et al. and entitled Chemical Filming Solution and Process for Plating Therewith and now U.S. Pat. No. 3,738,867. This application is also related to U.S. Pat. application Ser. No. 130,468, filed on Apr. 1, 1971 in the name of Helmut Franz, and entitled Removal of Metal Containing Deposits from Non-Metallic Substrates.
BACKGROUND OF THE INVENTION 1. Field of the Invention: This invention relates to an apparatus for providing non-conductive transparent substrates with transparent coatings having optical properties of good uniformity, and particularly relates to a squeegee/shield apparatus that avoids sources of non-uniformity of said optical properties.
2. Description of the Prior Art: In the past, transparent metal coated glass articles have been produced by various vapor deposition techniques which generally involve the deposition, from the vapor phase, of substantially pure metals, such as nickel or chromium on a prepared glass substrate. However, while such techniques are generally capable of providing metal films of acceptably uniform thickness and specified -visual transparency, commercial films of this type have been observed to possess an undesirably high number of visible pin-holes. Further, this process is expensive and complex. Metal coated metallic and non-metallic articles have been produced by various well-known electroless or chemical plating techniques. These techniques generally involve the immersion of a metallic article or a sensitized non-metallic article into a suitable electroless plating bath comprising an aqueous medium having dissolved therein a metal salt and an appropriate reducing agent, whereupon a metal film is deposited upon the immersed article by an autocatalytic mechanism.
The electroless process is an old and established one. For example, Brenner and Riddell disclosed in 1944 that an opaque coating of nickel could be autocatalytically deposited upon metallic substrates by immersing the substrates into a nickel salt solution containing sodium hypophosphite. U.S. Pat. Nos. 2,532,283 and 2,532,284 were issued to Brenner and Riddell upon their discoveries. The use of sodium hypophosphite as the reducing agent results in deposits which are not pure metal, but which contain about 2 to 10 percent elemental phosphorous by weight. In this connection, it is known that the presence of phosphorous in a deposited nickel film affects certain of the film characteristics, including its dominant wave lengths, infrared absorption characteristics, excitation purity and electroconductivity. In addition, and for reasons not wholly understood, it has been found that the uniformity of deposited nickel-phosphorous films generally decreases rapidly with increased thickness when the thickness of the coated glass substrates is greater than about threesixteenths of an inch.
Other electroless immersion plating processes involve the use of boron-containing reducing agents which are effective at room temperature. U.S. Pat. Nos. 2,968,578, 3,140,188, 3,096,182 and 3,045,334 are representative of improved electroless plating processes of this type. U.S. Pat. No. 2,956,600, issued to Carlson et al, describes a spraying process wherein two separate solutions are sprayed upon substrates to form nickel coatings. This process uses sodium hydrosulfite and sodium hypophosphite as a reducing agent.
To a large extent the prior art has been concerned with production of opaque coatings by electroless coating, although it is understood that the assignee of U.S. Pat. No. 2,702,253 produces a glass plate having a transparent nickel coating possibly by the process therein disclosed. The problem of producing transparent glass or like articles is much more difficult because relatively minute variations in thickness are readily visible to the naked eye as unsightly defects. Other variations in such coatings can provide streaks with a glass region appearing almost opaque due to reflection of light in an otherwise transparent glass plate.
Many solutions suggested by the prior art develop a coating of gradually increasing thickness well beyondthicknesses which are opaque. The production of uniform transparent films with such solutions is especially difficult.
U.S. application Ser. No. 57,451, filed on July 23, 1970, in the name of Richard G. Miller, teaches a method whereby transparent substrates such as glass are provided with a uniform transparent coating by contacting the glass simultaneously with a mixture of a reducible metal salt in a solution and a reducing agent, which mixture becomes rapidly depleted of its film forming capacity before the resulting coating becomes opaque. This produces a uniform coating at a rate which is relatively rapid and then relatively slower and which effectively ceases to produce coating while the coating remains transparent. According to said application, it has been found that by using such mixtures and discontinuing the contact therewith after the rate of deposition of coating has reached the slower rate, transparent films of improved uniformity with few pin-holes can be achieved. The application further states that coatings of the best uniformity may be obtained even with large plates having four or more square feet of surface when the coating is applied by separately spraying a solution of reducing agent and a solution of the reducible metal salt on the glass plate preferably while the major surfaces thereof are in a horizontal or substantially horizontal plane. The process has been found to be effective over a broad temperature range for coating any of the so-cnlled catalytic metal substrates or non-catalytic substrates sensitized in a conventional manner to promote deposition of continuous, adherent transparent metal films. An advantage of the process is that it will deposit highly uniform transparent films when performed at about room temperature, i.e., from about 20C. to about 30C. The application further states that in order to insure that each of a plurality of substrates is provided with a coating that exhibits substantially the same physical and chemical characteristics, it is advantageous that the process temperature be held constant to within about :t 1C., for example, over 100 substrates or over 1,000 square feet of substrates, or the like. Best uniformity and appearance of transparent films is achieved when films are deposited to a thickness having a luminous transmission of about 35 to 40 percent or less, and when the films comprise nickel-boron, cobalt-boron, iron-boron, and the like. Films comprising mixtures of boron and nickel, cobalt and/or iron may also be provided. In all such films, the boron is present in a minor amount (rarely exceeding about percent by weight and normally between about 2 and 7 percent by weight) while the metal (nickel, cobalt and/or iron) is present in preponderant amounts (rarely less than 85 percent by weight and normally between about 93 and 98 percent by weight).
The transparent substrates obtained in accordance with the last-mentioned process may be employed, for example, as transparent windows or outside walls in a building such as a skyscraper or other multistory structure. These substrates may be especially advantageously employed as one of the plates which make up multiglazed units as described in the previously mentioned U.S. patent application Ser. No. 57,575, now abandoned. It will be understood that uniformity of coating in such uses is especially important because otherwise the reflected color of portions of the building differs sharply from that of other portions, thus distracting from its appearance.
To generalize, the prior art teaches a process whereby glass plates are conveyed along an article movement path through a sequence of rinse and spray stations. After a plate leaves a rince station, it is normally covered with a layer of water. When the plate enters a spray station, this layer of water is normally pushed toward the trailing edge of the plate and tends to accumulate toward the trailing edge. As more water accumulates at the trailing edge, the water tends to flow back into the spray zone. The problem is especially severe at the trailing edge where water is retained by the edge of the plate. After reaching equilibrium thickness at the trailing edge, some of the water flows back into the spraying zone so that the glass plate is sprayed while it is covered with a thin film of water of non-uniform thickness. As a result, there is an uneven dilution of the sprayed-on solutions in the sensitizing and coating stations, and this causes the coating on the plate to vary in thickness, in absorption and in reflectance. This is extremely pronounced adjacent to the trailing edge of the plate.
In addition, finger-like waves of sprayed-0n solution form immediately downstream and immediately upstream of each spray station. The deposition of solution begins prematurely in those areas of the sensitized sur- A the final coating. The prior art recognized the existence of the problem of non-uniformity of coating, but failed to recognize the cause and therefore the solution.
