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US3907660A - Apparatus for coating glass - Google Patents

Apparatus for coating glass Download PDF

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US3907660A
US3907660A US430424A US43042474A US3907660A US 3907660 A US3907660 A US 3907660A US 430424 A US430424 A US 430424A US 43042474 A US43042474 A US 43042474A US 3907660 A US3907660 A US 3907660A
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substrate
cathode
temperature
sputtering
oxygen
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US430424A
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Frank H Gillery
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PPG Industries Inc
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PPG Industries Inc
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    • 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
    • C23C14/00Coating by vacuum evaporation, by sputtering or by ion implantation of the coating forming material
    • C23C14/22Coating by vacuum evaporation, by sputtering or by ion implantation of the coating forming material characterised by the process of coating
    • C23C14/34Sputtering
    • 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
    • C23C14/00Coating by vacuum evaporation, by sputtering or by ion implantation of the coating forming material
    • C23C14/0021Reactive sputtering or evaporation
    • C23C14/0036Reactive sputtering
    • 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
    • C23C14/00Coating by vacuum evaporation, by sputtering or by ion implantation of the coating forming material
    • C23C14/06Coating by vacuum evaporation, by sputtering or by ion implantation of the coating forming material characterised by the coating material
    • C23C14/08Oxides
    • C23C14/086Oxides of zinc, germanium, cadmium, indium, tin, thallium or bismuth

Definitions

  • Apparatus conforming to one embodiment for performing the present invention has a series of vertically adjustable supports arranged in two sets of intersecting rows that provide spaced points of support for one or more flat or curved substrates as the case may be.
  • the bottom substreate surface is supported on spaced points having minimum heat exchange relation at the points of support.
  • the radiant heating means disposed to one side of the supported substrate or substrates is able to provide a uniform heating pattern over the entire bottom surface of the substrate so that it now becomes possible to maintain the substrate temperature approximately uniform even when a cathode is reciprocated in facing relation to the opposite surface of the substrate, since a sufficient portion of the heat input to the substrates treated to contol the substrate temperature radiates from the exposed heating means and only a minor portion of the heat input results from the sputtering between the moving cathode and the upper surface of the substrate, particularly during the early stages of the process before the substrate attains an equilibrium temperature range.
  • the metal to be deposited by cathode sputtering may be any metal known to have cathode sputtering properties. However, excellent results are obtained using metals from the group having atomic numbers from 48 to 51 and mixtures thereof, particularly mixtures of metals having atomic numbers that differ by one. Superior properties result from films produced by sputtering from a cathode having a target surface composed of a mixture of indium and tin containing between 1 and 2071 by weight of tin and the balance indium.
  • the apparatus of this invention may also be effectively employed to produce metallic films of metals such as chromium as well as of the metals preferred for the production of metal oxide films.
  • the maximum temperature to which the substrate or substrates are subjected during sputtering depends on the size and nature of the substrate. For example,
  • the atmosphere in which cathode sputtering takes place is preferably at a pressure less than 10 torr.
  • the atmosphere is carefully controlled by introducing a metered amount of oxygen and inert gas (preferably argon) to replace the gas removed by a vacuum pump.
  • a still further improvement provided by the present invention that results in a more uniform deposition of coating is the use of a scanning cathode that reciprocates in uniformly spaced relation to the glass surface APPARATUS FOR COATING GLASS CROSS-REFERENCE TO RELATED I APPLICATIONS
  • a scanning cathode that reciprocates in uniformly spaced relation to the glass surface
  • cathode sputtering is conducted in a low pressure atmosphere of oxygen and an inert gas, preferably argon, in which the oxygen content of the mixture is controlled within limits determined by the temperature developed in the substrate during the cathode sputtering operation.
  • Exposed electroconductive heating wires coupled electrically to a low voltage source to be coated during the cathode sputtering operation.
  • the reciprocation of the cathode with respect to the sheet causes each increment of the glass sheet that is sputtered as the cathode r eciprocates in spaced relation to the substrate to be coated in small increments.
  • This provides greater overall uniformity of coating for the substrate than a cathode sputtering operation using a large cathode of substantially the same size as the large glass sheet to be coated (for example, in excess of 6 inches for each dimension), because plasma emanating from a large cathode tends to concentrate in the central portion of the cathode and this concentration results in a similar concentration of coating on the substrate surface.
  • the present invention provides a technique wherein a "glass sheet is inserted into a vacuum coating chamber for coating and its processing is completed to form, a coated article having the requisite optical and electroconductive characteristics before the article'is removed I from the vacuum coating chamber.
  • FIG. 3' is a partly schematiic end view corresponding to the side view of FIG. 2;
  • FIG. 4 is a schematic representation of the apparatus of this invention showing the relationship of the means for controlling process conditions in the sputtering chamber.
  • the glass is cleaned with a mixture of 50% npropanol in water. If the glass has a surface stain or other surface defect,'mild blocking with cerium oxide is advised. Otherwise. the cleaning with the water-npropanol mixture is sufficient.
  • a gradually increasing voltage is slowly applied from a high voltage source (preferably 5000 volts DC. or more) to the cathode and a glow discharge starts. Rapid application of high voltage oftencaus es arcing and the possibibility of damage to the power supply.
  • a high voltage source preferably 5000 volts DC. or more
  • the resistance of the deposited film is monitored continually.
  • the oxygen concentration is varied to maintain a controlled rate of resistance decrease. If this is not done, the presence of too much oxygen can cause too slow a rate of decrease of resistance or even an increase in resistance. Too little oxygen can produce an opaque metallic film.
  • the amount of oxygen required in the gas mixture varies with many other system parameters as follows:
  • the amount of water vapor in the system The water vapor decomposes under the influence of the glow discharge.
  • the hydrogen ions carry current in the system but are ineffective in sputtering because of their low mass.
  • the oxygen ions produced by dissociation of water molecules in the system cause oxidation of the film. Even if the system is pumped or flushed with argon for many hours before coating, the glow disehrge can still release absorbed water vapor from the surfaces in the system.
  • the ionized gas atoms in this case argon and oxygen ions. are attracted to the cathode by the applied potential. An exchange of momentum takes place as the ions penetrate the target. Atoms of the target material are ejected and also electrons. Both travel away from the cathode, the charged electrons gaining energy because of the electric. field. At some point (the limit of the cathode dark space) the electrons have gained sufficient energy to ionize additional gas atoms and the process is repeated. The metal continue and are eventually deposited onto the substrate.
  • the momentum exchange process taking place at the cathode is most effective with heavy ions such as argon.
  • Argon is chosen for most sputtering processes because of its low cost and high mass. Xenon and krypton would produce more efficient sputtering but are expensive for general use.
  • the sputtering rate is greater at lower oxygen concentrations 2.
  • the specific resistivity generally decreases at lower oxygen concentrations.
  • EXAMPLE Ill Using a cathode composed of 9% tin and 91% indium by weight, a cathode to substrate distance of 2 inches. a total gas pressure of 23 millitorr, maintaining a substrate temperature at 550F, a voltage of 3000 volts and a current of 55S milliamperes during 8 minutes of cathode sputtering produced the following film thicknesses having the resistance per unit square recorded in the following table for various samples coating in argonoxygen mixtures having the recorded oxygen concentration added by volume.
  • cathode to substrate distance was 2 inches and a voltage of 3000 volts was impressed for 10 minutes to produce a current of 500 milliamperes during cathode sputtering under various concentrations of oxygen.
  • the concentration of tin in the indium cathode may range from I to 20% and has an optimum at around If no tin is added, the lowest resistance films cannot be made even though fairly high conductivity can be obtained from oxygen variances produced by low oxygen pressure.
  • the films so made with pure indium cathodes are prone to change resistance on heating at temperatures above about 150F., whereas films produced from indium cathodes containing 10% tin have stabel electrical conductivity even when heated to 300F.
  • a film made by sputtering a 10% tin- 90% indium cathode at 3000 volts, 250 milliamperes in a 312% oxygen, 96.8% argon l9 millitorr system and 600F.substrate temperature has a resistance of 90 ohms per square when freshly made. This changes to 85 ohms per square as it is cooled and exposed to air at 300F.
  • EXAMPLE VI The following experiments are performed using essentially the same equipment as before at 3000 volts, 2 inches cathode to substrate spacing and 600F. substrate temperature. a cathode composition of 5.6% tin, 94.4% indium, a current of 180 milliamperes and a pressure of 20 millitorr. Experiments were performed at various oxygen concentrations. Resistivities were measured after 15 minutes of cathode sputtering for each oxygen concentration tested. A first sample developed a film having a resistivity of 280 ohms per square after cathode sputtering under such conditions in a system containing 6.3% oxygen. After cooling in vacuum. the resistivity of the film dropped to ohms per square.
  • a second sample cathode sputtered in a system containing 3.2% oxygen under otherwise-identical conditions developed a film having a re sistivity of 75 ohms per square. This was reduced to 40 ohms per square by 5 minutes at 700F. in argon at 0.05 millitorr.
  • a third sample cathode sputtered inn a 1% oxygen system developed a film having a resistivity of 23 ohms per square, which became 26 ohms per square after cooling in a vacuum and remained 26 ohms per square after further exposure to air.
  • EXAMPLE Vll Using a fixed cathode 5 inches square of 5.6% tin and the balance indium spaced .l.4 inches from a 4 inch square sample of polished plate glass in center to center alignment, cathode sputtering for 60 minutes in an atmosphere at 37 millitorr pressure containing 24% hydrogen. ll% oxygen and 65% argon by volume at a voltage of 3,500 volts DC and 750 milliamperes current for 60 minutes developed a sample temperature of 600F. A film having an estimated thickness of 6,000 Angstroms, a resistivity of 3 to 4 ohms per square and a transmission of about 72% resulted. No attempt was made to control the substrate temperature.
  • the film can beneficially be cooled from its operating temperature in high vacuum (say below 10 torr).
  • a lower pair of parallel tracks 30 extend horizontally the length of the cylindrical chamber to receive a 1 Theater supporting carriage32.
