US2332309A - Gaseous metal deposition - Google Patents

Gaseous metal deposition Download PDF

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US2332309A
US2332309A US336191A US33619140A US2332309A US 2332309 A US2332309 A US 2332309A US 336191 A US336191 A US 336191A US 33619140 A US33619140 A US 33619140A US 2332309 A US2332309 A US 2332309A
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metal
strip
gaseous
generator
carbonyl
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US336191A
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Folsom E Drummond
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Commonwealth Engineering Company of Ohio
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Commonwealth Engineering Company of Ohio
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Priority to US374657A priority patent/US2344138A/en
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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
    • C23C16/00Chemical coating by decomposition of gaseous compounds, without leaving reaction products of surface material in the coating, i.e. chemical vapour deposition [CVD] processes
    • C23C16/44Chemical coating by decomposition of gaseous compounds, without leaving reaction products of surface material in the coating, i.e. chemical vapour deposition [CVD] processes characterised by the method of coating
    • C23C16/54Apparatus specially adapted for continuous coating
    • C23C16/545Apparatus specially adapted for continuous coating for coating elongated substrates

Definitions

  • This invention relates to the deposition of metals, and more particularly comprises a, method and apparatus for plating metal strip by utilizing gaseous metal carbonyl substances.
  • Another object is to provide an apparatus and method of applying a coating of metal to a surface without the use of electroplating solutions and wherein continuous deposition of the metal is eiected from a gaseous medium.
  • Another object is to provide an apparatus and method of utilizing gaseous metal compounds for plating articles wherein the metal is deposited from a volatile metal compound by continuously decomposing the compound and conducting the gaseous product resultant from the decomposition back to a source to regenerate the gaseous metal compound.
  • Another object is to provide a simplied method and apparatus for depositing metal by the use of volatile metal compounds and thereafter buiiing and polishing the coated article to provide a bright, smooth coating.
  • Figure 1 illustrates one embodiment of my invention showing diagrammatically an apparatus, partly in section, for treating continuous metal strips, or ribbons, with a gaseous metal carbonyl compound;
  • Figure 2 is a vertical sectional view taken substantially on the line 2--2 of Figure 1 and looking in the direction of the arrow;
  • Figure 3 is a. fragmentary sectional View of a modication of the apparatus shown in Figure 1.
  • the cleaning of the metal strip, or ribbon, prior to the plating may be effected by employing the conventional methods used in the art comprising electrochemically cleaning the strip by moving the same through a bath of alkali or acid electrolyte, wherein the strip is made the cathode or Pickling of the metal strip with hydrochloric, sulphuric, or nitric acid, or a combination of these acids, may be also made as a part of the cleaning process and the strip thoroughly rinsed, or Washed, prior t0 advancing the same through the gaseous carbonyl plating apparatus of this invention.
  • a continuous metal strip I0 is arranged to be drawn through a tank I2, which is iilled with liquid I4, such as water or other liquid, which will form a liquid seal for the strip as it passes through the tank.
  • liquid I4 such as water or other liquid
  • a chamber I6 which comprises an inverted closed container having the depending side wall portions I8 which are immersed in the liquid I4 so as to provide a liquid seal chamber 20 through which the strip I0 is moved.
  • Suitable guide rolls 2l are positioned on the ends of the tank I2 over which the strip is moved and similar immersed guide roll members 23 are suitably mounted in the end walls I8 forming the gaseous chamber for conducting this strip into the chamber 20.
  • the gaseous metal carbonyl compound M(CO)4 wherein the M may be nickel (Ni), for example,
  • the gaseous metal carbonyl compound is circulated through the conduit 25 into the chamber 20 by means of the suction fan 2l.
  • This fan is preferably arranged at one end within the chamber 2l and is partially surrounded by a heat insulating wail portion 30, as shown in Figure 1. It is arranged to move the gaseous metal carbonyl from the generator through the pipe 25 and discharge conduit 32 and into the conning chamber I4 arranged adjacent the surface of the strip lo. After the gaseous metal compound is moved over the surface of the metal and decomposed under the action of heat, the products of decomposition pass out at the other end of the confining chamber 34, as at 36,' and are discharged through the conduit 38 and returned to the generator 24, as shown in Figure 1.