SUMMARY OF THE INVENTION It has now been discovered that the manner in which the solution contacts the sensitized glass surface is extremely critical, if a uniform coating is to be obtained. Optimum film quality is obtained when the first contact is made by fresh spray solution. The solution cannot be permitted to flow back onto the sensitized area or the glass surface will be covered non-uniformly by a mixture of fresh solution and spent solution, causing banding and streaking defects in the final coating. The solution cannot be permitted to accumulate at the trailing edge of the plate or defects will be most pronounced in this area. In addition, rinse water cannot be permitted to flow back into the spray zone in an uneven fashion or an uneven dilution of the solution (and therefore an uneven coating) will result.
According to the present invention, a squeegee/- shield apparatus is installed immediately downstream of the first spray station. This apparatus prevents the formation of rear waves rearward of the apparatus and prohibits splashing of the solution onto the sensitized surface rearward of the apparatus, thereby eliminating any accumulation of solution at the trailing edge. In addition, it only permits a thin, uniform film of rinsing medium to pass beneath the spray station.
The location of the squeegee/shield apparatus relative to the surface to be coated and to the cone of dispensed rinsing medium is an important part of the present invention. The squeegee must touch the sensitized glass surface so that no dispensed solution passes rear ward of the squeegee and only a thin, uniform layer of rinsing medium reaches the spray area. It must also cut off a portion of the spray fan to insure that initial contact with the glass surface is by fresh solution. Ideally, the squeegee should be placed so that it touches the tip of the spray fan, but since it is very impractical to maintain an exact relative positioning, the squeegee generally is positioned initially to overlap the spray fan by about one-fourth of an inch. If there is a gap between the spray fan and the squeegee, spent solution may contact the glass surface before fresh solution in random areas, causing coating defects. If the squeegee cuts off, for example, about 2 inches of the spray fan, too much spray solution drips down onto the sensitized surface from the squeegee, instead of being sprayed onto the surface. The shield is above the squeegee to prevent splashing of the spray solution rearward onto the sensitized area before the sensitized surface reaches the dispensing station.
The squeegee may be made in the form of a lip seal of any soft, elastomeric material, such as natural rubber, neoprene, silicone rubber, and some plastic materials such as polyvinyl chloride. It is important to note that the material have a durometer of between about 50 and about 90, and preferably about 70. Certain plastics, such as polytetrafluoroethylene, have been proven to be too hard, therefore damaging the surface.
In another embodiment of the present invention, the squeegee is made in the form of a roller rather than a lip seal as previously described. The roller can be, for example, 1 /2 inches in diameter and driven by friction at the sensitized surface. As in the case of the lip seal, the roller can be made of any soft, elastomeric material, however, a closed cell foam rubber over a steel tube has proved very desirable.
Coated glass, made in accordance with the present invention, is capable of inhibiting transfer of radiant heat such as that from the suns rays by the light reflectance and absorption of the film and the fact that it permits transmittance of less than 35 to 40 percent of visible light from sunlight. Panels having light transmittance of 5 to 25 percent are especially useful in warm to temperate climates such as the United States. In other climates such as Northern Europe, panels of greater transmittance are preferred.
The color of the panels is dependent upon the amount and composition of metal which is reduced. Especially attractive nickel-boron and like metal-boron coatings which have a neutral color reflecting and passing essentially white light are provided according to the invention. Cobalt coatings are blue while iron coatings are brown. Other colors can be obtained by producing mixtures of these coatings.
The nickel-boron and metal-boron compounds herein contemplated are usually electroconductive.
Thus, these films may be used as heating elements. For
example, in a double-glazed window comprising twospaced glass panels enclosed by a glass, metal or organic sealing around the edge of the panel, one such panel may be coated on its interior side by the process of this invention. By applying an electromotive force across this coating, heat may be generated in the panel, thus minimizing or preventing substantial heat loss from the interior of the building in which such windows are mounted.
Coatings having one or more of the desirable properties set forth above are effectively produced according to this invention by spraying, as hereinafter disclosed in greater detail. Such a process is especially valuable in producing uniform coatings on large articles such as plates of glass or other substrates having one dimension in excess of 3 feet, with the other being in excess of 1.5 feet, for example, panels of 3 feet by 6 feet or larger.
Immersion processes have serious disadvantages. These disadvantages are especially acute where transparent coatings are desired since, for example, the composition of the plating bath changes during use, thereby requiring frequent chemical analysis and addition of materials to maintain a constant bath composition. If a constant bath composition is not maintained, the metal films formed thereon will not be uniform. In this latter connection, it should be appreciated that contamination of a bath composition, which may be caused, for example by an inadvertent admixture therewith of the solutions employed to activate the glass being coated, may necessitate a complete shut down of the process and a renewal of the bath. Furthermore, immersion processes are not especially adoptable to forming transparent films inasmuch as the rate of deposition is difficult to control. Thus, it is relatively common for a heavier coating to be deposited on that portion of the substrate which is first to enter and last to leave the plating bath.
Spraying a coating avoided the tapered coating thickness associated with dip coating in a plating bath. However, prior to the present invention, the non-uniformity of appearance of transparent coatings in some frequency made it necessary to improve the coating operation.
DESCRIPTION OF THE DRAWINGS A complete understanding of the invention may be obtained from the foregoing recital of the prior art and following description of an illustrative embodiment of the present invention, taken together with the appended drawings, in which:
FIG. I is a diagrammatic top plan view, with portions removed for the sake of clarity, of an apparatus suitable for carrying out the process of the present invention on a continual basis;
FIG. 2 is a diagrammatic front elevation of the apparatus of FIG. ll;
FIG. 3 is a diagrammatic partial perspective view of a glass loading and cleaning section of the apparatus of FIG. 1;
FIG. 4 is a diagrammatic partial perspective view of a sensitizing and activating section of the apparatus of FIG. 1;
FIG. 5 is a diagrammatic partial perspective view of a metal-boron deposition section of the apparatus of FIG. 1;
FIG. 6 is a diagrammatic partial perspective view of a drying section in the apparatus of FIG. 1;
FIG. 7 is a diagrammatic partial perspective view of a film density measuring and unloading section included in the apparatus of FIG. 1;
FIG. 8 is a diagrammatic top plan view of a metal solution-reducing solution dispensing spray gun set of a metal-boron deposition coating of the apparatus of FIG. 1, illustrating the disposition of spray guns in said set relative to each other and to an advancing glass substrate, and illustrating a fan-shaped pattern assumed by the respective solutions being sprayed;
FIG. 9 is a diagrammatic side elevational view of the coating apparatus illustrated in FIG. 8;
FIG. 10 is a diagrammatic front elevational view of the apparatus illustrated in FIG. 8;
FIG. llll is a diagrammatic perspective view of a metal-boron spray gun set without a squeegee/shield apparatus;
FIG. 12 is a diagrammatic side cross-sectional view showing the details of a squeegee/shield apparatus made in accordance with a first embodiment of the present invention together with a spray gun;
FIG. 13 is a diagrammatic side cross-sectional view showing the details of a squeegee/shield apparatus made in accordance with a second embodiment of the present invention together with a spray gun;
FIG. I4 is a diagrammatic side cross-sectional view showing the details of a squeegee/shield apparatus made in accordance with a third embodiment of the present invention together with a spray gun; and
FIG. 15 is a diagrammatic side cross-sectional view showing the details of a squeegee/shield apparatus made in accordance with a fourth embodiment of the present invention together with a spray gun.