  • An upper pair of parallel tracks'33 is also provided for purposes to be described later.
  • the heatersupp'orting carriage 32 has rollers 34 that ride on the tracks 30 from a position within the cylindrical chamber lt) to a lower set of tracks 36 supported on a loading table 38 disposed outside the I chamber 10.
  • the loading table 38 is provided with pivoted casters 39 to facilitate placing the loading table 38 in alignment with the cylindrical chamber 10 both before and after cathode sputtering operation.
  • a grounded bar 46 extends parallel to bus bar 44.
  • the bus bars 44 and 46 are /2 inch by 2 inch in cross section and 6 feet long and are interconnected at each inch of length by one of a series of parallel heating wires 48.
  • Pivots 50 are connected at one end to the grounded bus bar 46 and at their other end to a grounded expansion spring 52.
  • the spring loading keeps the heating wires straight and parallel as they become heated during the application of voltage across the bus bars.
  • An insulated power line 54 connects the bus bar 44 to a source of A.'C. voltage (not shown) outside the chamber 10 through an insulated terminal 55.
  • This source is preferably no morethan 50 volts and the heating wires are nich'rome type 5 wire (17 gauge) and are approximately 3 feet long.
  • the anode plate supports a series of posts 56 arranged in checkerboard arrangement to support one or more glass sheets during a cathode sputtering operation.
  • the posts 56 are off-set with respect to the paths traversed by the parallel heating wires 48 and are of such size that the glass is spaced about 2 inches from the plane occupied by the heating wires 48.
  • a thermal sensing device 49 peers through an aperture in anode plate 40 and is focused on the substrate to record its temperature.
  • the posts 56 and the anode 40 are both vertically adjustable in any manner well known in the art, such as by-adjustment nuts and externally threaded shafts.
  • the posts 56 are provided with rounded or' pointed heads 57 to provide minimum areas of contact while supporting the substrate G.
  • the posts may be adjusted'vertically to support flat or curved glass.
  • the spacing between adjacent post may be from 1 to-6 inches depending on the size of substrate treatedand the temperature of treatment.
  • the upper carriage 60 supports a set of brackets 62 at each longitudinal end thereof.
  • One of theshafts 63 is connected to a reversing drive motor (not shown) located outside the chamber 10.
  • Chain 66 is connected to a lug 70 connected to wheels 72 that ride on a rail 74.
  • the lug70 is connected to one side of a transverse bar member 76.
  • the heater supporting carriage 32 is provided with an i 78 is connected to chain 68.
  • the other end of the transverse bar member 76 is connected to wheels 79 that ride on a rail 80 parallel to rail 74.'Actuation of the reversing drive motor causes the transverse bar member 76 to reciprocate transverse to its length.
  • the transverse bar member 76 is attached in insulated coordination'on to a cathode 77.
  • the latter has a coating of metal (for example 5% tin and the rest indium) on its bottom surface.
  • a cathode connection 82 is connected to the transverse cathode 77.
  • a flexible insulated wire 83 interconnects the cathode connection 82 to a coupling (not shown) adapted for connection to the cathode of a high DC. voltage power source (not shown) to supply power for sputtering located outside the chamber 10.
  • a pair of water connectors 90 are connected to cooling pipes 91 supported between the bar member 76 and the cathode 77 to cool the latter when necessary.
  • the cathode 77 scans the glass substrate G supported at the top of the checkerboard array of posts 56.
  • the carriages 32 and 60 are removable from the chamber 10 for loading and unloading glass sheets (including framing sheets that abut the edges of the sub strate to avoid edge effects) and for any maintenance needed.
  • the electrical connectors are very carefully insulated and are sufficiently long to allow for move ment of the cathode 77 and the carriages 32 and 60.
  • the connectors can be attached to exterior water sources at various additional feed throughs. Suitable packing seals are provided to maintain a good seal for the chamber 10 at each feed through. These connectors and seals are available commercially and form no part of the present invention.
  • thermocouples 56 and positioned so that the bead of each thermo couple is in contact with the underside of the substrate.
  • the signal leads, 102, of the thermocouples are brought out through the chamber wall by means of a sealed feed through.
  • the thermocouples may be connected in parallel to provide a signal corresponding to the average substrate temperature or may be separately maintained and connected to conventional indicators, recorders or controllers, 103. One to ten thermocouples will typically be employed.
  • thermocouple signal upon which control is based is directed to a conventional temperature indicator, recorder, controller, 103, by wire conductors.
  • the temperature controller, 103 is connected to a variable auto transformer, 104, on the primary of a conventional low voltage transformer, 105, which has its secondary connected to bus bar, 44, by means of powerline, 54.
  • the control loop may be designed for manual control with no conventional indicator, recorder, controller provided but rather with the control thermocouple signal directed to a conventional indicator, recorder. In this instance an operator controls the temperature by manual adjustment of the variable auto transformer, 104, responsive to the observed recorded temperature.
  • the temperature of the substrate may also be monitored by an externally positioned thermal sensing device, 49, such as a radiation pyrometer.
  • a pyrometer for example an Ircon radiamatic pyrometer, may be positioned outside the chamber and aimed through a window, 17, in the chamber wall and through an opening, 43, in the anode plate, 40, at the substrate, with the device focused at the substrate.
  • the window, 17, will preferably be constructed of a high infrared transmittance material, such as calcium fluoride, and the pyrometer will be calibrated to compensate for any infra red absorption by the window.
  • the pyrometer signal leads may be connected to a conventional indicator. recorder, controller and powerstat as described before, providing an alternate means of temperature control responsive to a detected substrate temperature.
  • the pyrometer or thermocouples may be connected through an indicator, recorder, controller to valve operators, 106, operating the position of the valves on lines 24 and 26, or these valves may be operated manually responsive to indicated or recorded temperatures.
  • the means for controlling oxygen and argon in flow comprises valves on the lines 24 and 26.
  • micrometer calibrated needle orifice valves will be employed these are characterized in the art as controlled leak valves. In the practice of this invention described here Vactronic valves have been used in combination with Brooks rotometers.
  • the inflow of oxygen and argon may be controlled by manual adjustment of these valves responsive to the indicated or re corded substrate temperature prov'idedby'the means described above, or a conventional controller may be employed in combination with a stepping 'motor, pneumatic actuator or the like to act as a valv e operator, 106, adjusting the valve positions.
  • the preferred means for monitoring the conductivity or resistance of the films during sputtering comprises a monitor plate, 110, connected by means of electrical leads, 113, to an externally positioned indicator, re corder or controller, 114, preferably a conventional ohmmeter.
  • the monitor plate, 110 is preferably a 4 inch-by-4 inch glass plate having ceramic silver bus bars, 111 and 112, on opposite sides of one major surface.
  • An electrical lead is connected to each bus bar, and these leads, 113, are connected to an ohmmeter, such as Simpson Model 260 or the like.
  • the monitor plate, 110 is placed adjacent a workpiece or, substrate, G, to be sputter coated and is sputter coated simultaneously with the workpiece.
  • the resistance is noted during sputtering, and the valves on lines 24 and 26 are adjusted responsive thereto.
  • This adjustment may be manual, or the indicating meter employed may be a conventional indicator, recorder, controller, 114, connected to a valve operator, 115, as described above.
  • the parameters include an atmosphere of 20 millitorr, a cathode to sub strate spacing of 2 inches, 3,000 volts D.C., a cathode 6 inches wide and 40 inches long, a scanning path 36 inches long over the sample, a 2 inch frame of glass surrounding the sample and reciprocating the cathode in a direction transverse to its length at a speed to provide a complete cycle in 20 seconds.
  • the following minimum partial pressures of oxygen are estimated at the following substrate temperatures to produce a clear, metal oxide film of low resistance: 20% or 4 millitorr at 300F., 9% or 2 millitorr at 400F., 5% or I millitorr at 500F.. 4% at 600F.. and 3% at 700F. (or below 1 millitorr at above 500F.)
  • EXAMPLE Vlll Ten samples of /8 inch thick twin ground plate glass were cathode sputtered using the illustrated apparatus at a l .5 inches cathode to substrate spacing with a cathode 6 inches wide and 40 inches long having a sputtering surface composed of 10% tin and and 90% indium, for, 75 minutes at a DC. voltage of. 3,200 volts with I heating wires initially energized at 24 volts (350 amperes) for 10 minutes. followed by 5 minutes at volts (250 amperes) followed by 12 volts (150 amperes) for 2 minutes, then no voltage for the remainder of the cathodesputtering.
  • Specific resistance is the resistance between opposite faces of a cubic centimeter of material and is expressed by the equation where p is the specific resistance.
  • R is the resistance of the conductor.
  • A is the cross-sectional area of the conductor, and L is the length of the conductor.
  • this expression becomes RXWXI P I wherein Wand L are the surface dimensions and I is the film thickness.
  • W and L are equal and p R X r or R (resistance for a square area of surface) p/t.
  • cathodes having indium coatings and indium-tin alloys as coatings it is understood that other metals and alloys from the group of elements of atomic numbers 48 to 51 may be used. for example. tin cathodes containing up to 15% antimony produce films having better than luminous transmittance and about 100 ohms per square and cadmium cathodes containing up to 20% indium produce films having better than 60 7( luminous transmittance and about L000 ohms per square in resistivity.
  • the apparatus aspect of the present invention makes it possible to irradiate the substrate simultaneously with the cathode sputtering operation.
  • This hitherto unobtained result is made possible by limiting the voltage applied to the spaced heating elements in the form of the resistance wires 48 to a maximum of 50 volts.
  • This voltage particularly it if is a AC. voltage, is insufficient to cause arcing between the heating wires and grounded elements within the chamber.
  • the heating elements are spaced from or insulated from grounded elements.