  • the strip In order to present the largest amount of the metal strip surface which is to be coated to the volatile metal carbonyl gas, the strip is moved over a table means 40, which is provided with rollers 42,over which the strip is passed along.
  • a heating element 45 is arranged beneath the table surface so as to heat the metal strip to the temperature at which the metal carbonyl gas will be decomposed.
  • the temperature of the metal strip in the case of Ni(CO) 4, for depositing nickel would be above 180 degrees centigrade, or that sufficient to bring about a temperature in f the auxiliary chamber 48 whereby the carbonyl compound is decomposed and the metal deposited onto the surface of the strip I forming a coherent coating thereon.
  • an inwardly extended partitioning wall 49 is arranged in the chamber 20, as shown in Figure 1.
  • Guide wall 49 is preferably made of nonmetal heat insulating material to inhibit the deposition of metal thereon. All exposed parts preferably are covered with heat insulating coatings or fabrication so as to resist deposition of metal thereon. Glass, ceramic, or synthetic resinous products may be used for the purpose.
  • NiOz which is reduced with water gas (CO-i-Hz).
  • This mixture of nickel oxide and water gas is heated to 45 degrees to 90 degrees centigrade in a current of producer gas (CO, H2 and CH 4) This reaction forms gaseous Ni(CO) 4.
  • Ni(CO)4 heated to 180 degrees centigrade causes deposition of pure nickel and liberation of CO which is returned to the generator and used again to form more Ni(CO)4.
  • a. resilient pad 50 is provided which extends over the table 40 and having its ends immersed in the liquid of the tank, as illustrated in Figure 1.
  • the temperature in the zone 48 is controlled by suitable means so as to bring about the decomposition of the metal carbonyl and the carbon monoxide (CO) which is freed during the process is returned to the generator and used again to generate more of the metal carbonyl compound.
  • the apparatus provides a fluid-sealed apparatus for continuously treating metal strips of long lengths which are moved therethrough and whereby the regenration of the metal carbonyl and its decomposition is carried on continuously during the operation of the apparatus.
  • the apparatus provides a hermetically sealed device fcr'carrying out the method of this invention without the danger of poisonous gas coming in contact with the operator.
  • the blower for moving the gaseous metal carbonyl compounds from the generator into the restricted chamber 4B of the compartment 2li is omitted and suitable means, not shown. is provided in the generator 24 for moving the gas through the conduit 25 and into one end of the chamber 4l which confines the carbonyl gas adjacent the surface of the strip i0 as it is moved over the table 40.
  • suitable means is also provided for heating the metal strip as it passes over the table 40 by means of a fluid spray 52, which is directed yon the underside of the strip, as shown in Figure 3.
  • Suitable means, comprising conduit means 55 and spraying means 51, is provided for conducting the heated fluid into the chamber 20 beneath the table 40 over which the strip passes. Heated water, or steam may be employed for this purpose, or other suitable heat exchange means may be utilized which will not hinder the decomposition and deposition of the metal onto the surface of the strip.
  • the coating may be further treated as by heating, burnishing, bufiing, or polishing the same to provide the desired luster or brightness of the coating.
  • An apparatus for treating continuous metal lengths in the form of bands, ribbons, or the like comprising means for conveying said continuous metal lengths through a compartment, means for fluid-sealing said compartment, means comprising a generator for forming a volatile metal compound, and force circulating means and duct means connected with said generator for circulating said volatile metal compound through said compartment and in contact with said metal lengths as the same are moved therethrough, said generator, ducts and force circulating means forming a closed system whereby the volatile compound is circulated in contact with said metal lengths and decomposed and the gaseous decomposition product conducted back to said generator.