DESCRIPTION OF THE PREFERRED EMBODIMENT Referring to the drawings, there are shown several embodiments of an apparatus suitable for coating a monolithic substrate, such as a glass plate, with a transparent metal and boron-containing film of superior uniformity of film appearance in accordance with the present invention. As shown, the apparatus comprises five basic units or sections, which are designated a glass loading and cleaning section (section 100), a glass sensitizing and activating section (section 200), a metalboron coating composition deposition section (section 300), a glass drying section (section 400) and a film density measuring and glass unloading section (section 500). The apparatus also comprises a conveyor means including a plurality of belts 1 in section 100 and rollers 2 in sections 200, 300, 400 and 500 for carrying and advancing glass plates 3 (FIGS. 1 to 7) past the various sections 100 to 500 along an article movement path in the direction of the arrows Y. As explained below, the belts 1 and the rollers 2 are rotated by conventional means (not shown) so as to advance the plates 3 at a rate of from about 0.5 to about 7 feet per minute, and preferably from about 3 to about 6 feet per minute.
During continuous operation, a plurality of glass plates 3 are loaded onto the belts 1, so that the belts advance the plates into and through section 100 of the apparatus. Referring to FIGS. 1, 2 and 3, a plurality of rotating discs or blocks 101 gently abrade the uppermost surface of each plate, preferably with a mixture of cerium oxide or red rouge and water, to loosen and remove any dirt therefrom. This blocking operation is preferably carried out with cattle hair felt blocks having a diameter of from about 4 to about 12 inches. Each of the blocks is mounted on a shaft 102 which is rotated by a suitable motor 103 and gear means (not shown) at a rate of from about 200 to about 600 revolutions per minute. In the preferred embodiment, the blocks are rotated at about 300 to about 500 revolutions per minute and are oscillated, for example, a distance of about 2 to 4 inches in a direction transverse to the direction Y of the advancing plate to insure that the entire uppermost surface of the plate is blocked.
While still in section 100, each plate advances beneath a plurality of rotary cup brushes 104 that wash the surface of the plate with tap water. The brushes 104, which may have nylon bristles or the like, are generally rotated at the same rate as the blocks 101, and are preferably oscillated in the same manner as well. Each plate finally advances beneath a rotary cylinder brush 105 disposed across the advancing plate. The brush 105 may comprise nylon bristles or the like which contact the plate and complete the cleaning thereof. The brush is generally rotated at about 300 to about 400 revolutions per minute. Both the rotary cup brushes 104 and the rotary cylinder brush 105 may be driven by conventional means such as motors (not shown) that may be similar to motors 103.
Each plate 3 then enters into and passes through section 200 of the apparatus, wherein the surface thereof is sensitized and then activated (super-sensitized). As illustrated in FIGS. 1 and 2, and more particularly in FIG. 4, the plate is subjected to a first rinse, preferably with demineralized water, as it enters section 200 to remove any traces of cerium oxide, red rouge, tap water or any other undesirable matter carried over from section 100. The first rinse may be performed in any conventional manner. For example, the plate may be rinsed by reciprocating a single water spray apparatus transversely of the advancing plate, (i.e., in the direction of arrow X) while the plate advances in the direction indicated by arrow Y. However, the rinse is preferably performed by employing a cross-fire technique.
As illustrated in FIG. 4, when employing a cross fire technique, a mutually opposed pair of pipes 201 and 202 are supported from a carriage 203 that reciprocates along the X axis on a track 204 at a rate of between about 25 and about single passes per minute, and preferably between about 45 and about 60 single passes per minute. The carriage 203 is driven by a chain or belt 205 that runs over a pair of pulleys 206 and 207 arranged at the opposite ends of the track 204. A motor 208 drives the chain 205 while a connection 205A between the chain and the carriage slides up and down in a vertical groove 2058 in the carriage 203 as the connection moves around the pulleys. The drive construction is similar to that shown in Bramsen et al, US Pat. No. 2,246,502.
During the reciprocating motion of the carriage 203, demineralized water is fed alternately to the pipes 201 and 202 in such a program that water is sprayed only from nozzles 201A, 2018 and 201C when the carriage is moving from left to right in FIG. 4, and only from nozzles 202A, 202B and 202C when the carriage is moving in the opposite direction. The pipes 201 and 202 are supplied with water or other rinsing composition through lines 209 and 210, respectively, by any suitable means. The pipes are advantageously operated at pressures between about 25 and about pounds per square inch, preferably between about 25 and about 45 pounds per square inch, and at flow rates of about 500 to about 600 milliliters per minute per pipe.
There are many commercially available control means to alternate the flow of rinsing medium between line 209 and line 210. Valves V and V are illustrated as an example of suitable control means, either automatic or manual, that become apparent to one skilled in the art.
After undergoing the first rinse with demineralized water, the plate advances beneath a reciprocating gun 211 which sprays a dilute solution of stannous chloride on the clean surface. The stannous chloride solution may comprise any of the formulations known in the art as being capable of sensitizing non-conductive substrates to metal deposition. However, a preferred formulation comprises from about 0.02 to about 1.0 gram of stannous chloride per liter of solution, together with a small amount of hydrochloride acid. Such a solution may be prepared, for example, by mixing about 20 grams of stannous chloride and 2 to 3 milliliters of concentrated hydrochloric acid (12 N) in enough demineralized water to form one gallon of stock concentrate, and then diluting each part of the concentrate with about 19 parts of demineralized water. In a preferred embodiment, about one part of the above-described concentrate is injected into a stream comprising about 19 parts of demineralized water, whereafter the combined stream is mixed with air at about 60 to about 80 pounds per square inch, and sprayed through the gun 211 in a highly atomized state at a rate of about 500 to about 700 milliliters per minute.
As illustrated in FIG. 4, the stannous chloride composition dispensing spray gun 211 is supported from the same carriage 203 that supports the first rinse pipes 201 and 202. In addition, a second set of rinse pipes 212 and 213, a palladium chloride composition dispensing spray gun 214 and a third set of rinse pipes 215 and 216 may also be supported from carriage 203.
As the plate 3 continues to advance along the article movement path Y, it passes beneath the second set of rinse pipes 212 and 213. These pipes are operated in the same manner as pipes 201 and 202.
The sheet 3 then passes under the gun 214 which sprays an atomized mixture of air and dilute palladium chloride on the now sensitized surface so as to activate (or super-sensitize) the surface for the ensuing metalboron deposition. As is the case with the stannous chloride solution, the palladium chloride may comprise any of the well-known formulations that are suitable for activating a previously sensitized substrate. However, a formulation comprising from about 0.005 to about 1.0 gram of palladium chloride per liter of solution, together with a small amount of hydrochloride acid, is preferred. One such formulation may be prepared by mixing about 2 grams of palladium chloride and 2 to 3 milliliters of concentrated hydrochloric acid with a sufficient amount of demineralized water to form one gallon of concentrated stock solution, and then diluting each part of the stock solution with 19 parts of demineralized water. As is the case with the stannous chloride solution, the diluted palladium chloride is preferably mixed with air at a pressure of about 60 to about 80 pounds per square inch and sprayed onto the glass at a rate of about 500 to about 700 milliliters per minute.
After passing spray gun 214 and before leaving section 200 of the apparatus, the plate 3 undergoes a third demineralized water rinse. This rinse is carried out in the same manner as the first and second rinses, and is designed to remove any excess palladium chloride from the advancing plate before it reaches the metal-boron coating composition deposition section.