  • An apparatus for applying a uniform, transparent. metalcontaining. electronconductive coating to a substrate comprising:
  • c. means comprising a cathode and an anode for sputtering said coating onto said substrate while its temperature is elevated substantially, said cathode sputtering means having its cathode spaced from and in facing relation to said supporting means;
  • said radiant heating means being spaced from and in facing relation to said supporting means such that said support means is disposed between said cahode and said radiant heating means, and said radiant heating means comprising means for radiating heat toward substantially all the area embraced by said supporting means.
  • said radiant heating means comprises electric resistance 18 heating means for operating at voltages substantially lower than a voltage sufficient to operate a sputtering cathode.
  • said radiant heating means is coupled to an alternating current power source for providing a voltage across said radiant heating means of less than about 50 volts.
  • said cathode is coupled to a direct current power source for providing a voltage between said cathode and said anode of at least about [.000 volts.
  • said radiant heating means is provided with means for controlling the voltage thereto responsive to the temperature of said substrate, and said apparatus further comprises a plurality of temperature detecting means in operative communication with the area of said supporting means for detecting the temperature of said substrate supported thereby at a plurality of corresponding sites with said plurality of temperature detecting means being connected in parallel for providing an average substrate temperature to said controlling means.
  • said cathode has a sputtering surface that is elongated having a length greater than one dimension of a substrate receiving portion of said substrate supporting means; said apparatus further comprising means for reciprocating said cathode in a direction transverse to its length with said sputtering surface facing said substrate supporting means.

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  • Engineering & Computer Science (AREA)
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Abstract

Transparent, electroconductive articles produced by cathode sputtering on refractory substrates, a metal from the group of elements having an atomic number from 48 to 51 and mixtures thereof, and preferably a controlled proportion of tin to indium, in a low pressure atmosphere containing a controlled amount of oxygen at a controlled substrate temperature within a temperature range of 400*F. to a temperature at which the substrate becomes distorted or detrimentally affected, usually at or above 600*F.

Description

Attorney, Agent, or Firm-E. Kears Pollock; Edward I. Mates rl ma m u an fm mm a0 rt a bn wa g0 yum W6 mtah M fimw enm re n k 01mm 0: d .m mn r a en. t um W m e e 00 m. ..4 mmm mm cff Steckelmacher et al.,
Deposition of Optical Film Systems Vacuum, Feb. 2, 1959.
Primary Examiner-Oscar R. Vertiz Assistant Examiner-Wayne A. Langel Transparent lnventor: Frank H. Gillery, Allison Park, Pa.
Assignee: PPG Industries, Inc., Pittsburgh, Pa.
Jan. 3, 1974 Appl. No.: 430,424
Related US. Application Data Continuation of Ser. No. 241,543, April 6, 1972, abandoned, which is a continuation-in-part of Ser. No. 60,002, July 31, 1970, abandoned.
204/298; 204/192 Int. C23c 15/00 204/ 192, 298
References Cited UNITED STATES PATENTS 12/1968 Brichard..........
United States Patent Gillery 1 APPARATUS FOR COATING GLASS [22] Filed:
[58] Field of Search.............................
f, and preferably a controlled proportion of tin to indium, in a low pressure atmosphere containing a controlled amount of oxygen at a controlled substrate temperature within a temperature range of 400F. to a temperature at which the substrate becomes distorted or detrimen- Vegh et a1. FOREIGN PATENTS OR APPLICAT 3,480,535 11/1969 B1oom.............. 3,506,556 4/1970 Gillery et a1. 3,531,335 9/1970 I-leyerdahl et a1 3,630,873 12/1971 Moore et a1. 3,655,545 4/1972 Gillery et a1. 3,779,891 12/1973 6 Claims, 4 Drawing Figures tally affected, usually at or above 600F. IONS 4/1940 United Kingdom............,.... 204/298 US Patent Sept. 23,1975 Sheet 1 of 4 3,907,660
Sheet 2 of 4 Sept. 23,1975
US Patent Sheet 3 of 4 US Patent Sept. 23,1975
US Patent Sept. 23,1975 Sheet4 of4 3,907,660
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are used to heat the substrate by radiation rather than by convection or conduction by contact during the cathode sputtering. The heating wires are equally spaced from one another and are disposed in an area aligned with and extending beyond the area occupied by the substrate to insure a uniform blanket of radiant heat at the substrate.
This arrangement using radiant heat is superior to the prior art heat transfer by conduction by contact when an attempt is made to coat glass substrates whose length is more than 6 inches and whose width is more than 6 inches. This superiority from using radiant heat rather than conduction by contact with an anode to control temperature makes it possible to control the substrate temperature independently of the anode temperature, thus bringing better control to the coating operation.
ln coating very large sheets, the cathode target has been made of an elongated construction having one dimension longer than one dimension of a substrate and providing means for reciprocating the cathode along an axis with a displacement greater than the other dimension of the substrate. US. Pat. No. 3,414,503 to Brichard shows such a device for coating substrates supported in a vertical plane. This patented apparatus is so arranged that it is impossible to heat a substrate independently of the heat it develops incidental to the sputtering process.
Apparatus conforming to one embodiment for performing the present invention has a series of vertically adjustable supports arranged in two sets of intersecting rows that provide spaced points of support for one or more flat or curved substrates as the case may be. The bottom substreate surface is supported on spaced points having minimum heat exchange relation at the points of support. Hence, the radiant heating means disposed to one side of the supported substrate or substrates is able to provide a uniform heating pattern over the entire bottom surface of the substrate so that it now becomes possible to maintain the substrate temperature approximately uniform even when a cathode is reciprocated in facing relation to the opposite surface of the substrate, since a sufficient portion of the heat input to the substrates treated to contol the substrate temperature radiates from the exposed heating means and only a minor portion of the heat input results from the sputtering between the moving cathode and the upper surface of the substrate, particularly during the early stages of the process before the substrate attains an equilibrium temperature range.
The metal to be deposited by cathode sputtering may be any metal known to have cathode sputtering properties. However, excellent results are obtained using metals from the group having atomic numbers from 48 to 51 and mixtures thereof, particularly mixtures of metals having atomic numbers that differ by one. Superior properties result from films produced by sputtering from a cathode having a target surface composed of a mixture of indium and tin containing between 1 and 2071 by weight of tin and the balance indium. The apparatus of this invention may also be effectively employed to produce metallic films of metals such as chromium as well as of the metals preferred for the production of metal oxide films.
The maximum temperature to which the substrate or substrates are subjected during sputtering depends on the size and nature of the substrate. For example,
ill
thicker glass sheets as thick as V2 inch may be heated to as high as 800F. without distortion. whereas sheets as thin as 0.007 inch maintain good optical shape without distortion at 600F. for time sufficient to produce highly transparent, highly electroconductive films. Chemically tempered glass sheets are heated only to a maximum temperature of approximately 5()OF. during cathode sputtering to avoid any deleterious effects on the temper imposed chemically. These temperatures are below those required for forming transparent electroconductive films by pyrolysis ofa metal salt composition.
The atmosphere in which cathode sputtering takes place is preferably at a pressure less than 10 torr. The atmosphere is carefully controlled by introducing a metered amount of oxygen and inert gas (preferably argon) to replace the gas removed by a vacuum pump.
The electroconductivity of the film is monitored as the film forms and the substrate is heated by an independent heater to within a few degrees of a predetermined temperature. preferably above 500F. The coated article is retained in the sputtering atmosphere after sputtering is stopped and cooled before exposure to air. In case where the value of electrical resistivity is not important, this cooling can be minimal. However. in case the final resistance desired is a minimum, it is desirable to evacuate the sputtering atmosphere and cool the coated article to below the initial cathode sputtering temperature and, even more preferably, to below 30()F., before removing the article from the atmosphere and exposing the coated article to air. Postheating treatment needed in prior art techniques to obtain a lower resistance for the film so formed or to improve its luminous transmittance may be dispensed with provided the substrate temperature is controlled as taught by the present invention.
According to a more sophisticated operation, the partial pressure of oxygen in the low pressure atmosphere of the sputtering chamber is initially relatively high as the cathode sputtering begins and is reduced as the temperature of the substrate is increased during the cathode sputtering process performed simultaneously with independent heating.
This sophisticated version of the present invention involves initially providing an excess of oxygen over the partial pressure needed to balance the amount of metal being sputtered during the initial phase of cathode sputtering after the substrate temperature reaches a minimum of 400F. due to the application of heat from an external heat source. As the temperature of the substrate increases above the initial temperature at which cathode sputtering begins. the partial pressure of oxygen is reduced in the mixture added to replace the gases that are evacuated. The aforsaid technique develops a clear film that does not require post-heating in air as is necessary with earlier techniques in which only a trace of oxygen is used during the sputtering in the low pressure atmosphere. Furthermore. the conductivity of the resulting coatings as well as the transparency are superior to those resulting from prior art techniques involving the initial application of cathode sputtering in an atmosphere that has an excess of oxygen followed by post heating in a reducing atmosphere.
A still further improvement provided by the present invention that results in a more uniform deposition of coating is the use of a scanning cathode that reciprocates in uniformly spaced relation to the glass surface APPARATUS FOR COATING GLASS CROSS-REFERENCE TO RELATED I APPLICATIONS This is a continuation of application Ser. No. 24l,543, filed Apr. 6, 1972 which is acontinuation-inpart of application Ser. No. 60,002 filed July 31, 1970. These earlier applications are now abandoned. This application is also related to applicants copending application entitled Glass Coated with an Oxide of a Metal Having an Atomic Number of From 48 to 51 and filed on even date herewith.
BACKGROUND OF THE INVENTION This invention relates to COATING GLASS and 'particularly relates to transparent, electroconductive articles produced by depositing a transparent conductive film of a metal or metal oxide, preferably selected from the group of elements having anatomic number from 48to 51 and mixtures thereof, on a transparent ceramic base using a vacuum process, such as vacuum evaporation or cathode sputtering, preferably the latter: In particular, this invention relates to apparatus for producing such coated articles.