  • An apparatus for platingcontinuous metal strips comprising a generator for forming a volatile metal compound, a compartment for receiving volatile metal compound, means for moving said strip through said compartment, means for hermetically sealing said. compartment, means for circulating the volatile metal compound from said generator into said compartment and in contact with said metal strip material, means for decomposing said volatile metal compound to deposit said metal onto the surface of the strip material, and means for conducting the gaseous decomposition products away from said compartment and back to the generator.

Description

- F. E.. DRuMMoND 2,332,309
GASEOUS METAL DEPOS ITION Filed May 20, 1940 liz mail" OR HQT FoLsom EDRuMMoND, @ym e g) 2 Patented Oct. 19, 1943 GASEQUS METAL DEPOSITION Folsom E. Drummond, Dayton, Ohio, assignor, by mesne assignments, to The Commonwealth Engineering Company oi' Ohio, Dayton, Ohio, a corporation of Ohio Application May 20, 1940, Serial No. 336,191
3 Claims.
This invention relates to the deposition of metals, and more particularly comprises a, method and apparatus for plating metal strip by utilizing gaseous metal carbonyl substances. v
Heretofore it has been the common practice to deposit metal coatings by the use of electroplating solutions. Further, the plating of steel strip and the like has been effected by thermo-mechanical methods involving the use of relatively high temperatures and complicated, expensive equipment. My invention provides a simple and inexpensive method of plating metal strip, or ribbons. The strip or ribbon of metal is adapted to be moved continuously through the apparatus and receive a coating of the metal desired to be deposited on the surface. Thereafter the coating may be burnished, or otherwise treated, as desired, to produce a surface having the luster required.
It is the principal object of this invention to devise a. method and apparatus for utilizing the volatile metal carbonyl compounds for metal coating articles in sheet or strip form.
Another object is to provide an apparatus and method of applying a coating of metal to a surface without the use of electroplating solutions and wherein continuous deposition of the metal is eiected from a gaseous medium.
Another object is to provide an apparatus and method of utilizing gaseous metal compounds for plating articles wherein the metal is deposited from a volatile metal compound by continuously decomposing the compound and conducting the gaseous product resultant from the decomposition back to a source to regenerate the gaseous metal compound.
Another object is to provide a simplied method and apparatus for depositing metal by the use of volatile metal compounds and thereafter buiiing and polishing the coated article to provide a bright, smooth coating.
'Ihese and other objects and advantages will be apparent from the following description taken in connection with the drawing, wherein,
Figure 1 illustrates one embodiment of my invention showing diagrammatically an apparatus, partly in section, for treating continuous metal strips, or ribbons, with a gaseous metal carbonyl compound;
Figure 2 is a vertical sectional view taken substantially on the line 2--2 of Figure 1 and looking in the direction of the arrow;
Figure 3 is a. fragmentary sectional View of a modication of the apparatus shown in Figure 1.
In general, it has been proposed heretofore to utilize non-volatile carbonyls of iron in the proof the metal from the volatile compound by its f anode.
decomposition in the presence of the metal strip or article to be coated, which strip has been previously thoroughly chemically cleaned, so as to provide for ready cohesion of the metal particles onto the metal surface.
The cleaning of the metal strip, or ribbon, prior to the plating may be effected by employing the conventional methods used in the art comprising electrochemically cleaning the strip by moving the same through a bath of alkali or acid electrolyte, wherein the strip is made the cathode or Pickling of the metal strip with hydrochloric, sulphuric, or nitric acid, or a combination of these acids, may be also made as a part of the cleaning process and the strip thoroughly rinsed, or Washed, prior t0 advancing the same through the gaseous carbonyl plating apparatus of this invention.
Referring to the drawing in detail wherein there is illustrated an apparatus for carrying out the process of this invention, a continuous metal strip I0 is arranged to be drawn through a tank I2, which is iilled with liquid I4, such as water or other liquid, which will form a liquid seal for the strip as it passes through the tank. In the tank I2 there is provided a chamber I6 which comprises an inverted closed container having the depending side wall portions I8 which are immersed in the liquid I4 so as to provide a liquid seal chamber 20 through which the strip I0 is moved. This arrangement prevents the escape of the poisonous metal carbonyl gas into the surrounding atmosphere during the operation of the device. Suitable guide rolls 2l are positioned on the ends of the tank I2 over which the strip is moved and similar immersed guide roll members 23 are suitably mounted in the end walls I8 forming the gaseous chamber for conducting this strip into the chamber 20.