The spacing between the respective guns in section 200 of the apparatus may vary within wide limits depending, for example, upon the rate at which the plate 3 is advancing, the dimensions of the fan-shaped spray pattern generated by each gun, the rate of traverse of each gun, and the like. However, it is preferred to arrange the various guns in section 200 such that the time required for the leading edge of the given plate 3 to advance from each gun or set of guns to the next successive gun or sets of guns is from about to about 90 seconds.
As illustrated, the plate then passes from section 200 of the apparatus to section 300 thereof, wherein a metal and boron-containing coating, preferably nickelboron, cobalt-boron, iron-boron or a mixture of at least two of said metal-boron coatings is deposited on the now activated surface thereof. The deposition is preferably accomplished by simultaneously spraying a metalcontaining solution and a boron-containing reducing solution from separate spray nozzles and intermixing said solutions onto the activated surface such that the metal ions present in the contemplated metal solution become reduced to a transparent boron-containing metal film which tenaciously adheres to the activated surface.
It will be appreciated that the number, disposition,
and the spacing of the guns which spray the metal solution and the boron-containing reducing solution, and the rate at which they are reciprocated, are determined generally by the rate at which the plate advances, the temperature, pH, and concentration of the intermixed film forming composition and the like, and primarily by the time required for the film forming composition to be substantially depleted in its film forming capacity, and the desired thickness and transparency of the deposited film. The importance of these latter two parameters will become more apparent in view of the illustrative example set forth below.
For the sake of illustration, section 300 is shown in FIGS. 1, 2 and 5 as having two reciprocating spray gun sets 302 and 303, each comprising a first nozzle for dispensing a metal-containing solution, 302A and 303A, respectively, and an opposed second nozzle, 3028 and 30313, respectively, for dispensing a reducing solution. Section 300 also includes a mutually opposed pair of reciprocating water pipes 304 and 305 arranged for cross-fire rinsing. As shown, spray gun sets 302 and 303 are supported for transverse reciprocating movement, for example, in the manner described for reciprocating spray guns 211 and 2M in connection with FIG. 4. However, it should be noted that the gun set in section 300 must reciprocate much faster than those in section 200 or than those employed in conventional spray techniques for depositing silver, for example. in this connection, it has been found that uniformly and controllably transparent metal-boron coatings can best be made in accordance with the present invention only when the gun sets in section 300 are reciprocated at a rate of at least about 60 to about 65 single passes per minute, and preferably from about 72 to about 76 single passes per minute, when the plates being coated are about 4 feet wide and are advanced at a rate of from about 3 to about 6 feet per minute. Thus, for a 4-foot wide plate advancing at a rate of 3% feet per minute, i.e., 42 inches per minute, a spray gun set reciprocating at 74 single passes per minute will complete about 1.75 single passes over each inch segment of the advancing plate.
Accordingly, if the width of the applied spray in a direction of travel of the plate is from 10 to 12 inches, each inch segment of the plate will receive from about 17.5 to about 21.1 applications of solution per gun set. Of course, the required number of passes per minute will vary somewhat in accordance with changes in magnitude of the various parameters discussed herein. For example, the required number of passes would increase when the plate being coated or advanced more rapidly than approximately 3 to approximately 6 feet per minute.
Spray guns of each set 302 and 303 are connected through respective supply lines (not shown) to air under pressure at about 20 to about 60 pounds per square inch. In turn, the respective supply lines are in fluid communication with prepared metal and reducing solutions stored in separate solution tanks or containers (not shown), preferably of such size to hold a reasonable supply of fluid, such that when the prepared solutions are injected into the supply lines by any conventional means (not shown), the solutions are fed through the lines and aprayed from the guns in a fan-shaped pattern. It will be appreciated that the magnitude of air pressure required for a satisfactory spray varies considerably with the design of the guns of the various parameters of the solutions employed. In this connection, satisfactory results have been obtained with pressures as low as about 20 pounds per square inch and as high as about 55 pounds per square inch. Pressures in the range of about 25 to about 40 pounds per square inch are preferred. The rates at which the respective prepared solutions are sprayed from each gun may vary, but it is preferred that the rates of flow be maintained at about 300 to about 2,000 millimeters per minute per gun.
As illustrated in FIGS. 8, 9 and 10, each of the nozzles 302A and 302B in the metal depositing spray gun set 302 is preferably designed to provide a substantially fan-shaped stream which opens only a few degrees in the direction transverse to the advancing plate, and which opens in the direction of travel of the plate such that the stream contacts the advancing plate in an elliptical pattern having a major diameter of from about 8 inches to about 14 inches, and preferably from about l inches to about 12 inches in length (FIG. 8). Spray gun set 303 functions in the same manner.
The nozzles in each metal salt-reducing solution set are arranged to have an included angle of from about 80 to about 120 between the streams of composition they dispense. To accomplish this end, each of the metal salt solution dispensing guns is inclined obliquely from the vertical about 40 to about 60 toward a mutually opposed reducing solution dispensing gun, and vise versa in a vertical plane common to the dispensing guns of the set (FIG. 10). This arrangement is desirable so that the metal and reducing solutions are effectively and thoroughly mixed as they approach and strike the surface of the activated glass plate.
Referring to FIG. 1 1, there is shown a schematic perspective view of an apparatus illustrating the state of the art prior to the present invention. FIG. 11 shows a metal-boron composition dispensing spray gun set 302 reciprocating along the X axis and applying solution to the transparent sheet 3 as said sheet travels along its article movement path Y. Note that set 302 produces a rear wave 306 and a front wave 307 on the surface of the glass sheet 3. The rear wave comprises a mixture of fresh solution and spent solution containing precipitated nickel, decomposed reactants, rinsing medium and gas bubbles. This mixture reaches and covers the sensitized surface of the glass sheet 3 before the sheet reaches a position where its upper surface is sprayed with fresh solution from gun set 302. As pointed out above, when the advancing glass sheet is contacted initially with spent solution, the resultant coating does not possess uniform optical properties. Further, note that the boundary 308 of rear wave 306 does not extend across the sheet in a straight line. Rather, it extends transversely of article movement path Y in a finger-like pattern, causing non-uniform surface coverage and, therefore, streaks in the final coating. In addition, the amount of old solution per unit area of glass sheet covered and the age of the old solution is not uniform for all portions of the rear wave 306. This non-uniformity of amount and age of coating manifests itself in inhomogeneities in the resulting film.
Front wave 307 is principally composed of spent so lution and rinsing medium. In the case of any front wave, spent solution is contacting the surface of a substrate after fresh solution has been applied. Since spent solution does not adhere as readily to a metal surface as it does to a glass surface, front wave 307 does not affect the unifonnity of the finished coating to the extent that rear wave 306 affects it.
The terms front and rear" refer to the direction of movement of glass sheets along the article movement path as defined by the direction of arrow Y. In addition, the following description uses the terms upstream" and downstream to define the direction of glass sheets along the article movement path. The sheets are presumed to travel in a downstream direction.
According to the present invention, rear wave 306 has been completely eliminated and front wave 307 has been reduced in size by the use of a stationary squeegee/shield apparatus 301 immediately upstream of the first spray gun set 302, as shown in FIG. 5. The squeegee/shield apparatus 301 extends in direction X that is transverse to the article movement path Y, and it functions to control the thickness of rinse water remaining on the surface of sheet 3 from rinse pipes 215 and 216 to form a water film of uniform thickness on the glass surface when said sheet 3 and said spray gun set 302 are in alignment, while avoiding the formation of finger-like waves of solution upstream of said spray gun set. Unlike spray gun sets 302 and 303, and rinse pipes 304 and 305, the squeegee/shield apparatus is stationary and does not reciprocate along the X axis.