Prior to the present invention, others have attempted to apply conductive coatings by the vaccum evaporation of various metal oxides such as indium oxide. These techniques were developed as a lower temperature coating operation to replace the prior art pyrolixation processes in which it was necessary to heat the substrate to a temperature at which it softens and distorts,
and/or loses a temper previously imposed either thermally or chemically at these elevated temperatures.
In a pure oxygen atmosphere, vacuum evaporation must be done very slowly to insure that the metal combines with oxygen and to minimize decomposition which occurs. The films produced often have to be heated subsequently to the vacuum evaporation process to improve their clectroconductivity.
- Cathode sputtering has also been used to form oxide films of the aforesaid metals, particularly indium oxide films. Some of these previous methods of producing sputtered indium oxide films rely on the oxidation of the cathode and the sputtering of this oxide to produce the film. The rate of sputtering is limited by the rate of oxidation of the cathode. The cathode temperature cannot be raised to increase the rate of oxidation because indium melts at the very low temperature of about 315F. Others have tried to increase the rate of cathodeoxidation by using pure oxygen as a sputtering gas. This is inefficient because oxygen gives a low sputtering yield and because the stoichiometry of the finished film is difficult to control. Others have used sequential treatments in oxygen and argon, the former to oxidize the cathode and the latter to transfer the oxide from the cathode to the substrate. A multiple step process is inconvenient, time consuming, expensive and each added step increases the likelihood of losing control of the process.
Stillanother method of obtaining indium oxide films is described in U.S. Pat. No. 2,825,687 to Preston. In this patent, indium or other metal oxide is sputteredor the metal is sputtered in-an atmosphere containing only a trace of oxygen to produce-a colored or opaque film, and the film is subsequently heated in air to develop a permanent conductivity and improve film transmission. Again this process is inconvenient, time consuming and results in a high resistance film with inferior optical properties.
In an attempt to improve the optical transmission coefficient as well as the clectroconductivity of the resulting film, it has been proposed in application Ser. No.
709,l35 of Frank H. Gillery and Jean P. Pressau, filed February 28, 1968 to cathode sputter in a low pressure atmosphere containing sufficient oxygen to assure the formation of a colorless film havingadequate optical properties but insufficient electroconductivity, and then to heat the coated article in an oxygen-deficient atmosphere for sufficient time to increase'the electroconductivity and to discontinue the heating before the film develops a color. This technique produces films having a better combination of optical and electrical properties than those of the hitherto prior art. However, this process involves either evacuation of oxygen from'the low pressure atmosphere for the post-heating step or removal of the coated article to an evacuated environment for the post-heating step. Either alternative is time consuming.
Cathode sputtering causes a substrate to be heated. However, such heating is hard to regulate and nonuniform coating results. U.S. Pat. No. 3,369,989 to Kay, et al. discloses apparatus for controlling the temperature ofa substrate by providing substrate mounting means in the form of a hollow anode enclosing heating and cooling elements. The upper surface of the anode supports the substrate in surface to surface contact therewith and is alleged to be capable of controlling the substrate temperature at 300C. with 1C. throughout the extent of a small substrate. Thispatentimplies that the substrate must be maintained at a constant temperature throughout the cathode sputtering operation. The time needed to heat the substrate to an equilibrium temperature before starting cathode sputtering increases the time necessary for a complete coating operation. In addition, if the substrate is glass, whose length and width are more than 6 inches, it is impossible to maintain the uniformity of contact needed to provide conductivity of sufficient uniformity (less than '207z variation in local conductivity throughout the substrate) to satisfy present commercial requirements.
SUMMARY OF THE INVENTION It has now been discovered that it is not necessary to maintain the substrate at a constant temperature throughout the cathode sputtering operation provided the substrate is heated to a minimum temperature to about 400F. before starting the cathode sputtering and the substrate temperature varies between 400F. and a temperature below which the substrate becomes distorted or detrimentally affected during sputtering and the substrate is cooled to below the temperature at which cathode sputtering is started :before removing the substrate from the low pressure atmosphere used for cathode sputtering. Frequently, the low pressure atmosphere is evacuated during the cooling that follows cathode sputtering.
According to a sophisticated version of the present invention, cathode sputtering is conducted in a low pressure atmosphere of oxygen and an inert gas, preferably argon, in which the oxygen content of the mixture is controlled within limits determined by the temperature developed in the substrate during the cathode sputtering operation. Exposed electroconductive heating wires coupled electrically to a low voltage source to be coated during the cathode sputtering operation. The reciprocation of the cathode with respect to the sheet causes each increment of the glass sheet that is sputtered as the cathode r eciprocates in spaced relation to the substrate to be coated in small increments. This provides greater overall uniformity of coating for the substrate than a cathode sputtering operation using a large cathode of substantially the same size as the large glass sheet to be coated (for example, in excess of 6 inches for each dimension), because plasma emanating from a large cathode tends to concentrate in the central portion of the cathode and this concentration results in a similar concentration of coating on the substrate surface.
Another factor in promoting more uniformity of coating is the use of a frame of glass or other material surrounding the articleto be coated. This avoids edge effects. I 7,
There are many parameters that determine the film forming rate and the nature of the film formed. The present invention has made possible the selection of the more important parameters that determine certain film characteristics during the cathode sputtering operation toobtain suitable repeatabilityof optical and electrical characteristics from article to article. In other words, the present invention provides a technique wherein a "glass sheet is inserted into a vacuum coating chamber for coating and its processing is completed to form, a coated article having the requisite optical and electroconductive characteristics before the article'is removed I from the vacuum coating chamber.
' Iished, the temperature of the substrate and the partial pre'ssure'of oxygen in the low pressure atmosphere are kept in balance to obtain optimum quality films. Generally, the elee'troconductivity of a film produceda't a high substrate temperature during cathode sputtering is more permanent than that of a film produced at a lower substrate temperature, but a practical maximum temperature is one that is below the deformation temperature of the substrate. The composition of metal used for the cathode, particularly in the case of indiumtin cathodes, for example, the ratio of tin to indium, is a factor in the electroconductivity of the film formed. Films from pure indium cathodes are less electroconductive than those produced using a small proportion of tin and have less stable electroconductivities. Typically. indium cathodes having 1% to by weight of tin yield highly conductive films.
BRIEF DESCRIPTION OF THE DRAWINGS vacuum chamber, and
FIG. 3'is a partly schematiic end view corresponding to the side view of FIG. 2;
FIG. 4 is a schematic representation of the apparatus of this invention showing the relationship of the means for controlling process conditions in the sputtering chamber.
DESCRIPTION OF THE PREFERRED EMBODIMENTS The following experiments to coat 4 inch squaresubstrates of soda-lime-silica glass disclose more precisely the effect of the various parameters on the conductivity. its durability of conductivity, filmforming rate and other factors.
For all theexpcriments using glass sheets assubstrates, the glass is cleaned with a mixture of 50% npropanol in water. If the glass has a surface stain or other surface defect,'mild blocking with cerium oxide is advised. Otherwise. the cleaning with the water-npropanol mixture is sufficient.
After cleaning, the glass is placed in position in the chamber and the pumpdown is started. This continues until the pressure reaches 10 torr or below. Argon gas is admitted to the chamber to maintain this pressure and flush the system for several minutes.
A When the system has been purged of the greater part of its residual gas, a mixture of argon and oxygen (0.5 to 15% oxygen) is admitted while still pumping until the pressure is between 5 and 5() millitorr. To conserve gas, the pumping speed is decreased during coating by an adjustable baffle.
A gradually increasing voltage is slowly applied from a high voltage source (preferably 5000 volts DC. or more) to the cathode and a glow discharge starts. Rapid application of high voltage oftencaus es arcing and the possibibility of damage to the power supply.
During pumpdown and voltage applic'atibnQth substrate is being raised in temperature by electricalresistance wire heaters disposed in parallel relation. for example. at 1 inch spacing and 2 inches fromthe opposite surface of the substrate from that coated. According to the present invention, coating is not hegun untilthe substrate is heated to a temperature of 400F, 1
During coating, the resistance of the deposited film is monitored continually. The oxygen concentration is varied to maintain a controlled rate of resistance decrease. If this is not done, the presence of too much oxygen can cause too slow a rate of decrease of resistance or even an increase in resistance. Too little oxygen can produce an opaque metallic film.
The amount of oxygen required in the gas mixture varies with many other system parameters as follows:
I. The amount of residual oxygen in the system.
2. The amount of water vapor in the system. The water vapor decomposes under the influence of the glow discharge. The hydrogen ions carry current in the system but are ineffective in sputtering because of their low mass. The oxygen ions produced by dissociation of water molecules in the system cause oxidation of the film. Even if the system is pumped or flushed with argon for many hours before coating, the glow disehrge can still release absorbed water vapor from the surfaces in the system.
3. The temperature of the substrate, which controls the rate of reaction of indium or other metal with oxygen and also the metal-oxygen equilibrium.
4. The rate of deposition. To a certain extent the rate of arrival of indium on the substrate has to be balanced against the rate of bombardment by oxygen.
The ionized gas atoms, in this case argon and oxygen ions. are attracted to the cathode by the applied potential. An exchange of momentum takes place as the ions penetrate the target. Atoms of the target material are ejected and also electrons. Both travel away from the cathode, the charged electrons gaining energy because of the electric. field. At some point (the limit of the cathode dark space) the electrons have gained sufficient energy to ionize additional gas atoms and the process is repeated. The metal continue and are eventually deposited onto the substrate.
The momentum exchange process taking place at the cathode is most effective with heavy ions such as argon. Argon is chosen for most sputtering processes because of its low cost and high mass. Xenon and krypton would produce more efficient sputtering but are expensive for general use.
The oxygen is present to produce metal oxide rather than metal films. The metal oxide films are transparent whereasthe metal films are not. In this particular system the oxidation appears to take place on the substrate, since it is greatly affected by substrate temperature. Under different conditions, oxidation of the'cathode and oxide sputtering may take place at a slower sputtering rate not desired for commercial operations.
EXAMPLE l OXYGEN CON- FILM RESISTANCE RESlSTlVlTY CENTRATION THICKNESS OHMSl- OHM CMS.