Referring to FIG. 12, there is shown the details of a first embodiment 301A of a squeegee/shield made in accordance with the present invention, together with spray gun set 302. Squeegee/shield 301A includes a splash shield 310 and a squeegee 312 mounted beneath splash shield 310. Squeegee 312 comprises, for example, a loop made of soft rubber approximately 0.0l0 inch thick. The loop forms a lip portion 314 that engages the coated upper sensitized surface of each moving sheet of glass 3 that enters a spraying station. Squeegee 312 is held in place beneath shield 310 by any suitable means, such as, for example, an angular plate 316 which is bolted to a flange 318. The squeegee is made of an elastomeric material having a durometer hardness of from about 50 to about 90, and preferably about 70. Examples of suitable materials are: natural rubber, neoprene, silicone rubber and plasticized polyvinyl chloride. Stiff plastics such as Teflon, Mylar, Lexan and many polycarbonates tend to scratch the sensitized surface.
Shield 310 and squeegee 312 prevent the spray-fan M from gun set 302 from splashing onto the galss surface and congragating in an upstream area 320 of set 302. Squeegee 312 prevents any of the spray M from flowing beneath shield 310 to upstream area 320. Together, the shield 310 and the squeegee 312 eliminate the rear wave and its assoiated problems.
Shield 310 may be constructed of any material that is capable of adding structural integrity to the apparatus 301 and is not attacked by the spray-fan M. Stainless steel is an example of a meterial suitable for use with a nickel-boron spray. Actually, the squeegee could be extended upward to replace the shield and perform its splash prevention function, as long as some measure is taken to add structural integrity to the apparatus. This could be done by, for example, reinforcing the upper portion of the squeegee or varying its thickness so that is is thicker, and therefore stronger, at its upper portion.
The squeegee 312 and particularly lip portion 314 performs two additional functions. Some of the rinse water from pipes 215 and 216 remains on the glass sheet 3 in a random manner as it approaches gun set 302 along the article movement path Y. If this rinse water is allowed to sit on the glass surface beneath gun set 302, there will be a non-uniform dilution of the spray solution and a coating with inferior optical properties will result. Lip portion 314 acts as a wiper to insure that no puddles of rinse water pass beneath gun set 302. It allows only a thin uniform rinsing fllm of from about 0.03 inch to about 0.10 inch, and preferably about 0.05 inch, to sit on the glass beneath the coating station. In addition, lip 314 is positioned so that it slightly overlaps the side edge 309 of spray-fan M by about one-eighth or about one-fourth of an inch at the upper glass surface to intercept a portion of spray M. Ideally, the tip of lip 314 should just touch the side edge of spray-fan M to insure that fresh spray solution contacts the glass surface first, but it is impractical to maintain this relationship with precision. If the squeegee is positioned so that lip 314 does not either touch the side edge or intercept a portion of spray-fan M, spent solution may contact the glass surface in random areas before fresh solution contacts the surface in those areas and a coating having non-uniform optical properties may result. Moving the squeegee downstream so that the tip of lip 314 is one-half inch from the side edge of the spray-fan M produces streaky coatings. As a practical matter, if the squeegee intercepts too much of the spray M, such as, for example, about 1 inch, an unnecessary amount of solution is wasted.
Referring to FIG. 13, 14 and 15, alternate embodiments of the present invention are shown with similar numerals used to indicate similar parts. FIG. 13 shows a squeegee/shield 3013 including a squeegee 322 comprising a thin plastic reinforcement 324 enclosed within a looped elastomeric covering 326. The covering 326 may be made, for example, of soft material, similar to the ones described in connection with squeegee 312. The reinforcement 324 can be made, for example, of polyvinyl butyral, approximately 0.030 inch thick.
Referring to FIG. 14, there is shown a third embodiment 301C of the squeegee/shield apparatus of the present invention. In this embodiment, the squeegee comprises a curtain 322 approximately three-fourths of an inch to 1 inches long and approximately 0.007 to approximately 0.040 inch thick, hanging freely from splash shield 310. The curtain 332 may be made of any of the suitable materials descirbed above in connection with squeegee 312.
Referring to FIG. 15, there is shown a fourth emboidment 301]) of the squeegee/shield apparatus of the present invention. In this embodiment, the squeegee is in the form of a roller 340, driven by friction at the sensitized surface. It is possible to drive roller 340, but this is unnecessary and can lead to complications if roller 340 is not driven at the exact speed as the rollers 2 beneath the glass sheet 3. The roller may be made of any of the abovementioned squeegee materials, but is preferably made of closed cell foam rubber. Enclosed within the foam rubber is a metallic tube 342. Shield 3344 includes a sheet 346 and rods 348 with ribs 350 connecting the sheet to the rods. Axle 352 is rotatably connected to the base of rods 348and roller 340 rotates about axle 352. In the embodiments illustrated in FIGS. 13-15, the squeegee operates to perform the functions described in connection with the embodiment of FIG. 12.
It is customary to use either two or three, or sometimes even four, spray gun sets. It might occur to one skilled in the art to use a squeegee/shield apparatus prior to each spray gun set. It has-been discovered, however, that the installation of any squeegee/shield apparatus after the first spray gun set is detrimental in that it damages the freshly coated metal-boron surface.
Further, a subsequent spray gun set appears to be able to sweep the spent solution from the surface of substrate 3 without damaging the prior coating. This can be explained by the fact that the spent solution does not adhere as readily to the fresh coating as it does to sensitized glass. Therefore, the use of squeegee/shield apparatus after the first spray gun set is unnecessary and even undesirable.
The shields 310 and 344 have been illustrated as being oriented at an angle of about 30 with the verti cal, but this angle is not critical. Actually, the shield may even lie within a vertically extending plane. By tilting the shield to an angle of from about 15 to about 50 with the vertical, the top portion of the shield is spaced from gun set 302 to make gun set 302 more accessible.
As the plate advances beyond each spray gun set 302 and 303, the intermixed film forming composition which is uniformly distributed on the surface of the plate is permitted to rest relatively quietly. This quiescent period or period of minimum turbulence is highly desirable since it enables the film forming composition to deposit a transparent coating which is substantially free from visual defects normally attributed to turbulence or agitation of the filming composition during deposition. In addition, it is during this quiescent period that the intermixed filming compositions comtemplated herein undergo a change in their capacity for depositing a film such that the rate of film deposition, which is initially relatively rapid, decreases and then effectively completely ceases while the deposited film is still transparent. While the time required for this change in filming capacity to occur will vary considerably depending upon the chemistry of the actual filming composition employed, a filming composition comprising equal amounts of the nickel acetate solution and borohydride reducing solution, illustrated respectively in Tables I and II of US. Pat. application Ser. No. 57,451, will normally undergo a substantial decrease in its filming capacity within from about 10 seconds to a few minutes, e.g., 5 minutes. In this regard, a glass plate that is coated with a metal and boron-containing film at room temperature by a single 15; second spray application of the above illustrated intermixing filming composition will normally have a luminous transmission of from about 30 to about 40 percent when the filming capacity of the composition has depleted and filming has effectively ceased.
Referring once again to FIGS. 1 and 5, it will be appreciated that once the film forming composition has become dead, i.e., depleted of its filming capacity, it may be removed from the plate by any convenient means without affecting the thickness, and thus the transparency of the film. It will also be appreciated tha the lowest degree of transparency obtainable will depend primarily upon the amount of film that will deposit from a given film forming composition before it becomes dead, the number of gun sets in section 300, and the distance between each gun set. The effect of these variables on the thickness, uniformity and transparency of the metal-boron films formed in accordance with this invention will be more fully appreciated in light of the example recited hereinbelow.
After undergoing the quiescent period after its exposure to the mixed composition dispensed by spray gun set 303, the plate has a luminous transmittance of about 15 to 25 percent. If a third apray gun set is used (not illustrated), a luminous transmittance of as little as 10 percent may be obtained. Each additional gun provide a quiescent period designed to allow the partially formed metal-boron film to increase in thickness uniformly in the substantial absence of adverse effects caused by turbulence. Even more important, however, this period is designed to allow sufficient time for the film forming composition on the surface of the plate to become substantially depleted of its film-forming capacity so that the rate of deposition of the metal-boron film will have materially slowed down, and preferably effectively ceased, before the plate is rinsed under pipes 304 and 305. In this latter connection, it will be appreciated that the necessary distance between pipes 304 and 305 and the last metal depositing gun set 303 is related to the rate at which the plate is advanced. Thus, while maintaining all of the various parameters within the bounds described herein, the distance between the final rinse pipes 304 and 305 and the last spray gun set 303 should be at least about 30 inches, and preferably at least about 35 to 40 inches to provide a final film thickness corresponding to a luminous transmittance of about 20 percent.
After undergoing a final water rinse under rinse pipes 304 and 305, the plate 3 advances into section 400 of the coating apparatus where it is dried by means of a suitable air knife 401 (FIG. 6). The air knife 401 may comprise any conventional blow-off device, but it is preferred to employ a high volume-low pressure knife to avoid disturbing the quality of the metal-boron film. For example, it is desirable to employ a knife that operates at a pressure of about 3 to 7 ounces per square inch, while forcing from about 300 to about 400 cubic feet of air per minute against the metal-boron coated glass plate.
After passing beneath the air knife, the completed metal-boron coated plate passes into section 500 where the thickness of the deposited film is measured by a conventional measuring device 501. Thereafter, the transparent glass plate is removed from the rollers 2 and is ready for use.
The present invention is applicable in forming transparent metal-boron films on clear plastic (e.g. polymethyl methacrylate) and glasses, especially soda-limesilica glasses, but can be used to film a wide variety of glass, ceramic, glass-ceramic, siliceous and calcareous based compositions. For example, this invention can be used to provide metal-boron and particularly nickelboron films on the following types of glasses: soda-limesilica glasses; alkali-alumina-silica glasses, such as those containing lithia as a component alkali; aIkali-zirconiasilica glasses; alkali-alumina-zirconia-silica glasses; brosilicate glasses, etc. Bearing this in mind, the present invention is described hereinabove with specific reference to soda-lime-silica glass.
The soda-lime-silica glass to be treated can be a clear glass or it can be a colored glass tinted by the introduction or various conventional materials into the glass forming batch. These latter glasses are often referred to as heat absorbing glasses especially when they contain iron oxide. Representative soda-lime-silica glass bases which can be treated in accordance with this invention usually contain 65 to 75 percent by weight SiO 10 to l8 percent by weight Na O, 5 to percent by weight CaO, l to 5 percent by weight MgO, 0 to 1.0 percent by weight Na SO 0 to 5 percent by weight aluminum oxide (M 0 0 to 8 percent by weight K 0, 0 to 8 percent by weight B O O to 1 percent by weight iron oxide (Fe o and 0 to 0.7 percent by weight of NaCl, S0 A5 0 BaO, NiO, C00 and Se and combinations thereof.
A representative range of composition for sode-limesilica glasses is listed as follows (wherein the given amounts of metals listed are determined as their oxides, except as otherwise noted):
Component Percent by Weight SiO, 68-735 Na,0 I 2-] 7 C20 7-12 MgO 2-4 Na,SO 0-0.8 NaCl 0-0.3 Fe,O 0.05-0.09 M 0, 0-3.5 B 0 0-6 K 0 0l.5 A5 0 00.5 BaO 0-O.7 NiO 00.l C00 0-0.l SO; 0-0.5 Se 00.l
The invention will be further understood from the specific example which follows. It should be noted, however, that the present invention is not necessarily limited to specific materials, temperatures, contact times, and pH values noted in the below example:
EXAMPLE A 40 inch X 70 inch X A commercial soda-lime-silica glass plate is coated with a nickel-boron film with the apparatus illustrated schematically in FIG. 1. Four blockers are used, each comprising a 3-inch thick cattle hair felt disc of 8-inch diameter. The blockers are arranged at l2-inch centers in the direction parallel to the rollers, hereafter referred to as the transverse direction, and are rotated at about 350 revolutions per minute. The blockers are oscillated about 4 inches in the transverse direction at a frequency of about 15 cycles per minute. Four 6-inch diameter rotary cup brushes are arranged at 12-inch centers in a transverse direction such that the longitudinal distance between the blockers argthe rotary cup brushes is about 9 inches. The rotary cup brushes are equipped with No. 12 nylon bristles and are rotated at about 350 revolutions per minute. The brushes are also oscillated about 4 inches in the transverse direction at a frequency of 15 cycles per minute. During operation, the blockers are supplied with a mixture of cerium oxide and tap water, while a spray of tap water is applied beneath the rotary cup brushes. The rotary cylinder brush has a 6-inch diameter, comprising No. 12 nylon bristles, and has its axis disposed 8 inches from the rotary cup brushes. The first, second and third rinse sets, as well as the tin composition dispensing gun and the palladium composition dispensing gun, i.e., all of the rinse sets and the guns in section 200, are mounted from a single boom that reciprocates in a transverse direction at a rate of about 45 single passes per minute. Each of the rinse nozzles comprises a single UniJet-T8002 spray noule (manufactured by Spraying Systems Company, Dellwood, Ill.) and is operated at a pressure of about 40 pounds per square inch, at an average flow rate of about 0.2 gallon of demineralized water per minute. Each of the tin and palladium composition dispensing guns comprises a single, type C, spray gun equipped with a Paasche U2, F2-8 nozzle, manufactured by Paasche Air Brush Company, Chicago, Ill., and operated at an air pressure of about 70 pounds per square inch and a flow rate of about 500 milliliters of the solution described below per minute. The distance between the rotary cylinder brush and the first rinse pipes 201 and 202 is about 30 feet, while the distance from each gun to the next successive gun is about feet.
The gun sets in section 300 of the apparatus are spaced apart from those in section 200 such that the distance between rinse pipes 215 and 216 and gun set 302 is about feet. In addition, gun set 302 is spaced about 3 feet from gun set 303. The distance between the tip of the gun dispensing nickel solution and the tip of the gun dispensing reducing solution in each respective set is about 10 inches. All of the guns in section 300 employlaasche U2, F2-8 nozzles, which are arranged so that the tip of each nozzle is about 7 inches above the surface of the glass being coated, and so that each respective gun set generates a fan-shaped stream of intermixed film forming solution that contacts the glass surface in a generally elliptical pattern having a major diameter of about 1 1 inches extending in a longitudinal direction. All of the rinse sets and the spray guns in section 300 are mounted from a single boom that reciprocates in the transverse direction at a rate of about 72 passes per minute which is equal to 36 round trips per minute. During operation, each of the metal deposition gun sets in section 300 is maintained at a pressure of about 40 pounds per square inch and a flow rate of about 800 milliliters of solution per minute, while the final cross-fire rinse pipes 304 and 305 are operated at a pressure of about 40 pounds per square inch at an average flow rate of about 0.2 gallon of demineralized water per minute per nozzle. The distance between rinse pipes 304 and 305 and the last metal depositing gun set 303 is about 70 inches.