(A) SQUARE 6.371 1410 I50 1.96 X 10' 3.2 /1 I700 92 L55 X l L67 2260 S6 l.l2 l0 L357! 2700 36 0.921 X l0 l.0l'/r' 3400 29 0.985 X 10 0.7% Metallic Indium Film Within the limits of measurement, the above results show the following:
1. The sputtering rate is greater at lower oxygen concentrations 2. The specific resistivity generally decreases at lower oxygen concentrations.
3. The lower limit of oxygen concentration suitable for cathode sputtering is reached when metallic indium rather than indium oxide is produced.
EXAMPLE [I The following samples are coated under conditions similar to those used in Example 1 except that the substrate temperature and oxygen concentration is varied to produce the following results.
SUBSTRATE OXYGEN RESlSTlVlTY TEMPERA- CONCENTRA- (OHMS/SQUARE) TURF. TION 5 400F. l.()'/( 93 6 l 0F. l .0'7: 29 800F. 1.071 l7 400F. L357: 75 610F. l.35'7l 36 800F. 1.35% l9 l0 400F. 1.671 I76 6l0F. l .691 V 56 800F. L671 l4 400F. 3.2'7' )l0 400F. 3.27: 670 6 10F. 3.271 92 800F. 3.2/71 50 I5 400F. 6.371 590 610F. 6.37: I50 800F. 6.3% lZl The above example indicates that the temperature of the substrate while the film is being deposited is important. The higher temperatures give the best results but in this work the highest temperature investigated was 800F. since much higher temperatures than this will affect the soda-lime glass substrates used as samples. At temperatures lower than 400F., the oxygen pressure required to produce conductive films becomes so critical that metallic indium films are often inadvertently produced. At the lower temperatures also the rate of reaction of indium atoms with oxygen atoms on the substrate becomes controlling and the rate of deposition of indium may have to be decreased.
Further experiments were preformed using cathodes of different compositions and maintaining the substrate at the indicated substrate temperature for each experiment. The controls and results obtained are enumerated in Examples III, IV and V for different cathodes.
EXAMPLE Ill Using a cathode composed of 9% tin and 91% indium by weight, a cathode to substrate distance of 2 inches. a total gas pressure of 23 millitorr, maintaining a substrate temperature at 550F, a voltage of 3000 volts and a current of 55S milliamperes during 8 minutes of cathode sputtering produced the following film thicknesses having the resistance per unit square recorded in the following table for various samples coating in argonoxygen mixtures having the recorded oxygen concentration added by volume.
RESULTS FROM 9% TIN )l71 lNDlUM CATHODE Oxygen Film Thickness OHMS Per Concentration Angstroms Square Remarks 10% l098 I00 Clear film 971 1298 l l0 8'7: l3 I0 I I0 771 I069 1 l0 6'/( 1472 80 s92 l6l9 s5 4% I855 65 3% 1885 50 27: 2356 2S 171 25 Cloudy film l/; 50 Gray l'ilm l'/( 60 Cloudy film 1'7! 20 EXAMPLEIV A setup similar to Example lll was used except that the cathode was pure indium, the total gas pressure was 29 millitorr, the substrate temperature was 600F, the
cathode to substrate distance was 2 inches and a voltage of 3000 volts was impressed for 10 minutes to produce a current of 500 milliamperes during cathode sputtering under various concentrations of oxygen.
RESULTS FROM PURE lNDlUM CATHODE Thefollowing experiments were performed using a cathode composed of 7.5% antimony and92.5% tin by weight at a cathode substrate distance of 2 inches, a voltage of 3000 volts impressing a current of 600 milliamperes for 15 minutes in various argon-oxygen systems containing different oxygen concentration at a pressure of 33 millitorr. The results are recorded below:
RESULTS FROM 75% ANTIMONY 92.5% TIN CATHODE OXYGEN OHMS PER CONCENTRA- SQUARE REMARKS TlON 10% 700 Clear film 5% 250 Clear film 2% 100 Clear film The concentration of tin in the indium cathode may range from I to 20% and has an optimum at around If no tin is added, the lowest resistance films cannot be made even though fairly high conductivity can be obtained from oxygen variances produced by low oxygen pressure. The films so made with pure indium cathodes are prone to change resistance on heating at temperatures above about 150F., whereas films produced from indium cathodes containing 10% tin have stabel electrical conductivity even when heated to 300F.
For instance, a film made by sputtering a 10% tin- 90% indium cathode at 3000 volts, 250 milliamperes in a 312% oxygen, 96.8% argon l9 millitorr system and 600F.substrate temperature has a resistance of 90 ohms per square when freshly made. This changes to 85 ohms per square as it is cooled and exposed to air at 300F.
A film made by sputtering a pure indium cathode at 3000 volts, 215 milliamperes in an oxygen-argon mixsquare when freshly made but this increases to 150 ohms per square when it is exposed to air at 300F.
EXAMPLE VI The following experiments are performed using essentially the same equipment as before at 3000 volts, 2 inches cathode to substrate spacing and 600F. substrate temperature. a cathode composition of 5.6% tin, 94.4% indium, a current of 180 milliamperes and a pressure of 20 millitorr. Experiments were performed at various oxygen concentrations. Resistivities were measured after 15 minutes of cathode sputtering for each oxygen concentration tested. A first sample developed a film having a resistivity of 280 ohms per square after cathode sputtering under such conditions in a system containing 6.3% oxygen. After cooling in vacuum. the resistivity of the film dropped to ohms per square. Further exposure to air raised the resistivity to ohms per square. A second sample cathode sputtered in a system containing 3.2% oxygen under otherwise-identical conditions developed a film having a re sistivity of 75 ohms per square. This was reduced to 40 ohms per square by 5 minutes at 700F. in argon at 0.05 millitorr. A third sample cathode sputtered inn a 1% oxygen system developed a film having a resistivity of 23 ohms per square, which became 26 ohms per square after cooling in a vacuum and remained 26 ohms per square after further exposure to air.
EXAMPLE Vll Using a fixed cathode 5 inches square of 5.6% tin and the balance indium spaced .l.4 inches from a 4 inch square sample of polished plate glass in center to center alignment, cathode sputtering for 60 minutes in an atmosphere at 37 millitorr pressure containing 24% hydrogen. ll% oxygen and 65% argon by volume at a voltage of 3,500 volts DC and 750 milliamperes current for 60 minutes developed a sample temperature of 600F. A film having an estimated thickness of 6,000 Angstroms, a resistivity of 3 to 4 ohms per square and a transmission of about 72% resulted. No attempt was made to control the substrate temperature.
The above experiment involved the use of hydrogen. in view of the danger involved in handling hydrogen. efforts were directed to developing another technique to produce highly transparent, highly electroconductive metal oxide films by cathode sputtering in the absence of hydrogen.
Smaller substrates have more uniform films when so treated and larger substrates less uniform films when so treated. Accordingly, apparatus containing a scanning cathode modifiedfrom that disclosed in U.S. Pat. No. 3,414,503 to Br ichard and containing heating and cooling elements positioned to control the substrate temperature during a vacuum coating operation was developed to coat substrates having minimum dimensions of about 6 inches on each side. The apparatus is described below.
The resistance of a film after deposition can be changed according to how it is treated. The film after deposition is close to equilibrium with the atmosphere at the temperature involved. If the film is exposed to more oxidizing conditions, it tends to increase in resistance; if it is exposed to more reducing conditions it tends to decrease in resistance. The rate of change is dependent on the film temperature, and with the stability of the film as discussed before.
Thus, it is unwise to allow air to come into contact with the film at temperatures above 300F. On the other hand, if a lower resistance is desired, the film can beneficially be cooled from its operating temperature in high vacuum (say below 10 torr).
Prior to the present discovery of the benefits of heatingthe substrate to a controlled temperature above 400F. during the cathode sputtering operation, the cathode sputtering operation in low pressure atmospheres was difficult to control and it was only occasionally that coated glass samples having adequate optical properties and electroeonductive properties were produced. Of about two hundred experiments performed wherein the sputtering was started at whatever substrate temperature existed in the vacuum chamber. the resistances obtained were considerably higher and optical transparencies lower than those obtained with the temperature controlled substrate operation suggested by the present invention, even though the experiments were performed with small articles that, in retrospect, are easier to coat uniformly than larger articles. Furthermore, many experimental samples formed metallic films and those that were electroeonductive had resistances that varied by asmuch as more than 100:1 ratio from one locality to another. 7
An illustrative example of apparatus suitable for performing the present invention will be described in order to facilitate the ability of one skilled in the art to produce transparent electroeonductive articles having superior optical and electroeonductive properties, particularly those having dimensions of at least 6 inches.
DETAILED DESCRIPTION or APPARATUS I, Referring to-the drawings, a typical-apparatus-for cathode sputtering comprises a horizontally disposed chamber 10 arranged in the form of a horizontallyorientedcylinder'72 inches long and 66 inches in diameter having hinges 11 on which a door 12 is pivoted open.
7 Clamps 13 (FIG. 3)-are provided to lock the door 12. Another end door 14 is closed at its other end. Exhaust shown), respectively. The feed lines 24 and 26 are valved'to control inward flow of the respective gases at a metered rate offlow for each gas. The'chamber l is supported in spaced relation above the ground on vertieal posts 28'. I
A lower pair of parallel tracks 30 extend horizontally the length of the cylindrical chamber to receive a 1 Theater supporting carriage32. An upper pair of parallel tracks'33 is also provided for purposes to be described later. The heatersupp'orting carriage 32 has rollers 34 that ride on the tracks 30 from a position within the cylindrical chamber lt) to a lower set of tracks 36 supported on a loading table 38 disposed outside the I chamber 10. The loading table 38 is provided with pivoted casters 39 to facilitate placing the loading table 38 in alignment with the cylindrical chamber 10 both before and after cathode sputtering operation.
plate on its upper surface. A grounded bar 46 extends parallel to bus bar 44. The bus bars 44 and 46 are /2 inch by 2 inch in cross section and 6 feet long and are interconnected at each inch of length by one of a series of parallel heating wires 48.