The air knife 401 comprises an elongated metal housing having a 0.002-inch wide delivery slot extending along the length of its bottom wall. The knife 401 is disposed at a 45 angle relative to the advancing plate and had its centermost portion spaced about 8 feet from the final rinse pipes 304 and 305. The air knife is operated at about 5 ounces per square inch and at a flow rate of about 350 cubic feet per minute. The ambient air temperature is about 82F., while the temperature of the demineralized and tap water used throughout this example is about 63F. The glass plate is advanced at a rate of about 5 feet per minute, while the slot opening of the air knife is spaced about one-half inch from the plate. On the basis of a liter of solution, each of the prepared aqueous solutions employed has the following composition:
Nickel Solution Nickelous acetate 5.0 grams Boric acid 2.5 grams Sodium gluconate 9.0 grams Hydrazine sulfate 0.5 grams Water Added to 1 liter Ammonium hydroxide Added to pH 7.4
Ethomeen C-20* 0.06 grams Etl'iBin eQH C-ZO (trademark of Armour and Company) is a cocoamine having an average molecular weight of 645 and the following generalized formula:
)CHaCHnOhH R-N wherein R is derived from a cocoamine and x y 10.
Reducing Solution Sodium borohydride 0.5 gram Water Added to 1 liter Sodium hydroxide Added to pH 1 1.6
Hydrochloric acid (12 N) Water Added to 1 liter 0.04 milliliter Palladium Solution Palladious chloride Water Added to 1 liter The temperature of each of these solutions is about F. The pH of the intermixed nickel and borohydride solutions is about 7.7. A nickel film is formed which contains about 5 to 10 percent by weight boron and the resulting coated plate has a luminous transmission of about 22 percent. The film is very adherent to the glass plate and is very uniform in appearance. It has an initial resistivity of 300 ohms per square.
Having now fully disclosed the invention, what I claim is as follows:
1. An apparatus for coating :1 surface of an article having a liquid medium on said surface comprising:
means for applying a spray of coating composition to the surface of said article having said liquid medium thereon,
means for moving said article along a path of movement extending beneath said first named means, and
means disposed above said surface of said article and extending into contact with the liquid medium thereon for maintaining said liquid medium in a film of substantially uniform thickness, said last named means being located along the path of movement of said article toward said first named means and being positioned so as to intercept a portion of the spray of the coating composition applied to said surface of said article.
2. An apparatus for coating a surface of an article comprising:
a first-named means for applying a liquid rinsing medium to the surface of said article to be coated,
a second-named means for applying a spray of a coating composition to the surface of said article having liquid rinsing medium thereon,
means for moving said article along a path of movement beneath said firstand second-named means, and
means disposed above said surface of said article and extending into contact with the liquid medium thereon for maintaining said liquid medium in a film of substantially uniform thickness, said last named means being located along the path of movement of said article toward said secondnamed means and downstream with respect to said first-named means, and being positioned so as to intercept a portion of the spray of the coating composition applied to said surface of said article.
3. An apparatus as defined in claim 2 wherein said means for maintaining the thickness of said film of liquid rising medium substantially uniform comprises a squeegee disposed between said means for applying a 0.02 gram 0.04 milliliter liquid rinsing medium and said means for applying a spray of a coating composition.
4. An apparatus as defined in claim 3, wherein said squeegee has a soft lower portion and means is pro vided to reinforce a portion of said squeegee above its said soft lower portion.
5. An apparatus as defined in claim 4 wherein said squeegee reinforcing means comprises a shield disposed in spaced relation above said surface and made of a material that is not attacked by said composition, said squeegee being attached thereto to extend downwardly therefrom.
6. An apparatus as defined in claim 5 wherein said squeegee is lipshaped.
7. An apparatus as defined in claim 6 wherein said means for applying a spray of a coating composition to the surface of said article comprises a spray gun for applying a fan-shaped spray of said coating composition in a direction extending toward said surface and located in a position relative to said squeegee that said squeegee intercepts a portion of said fan-shaped spray directed toward said surface.
8. An apparatus as defined in claim 7 wherein means are provided to reciprocate said spray gun along a path that is transverse to said article movement path.
9. An apparatus as defined in claim 7 wherein said squeegee is so disposed relative to said spray gun to intercept less than about two inches of said fan-shaped spray measured along the path of movement of said article.
10. An apparatus as defined in claim 9 wherein said squeegee is so disposed relative to said spray gun to intercept about one-fourth of an inch of said fan-shaped spray measured along the path of movement of said article.
11. An apparatus as defined in claim 3 wherein said squeegee is in the form of a hoop.
12. An apparatus as defined in claim 11 wherein said hoop has an internal reinforcement.
13. An apparatus as defined in claim 3 wherein said squeegee is in the form of a curtain.
14. An apparatus as defined in claim 3 wherein said squeegee is in the form of a roller.
15. An apparatus as defined in claim 14 wherein said roller is constructed of closed cell foam rubber.
16. An apparatus as defined in claim 9 wherein said squeegee is so disposed relative to said spray gun to intercept about one-fourth of an inch of said fan-shaped spray measured along the path of movement of said article.
17. An apparatus for coating a surface of an article comprising:
a first-named means for applying a sensitizing composition to the surface of an article to be coated,
a second-named means for applying a liquid rinsing medium to the sensitized surface of the article to be coated,
a third-named means for applying a spray of a coating composition to the sensitized surface of said article having a liquid rinsing medium thereon,
means for moving said article along a path of movement beneath said first-, second-, and third-named means, and
means disposed above said surface of said article and extending into contact with the liquid medium thereon for maintaining said liquid medium in a film of substantially uniform thickness, said last named means being located along the path of movement of said article toward said third-named means downstream with respect to said secondnamed means and being positioned so as to intercept a portion of the spray of the coating composition applied to said surface of said article.
18. An apparatus as defined in claim 17 wherein said means for maintaining the thickness of said film of liquid rinsing medium substantially uniform comprises a squeegee disposed between said means for applying a liquid rinsing medium and said means for applying a spray of a coating composition.
19. An apparatus as defined in claim 18 wherein said squeegee has a soft lower portion and means is provided to reinforce a portion of said squeegee above its said soft lower portion.
20. An apparatus as defined in claim 19 wherein said squeegee reinforcing means comprises a shield disposed in spaced relation above said surface and made of a material that is not attacked by said composition, said squeegee being attached thereto to extend downwardly therefrom.
21. An apparatus as defined in claim 20 wherein said squeegee is lip-shaped.
22. An apparatus as defined in claim 21 wherein said means for applying a spray of a coating composition to the surface of said article comprises a spray gun for applying a fan-shaped spray of said coating composition in a direction extending toward said surface and located in a position relative to said squeegee that said squeegeeintercepts a portion of said fan-shaped spray directed toward said surface.