The wires occupy an area aligned with and extending beyond the edges of the substrate. Pivots 50 are connected at one end to the grounded bus bar 46 and at their other end to a grounded expansion spring 52. The spring loading keeps the heating wires straight and parallel as they become heated during the application of voltage across the bus bars.
An insulated power line 54 connects the bus bar 44 to a source of A.'C. voltage (not shown) outside the chamber 10 through an insulated terminal 55. This source is preferably no morethan 50 volts and the heating wires are nich'rome type 5 wire (17 gauge) and are approximately 3 feet long.
The anode plate supports a series of posts 56 arranged in checkerboard arrangement to support one or more glass sheets during a cathode sputtering operation. The posts 56 are off-set with respect to the paths traversed by the parallel heating wires 48 and are of such size that the glass is spaced about 2 inches from the plane occupied by the heating wires 48. A thermal sensing device ,49 peers through an aperture in anode plate 40 and is focused on the substrate to record its temperature.
The posts 56 and the anode 40 are both vertically adjustable in any manner well known in the art, such as by-adjustment nuts and externally threaded shafts. The posts 56 are provided with rounded or' pointed heads 57 to provide minimum areas of contact while supporting the substrate G. The posts may be adjusted'vertically to support flat or curved glass. The spacing between adjacent post may be from 1 to-6 inches depending on the size of substrate treatedand the temperature of treatment.
Theloading table 38 is provided with-an outer and upper pair of tracks 58 that extend horizontally laterally beyond and above the plane occupied by the first set of tracks 36 in position to form extensions of tracks 33 within the vacuum chamber 10. These outer tracks 58 support an upper carriage'60 which comprises a frame larger and higher than the heater supporting carriage 32 and enable one to transfer the upper carriage 60 into and out of the chamber 10.
The upper carriage 60 supportsa set of brackets 62 at each longitudinal end thereof. A shaft 63 having sprockets 64 and 65 fixed thereto interconnects the aligned brackets of each set and a chain66 or 68 is entrained about each pair of sprockets 64 or 65, respectively. One of theshafts 63 is connected to a reversing drive motor (not shown) located outside the chamber 10. Chain 66 is connected to a lug 70 connected to wheels 72 that ride on a rail 74. The lug70 is connected to one side of a transverse bar member 76. A similar lug The heater supporting carriage 32 is provided with an i 78 is connected to chain 68. The other end of the transverse bar member 76 is connected to wheels 79 that ride on a rail 80 parallel to rail 74.'Actuation of the reversing drive motor causes the transverse bar member 76 to reciprocate transverse to its length.
The transverse bar member 76 is attached in insulated relatii'on to a cathode 77. The latter has a coating of metal (for example 5% tin and the rest indium) on its bottom surface. A cathode connection 82 is connected to the transverse cathode 77. A flexible insulated wire 83 interconnects the cathode connection 82 to a coupling (not shown) adapted for connection to the cathode of a high DC. voltage power source (not shown) to supply power for sputtering located outside the chamber 10. A pair of water connectors 90 are connected to cooling pipes 91 supported between the bar member 76 and the cathode 77 to cool the latter when necessary. Flexible water lines 92 of electrically insulated material, such as plastic, interconnect the connectors 90 to a water source through a feed through 94 carried at the bottom of the chamber 10. Other suitable water and electrical connectors are mounted in the wall of the chamber in a similar manner. For example. another flexible water line 92 feeds water to the water cooling system 41 for the anode 40.
When the reversing drive motor is actuated, the cathode 77 scans the glass substrate G supported at the top of the checkerboard array of posts 56.
The carriages 32 and 60 are removable from the chamber 10 for loading and unloading glass sheets (including framing sheets that abut the edges of the sub strate to avoid edge effects) and for any maintenance needed. The electrical connectors are very carefully insulated and are sufficiently long to allow for move ment of the cathode 77 and the carriages 32 and 60. The connectors can be attached to exterior water sources at various additional feed throughs. Suitable packing seals are provided to maintain a good seal for the chamber 10 at each feed through. These connectors and seals are available commercially and form no part of the present invention.
The apparatus is provided with sensing and control devices to monitor and control processing conditions in accordance with the preferred methods of carrying out this invention. The temperature of the substrate is mea sured before, during and after sputtering by a plurality of thermocouples, 101, preferably chromel-alumel thermocouples, which are placed between the posts,
56, and positioned so that the bead of each thermo couple is in contact with the underside of the substrate. The signal leads, 102, of the thermocouples are brought out through the chamber wall by means of a sealed feed through. The thermocouples may be connected in parallel to provide a signal corresponding to the average substrate temperature or may be separately maintained and connected to conventional indicators, recorders or controllers, 103. One to ten thermocouples will typically be employed.
The thermocouple signal upon which control is based is directed to a conventional temperature indicator, recorder, controller, 103, by wire conductors. The temperature controller, 103, is connected to a variable auto transformer, 104, on the primary of a conventional low voltage transformer, 105, which has its secondary connected to bus bar, 44, by means of powerline, 54. Alternatively, the control loop may be designed for manual control with no conventional indicator, recorder, controller provided but rather with the control thermocouple signal directed to a conventional indicator, recorder. In this instance an operator controls the temperature by manual adjustment of the variable auto transformer, 104, responsive to the observed recorded temperature.
The temperature of the substrate may also be monitored by an externally positioned thermal sensing device, 49, such as a radiation pyrometer. A pyrometer, for example an Ircon radiamatic pyrometer, may be positioned outside the chamber and aimed through a window, 17, in the chamber wall and through an opening, 43, in the anode plate, 40, at the substrate, with the device focused at the substrate. The window, 17, will preferably be constructed of a high infrared transmittance material, such as calcium fluoride, and the pyrometer will be calibrated to compensate for any infra red absorption by the window. The pyrometer signal leads may be connected to a conventional indicator. recorder, controller and powerstat as described before, providing an alternate means of temperature control responsive to a detected substrate temperature. Also, the pyrometer or thermocouples may be connected through an indicator, recorder, controller to valve operators, 106, operating the position of the valves on lines 24 and 26, or these valves may be operated manually responsive to indicated or recorded temperatures. The means for controlling oxygen and argon in flow comprises valves on the lines 24 and 26. Preferably micrometer calibrated needle orifice valves will be employed these are characterized in the art as controlled leak valves. In the practice of this invention described here Vactronic valves have been used in combination with Brooks rotometers. The inflow of oxygen and argon may be controlled by manual adjustment of these valves responsive to the indicated or re corded substrate temperature prov'idedby'the means described above, or a conventional controller may be employed in combination with a stepping 'motor, pneumatic actuator or the like to act as a valv e operator, 106, adjusting the valve positions.
The preferred means for monitoring the conductivity or resistance of the films during sputtering comprises a monitor plate, 110, connected by means of electrical leads, 113, to an externally positioned indicator, re corder or controller, 114, preferably a conventional ohmmeter. The monitor plate, 110, is preferably a 4 inch-by-4 inch glass plate having ceramic silver bus bars, 111 and 112, on opposite sides of one major surface. An electrical lead is connected to each bus bar, and these leads, 113, are connected to an ohmmeter, such as Simpson Model 260 or the like. The monitor plate, 110, is placed adjacent a workpiece or, substrate, G, to be sputter coated and is sputter coated simultaneously with the workpiece. The resistance is noted during sputtering, and the valves on lines 24 and 26 are adjusted responsive thereto. This adjustment may be manual, or the indicating meter employed may be a conventional indicator, recorder, controller, 114, connected to a valve operator, 115, as described above.
While each particular operation and each particular apparatus has different minimum oxygen partial pressures required to produce a clear film at each substrate temperature, the following parameters were established for a glass sheet 2 feet by 3 feet. The parameters include an atmosphere of 20 millitorr, a cathode to sub strate spacing of 2 inches, 3,000 volts D.C., a cathode 6 inches wide and 40 inches long, a scanning path 36 inches long over the sample, a 2 inch frame of glass surrounding the sample and reciprocating the cathode in a direction transverse to its length at a speed to provide a complete cycle in 20 seconds. The following minimum partial pressures of oxygen are estimated at the following substrate temperatures to produce a clear, metal oxide film of low resistance: 20% or 4 millitorr at 300F., 9% or 2 millitorr at 400F., 5% or I millitorr at 500F.. 4% at 600F.. and 3% at 700F. (or below 1 millitorr at above 500F.)
in a typical operation using an initial oxygen partial pressure of about 10% when the substrate temperature is 400F. at the onset ofthe cathode sputtering. and reducing the rate of oxygen flow as the substrate temperature increases while maintaining the argon flow constant and while evacuating with a vacuum pump rated at 1,300 cu. ft. per minute produces a film having a re sistance of 2 ohms per square and 76% total luminous transmission coefficient as measured by a Gardner Hazemeter after one hour of such treatment. Such high transmission and high conductivity combination is not possible with prior art techniques.
EXAMPLE Vlll Ten samples of /8 inch thick twin ground plate glass were cathode sputtered using the illustrated apparatus at a l .5 inches cathode to substrate spacing with a cathode 6 inches wide and 40 inches long having a sputtering surface composed of 10% tin and and 90% indium, for, 75 minutes at a DC. voltage of. 3,200 volts with I heating wires initially energized at 24 volts (350 amperes) for 10 minutes. followed by 5 minutes at volts (250 amperes) followed by 12 volts (150 amperes) for 2 minutes, then no voltage for the remainder of the cathodesputtering. The cathode was reciprocated at an average linear speed of about 18 feet per minute and the atmosphere of the coating chamber was 4.46% oxy- .gen and the balanceargon maintained at a pressure of pare the conductivity of materials, it is inappropriate for describing the conductivity of very thin films becauseof the difficulty of measuring the thickness'of the film.
Specific resistance is the resistance between opposite faces of a cubic centimeter of material and is expressed by the equation where p is the specific resistance. R is the resistance of the conductor. A is the cross-sectional area of the conductor, and L is the length of the conductor. For a thin film, this expression becomes RXWXI P I wherein Wand L are the surface dimensions and I is the film thickness. For a square area of surface. W and L are equal and p R X r or R (resistance for a square area of surface) p/t. Thus. the conductivities of various types of films having approximately equivalent thickness may be directly compared by comparing resistance per square.
While the examples enumerated above concentrate on cathodes having indium coatings and indium-tin alloys as coatings, it is understood that other metals and alloys from the group of elements of atomic numbers 48 to 51 may be used. for example. tin cathodes containing up to 15% antimony produce films having better than luminous transmittance and about 100 ohms per square and cadmium cathodes containing up to 20% indium produce films having better than 60 7( luminous transmittance and about L000 ohms per square in resistivity.
The samples produced by cathode sputtering in an atmosphere in which the heating elements provided a controlled uniform temperature pattern throughout the area of the substrate had electrical conductivities that did not vary by more than 20% from the most conductive to the least conductive areas. Very rarely are films produced that lack the requisite transparency (over 70%) and electroconductive properties including uniformity of clectroeonductivity as well as low electrical resistivity (below 10 ohms per square) for substrates having at least 6 inch lengths and 6 inch widths. By comparison. earlier efforts to coat glass substrates without uniform heating thereof by heating means independent of the heat induced by sputtering resulted in coatings whose electroconductivities varied by a factor as high as 10 to I from protion to portion of the coated substrate even when scanning the cathode.
Another obvious improvement brought about by the present invention is seen from comparisons of electroconductive and optical properties of films produced by cathode sputtering with those produced by spraying a metal salt composition on a substrate heated to pyrolizing temperature. For example, an article having 10 ohms resistance between oppositely disposed bus bars for an indium oxide coating has a transmission coefficient of only 68% when produced by spraying and for the same composition produced by cathode sputtering using the temperature control criteria described above. In addition, articles with cathode sputtered films have significantly less distortion than those produced by heating to a temperature sufficient for pyrolysis followed by spraying.
The apparatus aspect of the present invention makes it possible to irradiate the substrate simultaneously with the cathode sputtering operation. This hitherto unobtained result is made possible by limiting the voltage applied to the spaced heating elements in the form of the resistance wires 48 to a maximum of 50 volts. This voltage, particularly it if is a AC. voltage, is insufficient to cause arcing between the heating wires and grounded elements within the chamber. The heating elements are spaced from or insulated from grounded elements.
irradiating with heat produced by electrically energized heating wires enables the present apparatus to uniformly heat substrates that do not have optically flat surfaces. Prior art temperature controllers for the substrate which supported the substrate by contact were limited for efficient use with substrates having optically flat surfaces.
While the description of working embodiments has been provided for illustrative purposes, it is understood that variations thereof may be made with out departing from the spirit of the invention as defined in the claimed subject matter that follow.
l claim:
1. An apparatus for applying a uniform, transparent. metalcontaining. electronconductive coating to a substrate comprising:
a. means for providing a low pressure atmosphere not exceeding torr and containing a mixture of oxygen and an inert gas;
b. means for supporting a substrate within said low pressure atmosphere by supporting said substrate at a plurality of support points permitting substantially all of the surfaces of said substrate free from contact by said supporting means;
c. means comprising a cathode and an anode for sputtering said coating onto said substrate while its temperature is elevated substantially, said cathode sputtering means having its cathode spaced from and in facing relation to said supporting means; and
d. means for radiantly heating said substrate to a substantially elevated temperature and for maintaining I such elevated substrate temperature during cathode sputtering, said radiant heating means being spaced from and in facing relation to said supporting means such that said support means is disposed between said cahode and said radiant heating means, and said radiant heating means comprising means for radiating heat toward substantially all the area embraced by said supporting means.
2. The apparatus according to claim 1 wherein said radiant heating means comprises electric resistance 18 heating means for operating at voltages substantially lower than a voltage sufficient to operate a sputtering cathode.
3. The apparatus according to claim 2 wherein said radiant heating means is coupled to an alternating current power source for providing a voltage across said radiant heating means of less than about 50 volts. 4. The apparatus according to claim 2 wherein said cathode is coupled to a direct current power source for providing a voltage between said cathode and said anode of at least about [.000 volts.
5. The apparatus according to claim 1 wherein said radiant heating means is provided with means for controlling the voltage thereto responsive to the temperature of said substrate, and said apparatus further comprises a plurality of temperature detecting means in operative communication with the area of said supporting means for detecting the temperature of said substrate supported thereby at a plurality of corresponding sites with said plurality of temperature detecting means being connected in parallel for providing an average substrate temperature to said controlling means.
6. Apparatus according to claim 1, wherein said cathode has a sputtering surface that is elongated having a length greater than one dimension of a substrate receiving portion of said substrate supporting means; said apparatus further comprising means for reciprocating said cathode in a direction transverse to its length with said sputtering surface facing said substrate supporting means.

Claims (6)

1. AN APPARATUS FOR APPLYING A UNIFORM TRANSPARENT, MATALCONTAINING, ELECTRONCONDUCTVE COATING TO A SUBSTRATE COMPRISING: A. MEANS FOR PROVIDING A LOW PRESSURE AT MOSPHERE NOT EXCEEDING 10-1 TORR AND CONTAINING A MIXTURE OF OXYGEN AND AN INERT GAS, B. MEANS FOR SUPPORTING A SUBSTRATE WITHIN SAID LOW PRESSURE ATMOSPHERE BY SUPPORTING SAID SUBSTRATE AT A PLURALITY OF SUPPORT POINTS PERMITTING SUBSTANTIALLY ALL OF THE SRFACES OF SAID SUBSTRATE FREE FRON CONTACT BY SAID SUPPORTING MEANS, C. MEANS COMPRISING A CATHODE AND AN ANODE FOR SPUTTERING SAID COATING ONTO SAID SUBSTRATE WHILE ITS EMPERATURE IS
2. The apparatus according to claim 1 wherein said radiant heating means comprises electric resistance heating means for operating at voltages substantially lower than a voltage sufficient to operate a sputtering cathode.
3. The apparatus according to claim 2 wherein said radiant heating means is coupled to an alternating current power source for providing a voltage across said radiant heating means of less than about 50 volts.
4. The apparatus according to claim 2 wherein said cathode is coupled to a direct current power source for providing a voltage between said cathode and said anode of at least about 1,000 volts.
5. The apparatus according to claim 1 wherein said radiant heating means is provided with means for controlling the voltage thereto responsive to the temperature of said substrate, and said apparatus further comprises a plurality of temperature detecting means in operative communication with the area of said supporting means for detecting the temperature of said substrate supported thereby at a plurality of corresponding sites with said plurality of temperature detecting means being connected in parallel for providing an average substrate temperature to said controlling means.
6. Apparatus according to claim 1, wherein said cathode has a sputtering surface that is elongated having a length greater than one dimension of a substrate receiving portion of said substrate supporting means; said apparatus further comprising means for reciprocating said cathode in a direction transverse to its length with said sputtering surface facing said substrate supporting means.