23. An apparatus as defined in claim 22 wherein means are provided to reciprocate said spray gun along a path that is transverse to said article movement path.
UNITED STATES PATENT OFFICE CERTIFICATE OF CORRECTION Patent No. 3,782,328 Dated January 1, 1974 Inventor-(R) Helmut Franz It is certified that error appears in the above-identified patent and that said Letters Patent are hereby corrected as shown below:
Claim 7, Column 19, line 20, after "squeegee" (first occurrence),
insert -such-.
Signed and sealed this 30th day of April 1911.
(SEAL) Attest:
EDWARD ILFLETGHER, JR. j C MARSHALL DAMN Attesting Officer- Commissioner of Patents FORM PO-IOSO (10 69) USC OMM-DC poem-Poo 1: as. sovsnumsm' PRINTING omc: Isis o-see-au.

Claims (23)

1. An apparatus for coating a surface of an article having a liquid medium on said surface comprising: means for applying a spray of coating composition to the surface of said article having said liquid medium thereon, means for moving said article along a path of movement extending beneath said first named means, and means disposed above said surface of said article and extending into contact with the liquid medium thereon for maintaining said liquid medium in a film of substantially uniform thickness, said last named means being located along the path of movement of said article toward said first named means and being positioned so as to intercept a portion of the spray of the coating composition applied to said surface of said article.
2. An apparatus for coating a surface of an article comprising: a first-named means for applying a liquid rinsing medium to the surface of said article to be coated, a second-named means for applying a spray of a coating composition to the surface of said article having a liquid rinsing medium thereon, means for moving said article along a path of movement beneath said first- and second-named means, and means disposed above said surface of said article And extending into contact with the liquid medium thereon for maintaining said liquid medium in a film of substantially uniform thickness, said last named means being located along the path of movement of said article toward said second-named means and downstream with respect to said first-named means, and being positioned so as to intercept a portion of the spray of the coating composition applied to said surface of said article.
3. An apparatus as defined in claim 2 wherein said means for maintaining the thickness of said film of liquid rising medium substantially uniform comprises a squeegee disposed between said means for applying a liquid rinsing medium and said means for applying a spray of a coating composition.
4. An apparatus as defined in claim 3, wherein said squeegee has a soft lower portion and means is provided to reinforce a portion of said squeegee above its said soft lower portion.
5. An apparatus as defined in claim 4 wherein said squeegee reinforcing means comprises a shield disposed in spaced relation above said surface and made of a material that is not attacked by said composition, said squeegee being attached thereto to extend downwardly therefrom.
6. An apparatus as defined in claim 5 wherein said squeegee is lip-shaped.
7. An apparatus as defined in claim 6 wherein said means for applying a spray of a coating composition to the surface of said article comprises a spray gun for applying a fan-shaped spray of said coating composition in a direction extending toward said surface and located in a position relative to said squeegee that said squeegee intercepts a portion of said fan-shaped spray directed toward said surface.
8. An apparatus as defined in claim 7 wherein means are provided to reciprocate said spray gun along a path that is transverse to said article movement path.
9. An apparatus as defined in claim 7 wherein said squeegee is so disposed relative to said spray gun to intercept less than about two inches of said fan-shaped spray measured along the path of movement of said article.
10. An apparatus as defined in claim 9 wherein said squeegee is so disposed relative to said spray gun to intercept about one-fourth of an inch of said fan-shaped spray measured along the path of movement of said article.
11. An apparatus as defined in claim 3 wherein said squeegee is in the form of a hoop.
12. An apparatus as defined in claim 11 wherein said hoop has an internal reinforcement.
13. An apparatus as defined in claim 3 wherein said squeegee is in the form of a curtain.
14. An apparatus as defined in claim 3 wherein said squeegee is in the form of a roller.
15. An apparatus as defined in claim 14 wherein said roller is constructed of closed cell foam rubber.
16. An apparatus as defined in claim 9 wherein said squeegee is so disposed relative to said spray gun to intercept about one-fourth of an inch of said fan-shaped spray measured along the path of movement of said article.
17. An apparatus for coating a surface of an article comprising: a first-named means for applying a sensitizing composition to the surface of an article to be coated, a second-named means for applying a liquid rinsing medium to the sensitized surface of the article to be coated, a third-named means for applying a spray of a coating composition to the sensitized surface of said article having a liquid rinsing medium thereon, means for moving said article along a path of movement beneath said first-, second-, and third-named means, and means disposed above said surface of said article and extending into contact with the liquid medium thereon for maintaining said liquid medium in a film of substantially uniform thickness, said last named means being located along the path of movement of said article toward said third-named means downstream with respect to said second-named means and being positioned so as to intercept a portion of the spray of the coating composition applied to said surface of said article.
18. An apparatus as defined in claim 17 wherein said means for maintaining the thickness of said film of liquid rinsing medium substantially uniform comprises a squeegee disposed between said means for applying a liquid rinsing medium and said means for applying a spray of a coating composition.
19. An apparatus as defined in claim 18 wherein said squeegee has a soft lower portion and means is provided to reinforce a portion of said squeegee above its said soft lower portion.
20. An apparatus as defined in claim 19 wherein said squeegee reinforcing means comprises a shield disposed in spaced relation above said surface and made of a material that is not attacked by said composition, said squeegee being attached thereto to extend downwardly therefrom.
21. An apparatus as defined in claim 20 wherein said squeegee is lip-shaped.
22. An apparatus as defined in claim 21 wherein said means for applying a spray of a coating composition to the surface of said article comprises a spray gun for applying a fan-shaped spray of said coating composition in a direction extending toward said surface and located in a position relative to said squeegee that said squeegee intercepts a portion of said fan-shaped spray directed toward said surface.
23. An apparatus as defined in claim 22 wherein means are provided to reciprocate said spray gun along a path that is transverse to said article movement path.
US00324730A 1971-07-06 1973-01-18 Squeegee /shield Expired - Lifetime US3782328A (en)

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US5786028A (en) * 1996-09-05 1998-07-28 Cantwell; Jay S. Masking tape and method
US6117488A (en) * 1998-09-25 2000-09-12 Erickson; Dennis Non-sag liquid application method
US20060134318A1 (en) * 2003-01-28 2006-06-22 Alan Hudd Method of forming a conductive metal region on a substrate

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US3894883A (en) * 1971-07-06 1975-07-15 Ppg Industries Inc Method and apparatus utilizing an angled crossfire rinse system
WO1980002390A1 (en) * 1979-04-27 1980-11-13 Caterpillar Tractor Co Method of painting
JPS6130672A (en) * 1984-07-23 1986-02-12 Hitachi Ltd Selective processing method
DE10146251A1 (en) * 2001-09-20 2003-04-17 Gruenenthal Gmbh Device for producing a pharmaceutical film

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US2489985A (en) * 1944-12-04 1949-11-29 American Cyanamid Co Process for impregnating fibrous materials and products thereof
US2800874A (en) * 1953-09-28 1957-07-30 Victor A Leslie Tire painting device
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US5786028A (en) * 1996-09-05 1998-07-28 Cantwell; Jay S. Masking tape and method
US6117488A (en) * 1998-09-25 2000-09-12 Erickson; Dennis Non-sag liquid application method
US20060134318A1 (en) * 2003-01-28 2006-06-22 Alan Hudd Method of forming a conductive metal region on a substrate

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