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Cited By (40)

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US4006070A (en) * 1971-02-05 1977-02-01 Triplex Safety Glass Company Limited Metal oxide films
US4010291A (en) * 1974-12-16 1977-03-01 Agency Of Industrial Science & Technology Method of making a low resistance indium oxide conductive film
FR2352393A1 (en) * 1976-05-19 1977-12-16 Battelle Memorial Institute PROCESS FOR CARRYING OUT A DEPOSIT IN A LUMINESCENT DISCHARGE ON AT LEAST ONE SUBSTRATE, AND IONIC PICKLING OF THIS SUBSTRATE AND DEVICE FOR IMPLEMENTING THIS PROCESS
US4065600A (en) * 1970-05-20 1977-12-27 Triplex Safety Glass Company Limited Metal oxide films
US4094763A (en) * 1970-07-31 1978-06-13 Ppg Industries, Inc. Sputter coating of glass with an oxide of a metal having an atomic number between 48 and 51 and mixtures thereof
US4113599A (en) * 1977-09-26 1978-09-12 Ppg Industries, Inc. Sputtering technique for the deposition of indium oxide
US4124474A (en) * 1976-11-15 1978-11-07 Commissariat A L'energie Atomique Method and apparatus for controlling the deposition of films by reactive sputtering
US4125446A (en) * 1977-08-15 1978-11-14 Airco, Inc. Controlled reflectance of sputtered aluminum layers
US4132624A (en) * 1971-02-05 1979-01-02 Triplex Safety Glass Company Limited Apparatus for producing metal oxide films
WO1980000713A1 (en) * 1978-09-27 1980-04-17 Massachusetts Inst Technology Transparent heat mirrors formed on polymeric substrates
US4248687A (en) * 1979-07-23 1981-02-03 Massachusetts Institute Of Technology Method of forming transparent heat mirrors on polymeric substrates
US4274936A (en) * 1979-04-30 1981-06-23 Advanced Coating Technology, Inc. Vacuum deposition system and method
US4336119A (en) * 1981-01-29 1982-06-22 Ppg Industries, Inc. Method of and apparatus for control of reactive sputtering deposition
US4379040A (en) * 1981-01-29 1983-04-05 Ppg Industries, Inc. Method of and apparatus for control of reactive sputtering deposition
US4466875A (en) * 1983-11-30 1984-08-21 Ppg Industries, Inc. Auxiliary heater for magnetron sputtering
US4512864A (en) * 1983-11-30 1985-04-23 Ppg Industries, Inc. Low resistance indium oxide films
US4534841A (en) * 1983-03-31 1985-08-13 Leybold-Heraeus Gmbh Solar controlled glazing and method of producing glazing
US4602239A (en) * 1982-01-08 1986-07-22 Ppg Industries, Inc. Spring tensioned wire resistance heater
US4634637A (en) * 1985-11-22 1987-01-06 Gila River Products, Inc. Solar control film
US4647548A (en) * 1983-01-10 1987-03-03 Merck Patent Gesellschaft Mit Beschrankter Haftung Targets for cathode sputtering
US4650557A (en) * 1982-11-03 1987-03-17 Donnelly Corporation Process for making a conductively coated glass member and the product thereof
US4655811A (en) * 1985-12-23 1987-04-07 Donnelly Corporation Conductive coating treatment of glass sheet bending process
US4797317A (en) * 1984-09-27 1989-01-10 Gila River Products, Inc. Solar control window film
EP0224080A3 (en) * 1985-11-26 1989-06-28 Sorin Biomedica S.P.A. Improvements in and relating to the manufacture of prosthetic devices
US4882028A (en) * 1988-01-22 1989-11-21 Micron Technology, Inc. R-F electrodes for removably providing electrical energy to an apparatus during R-F energy reactive treatment processes
US4962049A (en) * 1989-04-13 1990-10-09 Applied Materials, Inc. Process for the plasma treatment of the backside of a semiconductor wafer
US4988424A (en) * 1989-06-07 1991-01-29 Ppg Industries, Inc. Mask and method for making gradient sputtered coatings
US5075256A (en) * 1989-08-25 1991-12-24 Applied Materials, Inc. Process for removing deposits from backside and end edge of semiconductor wafer while preventing removal of materials from front surface of wafer
US5084151A (en) * 1985-11-26 1992-01-28 Sorin Biomedica S.P.A. Method and apparatus for forming prosthetic device having a biocompatible carbon film thereon
DE4131181C1 (en) * 1991-09-19 1993-01-07 Leybold Ag, 6450 Hanau, De
US5213650A (en) * 1989-08-25 1993-05-25 Applied Materials, Inc. Apparatus for removing deposits from backside and end edge of semiconductor wafer while preventing removal of materials from front surface of wafer
US5244559A (en) * 1991-07-31 1993-09-14 Leybold Aktiengesellschaft Apparatus for transport and heat treatment of substrates
US5370684A (en) * 1986-12-12 1994-12-06 Sorin Biomedica S.P.A. Prosthesis of polymeric material coated with biocompatible carbon
US5387247A (en) * 1983-10-25 1995-02-07 Sorin Biomedia S.P.A. Prosthetic device having a biocompatible carbon film thereon and a method of and apparatus for forming such device
US5443862A (en) * 1992-08-28 1995-08-22 Saint-Gobain Vitrage International Process for the treatment of thin films having properties of electrical conduction and/or reflection in the infrared
EP0678483A2 (en) 1991-04-30 1995-10-25 Saint-Gobain Vitrage Glass substrate with a thin multilayer coating for solar protection
US5911856A (en) * 1993-09-03 1999-06-15 Canon Kabushiki Kaisha Method for forming thin film
US5981075A (en) * 1995-02-13 1999-11-09 Canon Kabushiki Kaisha Optical articles and devices with a thin film containing krypton, xenon, or radon atoms
US20060011231A1 (en) * 2002-10-04 2006-01-19 Masashi Ueda Method for forming thin film and apparatus therefor
US20100314246A1 (en) * 2009-06-10 2010-12-16 Hon Hai Precision Industry Co., Ltd. Sputter-coating apparatus having heating unit

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Cited By (45)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4065600A (en) * 1970-05-20 1977-12-27 Triplex Safety Glass Company Limited Metal oxide films
US4094763A (en) * 1970-07-31 1978-06-13 Ppg Industries, Inc. Sputter coating of glass with an oxide of a metal having an atomic number between 48 and 51 and mixtures thereof
US4006070A (en) * 1971-02-05 1977-02-01 Triplex Safety Glass Company Limited Metal oxide films
US4132624A (en) * 1971-02-05 1979-01-02 Triplex Safety Glass Company Limited Apparatus for producing metal oxide films
US4010291A (en) * 1974-12-16 1977-03-01 Agency Of Industrial Science & Technology Method of making a low resistance indium oxide conductive film
FR2352393A1 (en) * 1976-05-19 1977-12-16 Battelle Memorial Institute PROCESS FOR CARRYING OUT A DEPOSIT IN A LUMINESCENT DISCHARGE ON AT LEAST ONE SUBSTRATE, AND IONIC PICKLING OF THIS SUBSTRATE AND DEVICE FOR IMPLEMENTING THIS PROCESS
US4124474A (en) * 1976-11-15 1978-11-07 Commissariat A L'energie Atomique Method and apparatus for controlling the deposition of films by reactive sputtering
US4125446A (en) * 1977-08-15 1978-11-14 Airco, Inc. Controlled reflectance of sputtered aluminum layers
US4113599A (en) * 1977-09-26 1978-09-12 Ppg Industries, Inc. Sputtering technique for the deposition of indium oxide
WO1980000713A1 (en) * 1978-09-27 1980-04-17 Massachusetts Inst Technology Transparent heat mirrors formed on polymeric substrates
JPS6314323B2 (en) * 1978-09-27 1988-03-30 Masachuusetsutsu Inst Obu Tekunorojii
US4274936A (en) * 1979-04-30 1981-06-23 Advanced Coating Technology, Inc. Vacuum deposition system and method
US4248687A (en) * 1979-07-23 1981-02-03 Massachusetts Institute Of Technology Method of forming transparent heat mirrors on polymeric substrates
US4379040A (en) * 1981-01-29 1983-04-05 Ppg Industries, Inc. Method of and apparatus for control of reactive sputtering deposition
US4336119A (en) * 1981-01-29 1982-06-22 Ppg Industries, Inc. Method of and apparatus for control of reactive sputtering deposition
US4602239A (en) * 1982-01-08 1986-07-22 Ppg Industries, Inc. Spring tensioned wire resistance heater
US4650557A (en) * 1982-11-03 1987-03-17 Donnelly Corporation Process for making a conductively coated glass member and the product thereof
US4647548A (en) * 1983-01-10 1987-03-03 Merck Patent Gesellschaft Mit Beschrankter Haftung Targets for cathode sputtering
US4534841A (en) * 1983-03-31 1985-08-13 Leybold-Heraeus Gmbh Solar controlled glazing and method of producing glazing
US5387247A (en) * 1983-10-25 1995-02-07 Sorin Biomedia S.P.A. Prosthetic device having a biocompatible carbon film thereon and a method of and apparatus for forming such device
US4512864A (en) * 1983-11-30 1985-04-23 Ppg Industries, Inc. Low resistance indium oxide films
US4466875A (en) * 1983-11-30 1984-08-21 Ppg Industries, Inc. Auxiliary heater for magnetron sputtering
US4797317A (en) * 1984-09-27 1989-01-10 Gila River Products, Inc. Solar control window film
US4634637A (en) * 1985-11-22 1987-01-06 Gila River Products, Inc. Solar control film
EP0224080A3 (en) * 1985-11-26 1989-06-28 Sorin Biomedica S.P.A. Improvements in and relating to the manufacture of prosthetic devices
US5084151A (en) * 1985-11-26 1992-01-28 Sorin Biomedica S.P.A. Method and apparatus for forming prosthetic device having a biocompatible carbon film thereon
US4655811A (en) * 1985-12-23 1987-04-07 Donnelly Corporation Conductive coating treatment of glass sheet bending process
US5370684A (en) * 1986-12-12 1994-12-06 Sorin Biomedica S.P.A. Prosthesis of polymeric material coated with biocompatible carbon
US4882028A (en) * 1988-01-22 1989-11-21 Micron Technology, Inc. R-F electrodes for removably providing electrical energy to an apparatus during R-F energy reactive treatment processes
US4962049A (en) * 1989-04-13 1990-10-09 Applied Materials, Inc. Process for the plasma treatment of the backside of a semiconductor wafer
US4988424A (en) * 1989-06-07 1991-01-29 Ppg Industries, Inc. Mask and method for making gradient sputtered coatings
US5075256A (en) * 1989-08-25 1991-12-24 Applied Materials, Inc. Process for removing deposits from backside and end edge of semiconductor wafer while preventing removal of materials from front surface of wafer
US5213650A (en) * 1989-08-25 1993-05-25 Applied Materials, Inc. Apparatus for removing deposits from backside and end edge of semiconductor wafer while preventing removal of materials from front surface of wafer
EP0678483A2 (en) 1991-04-30 1995-10-25 Saint-Gobain Vitrage Glass substrate with a thin multilayer coating for solar protection
US5244559A (en) * 1991-07-31 1993-09-14 Leybold Aktiengesellschaft Apparatus for transport and heat treatment of substrates
US5207885A (en) * 1991-09-19 1993-05-04 Leybold Aktiengesellschaft Target for reactive sputtering
DE4131181C1 (en) * 1991-09-19 1993-01-07 Leybold Ag, 6450 Hanau, De
US5443862A (en) * 1992-08-28 1995-08-22 Saint-Gobain Vitrage International Process for the treatment of thin films having properties of electrical conduction and/or reflection in the infrared
US5911856A (en) * 1993-09-03 1999-06-15 Canon Kabushiki Kaisha Method for forming thin film
US5981075A (en) * 1995-02-13 1999-11-09 Canon Kabushiki Kaisha Optical articles and devices with a thin film containing krypton, xenon, or radon atoms
US6372646B2 (en) 1995-02-13 2002-04-16 Canon Kabushiki Kaisha Optical article, exposure apparatus or optical system using it, and process for producing it
US6726814B2 (en) 1995-02-13 2004-04-27 Canon Kk Process for producing optical article
US20060011231A1 (en) * 2002-10-04 2006-01-19 Masashi Ueda Method for forming thin film and apparatus therefor
US8034418B2 (en) * 2002-10-04 2011-10-11 Ishikawajima-Harima Heavy Industries Co., Ltd. Method for forming thin film and apparatus therefor
US20100314246A1 (en) * 2009-06-10 2010-12-16 Hon Hai Precision Industry Co., Ltd. Sputter-coating apparatus having heating unit

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