In the apparatus shown in Figures l and 2, the gaseous metal carbonyl compound M(CO)4, wherein the M may be nickel (Ni), for example,
is generated in a generator 24 and the gaseous metal carbonyl compound is circulated through the conduit 25 into the chamber 20 by means of the suction fan 2l. This fan is preferably arranged at one end within the chamber 2l and is partially surrounded by a heat insulating wail portion 30, as shown in Figure 1. It is arranged to move the gaseous metal carbonyl from the generator through the pipe 25 and discharge conduit 32 and into the conning chamber I4 arranged adjacent the surface of the strip lo. After the gaseous metal compound is moved over the surface of the metal and decomposed under the action of heat, the products of decomposition pass out at the other end of the confining chamber 34, as at 36,' and are discharged through the conduit 38 and returned to the generator 24, as shown in Figure 1.
In order to present the largest amount of the metal strip surface which is to be coated to the volatile metal carbonyl gas, the strip is moved over a table means 40, which is provided with rollers 42,over which the strip is passed along. A heating element 45 is arranged beneath the table surface so as to heat the metal strip to the temperature at which the metal carbonyl gas will be decomposed. The temperature of the metal strip, in the case of Ni(CO) 4, for depositing nickel would be above 180 degrees centigrade, or that sufficient to bring about a temperature in f the auxiliary chamber 48 whereby the carbonyl compound is decomposed and the metal deposited onto the surface of the strip I forming a coherent coating thereon.
For guiding the metal carbonyl gas in a thin layer over the surface of the metal strip l0 an inwardly extended partitioning wall 49 is arranged in the chamber 20, as shown in Figure 1. Guide wall 49 is preferably made of nonmetal heat insulating material to inhibit the deposition of metal thereon. All exposed parts preferably are covered with heat insulating coatings or fabrication so as to resist deposition of metal thereon. Glass, ceramic, or synthetic resinous products may be used for the purpose.
In using nickel carbonyl, the regeneration of the carbonyl may be brought about with the use of NiOz which is reduced with water gas (CO-i-Hz). This mixture of nickel oxide and water gas is heated to 45 degrees to 90 degrees centigrade in a current of producer gas (CO, H2 and CH 4) This reaction forms gaseous Ni(CO) 4. Ni(CO)4 heated to 180 degrees centigrade causes deposition of pure nickel and liberation of CO which is returned to the generator and used again to form more Ni(CO)4.
In order to prevent the coating of the metal onto the underside of the strip, when this is not desired, a. resilient pad 50 is provided which extends over the table 40 and having its ends immersed in the liquid of the tank, as illustrated in Figure 1.
As explained, the temperature in the zone 48 is controlled by suitable means so as to bring about the decomposition of the metal carbonyl and the carbon monoxide (CO) which is freed during the process is returned to the generator and used again to generate more of the metal carbonyl compound. It will be observed that the apparatus provides a fluid-sealed apparatus for continuously treating metal strips of long lengths which are moved therethrough and whereby the regenration of the metal carbonyl and its decomposition is carried on continuously during the operation of the apparatus.
The apparatus provides a hermetically sealed device fcr'carrying out the method of this invention without the danger of poisonous gas coming in contact with the operator.
In the modification shown in Figure 3, the blower for moving the gaseous metal carbonyl compounds from the generator into the restricted chamber 4B of the compartment 2li is omitted and suitable means, not shown. is provided in the generator 24 for moving the gas through the conduit 25 and into one end of the chamber 4l which confines the carbonyl gas adjacent the surface of the strip i0 as it is moved over the table 40. In this modification means is also provided for heating the metal strip as it passes over the table 40 by means of a fluid spray 52, which is directed yon the underside of the strip, as shown in Figure 3. Suitable means, comprising conduit means 55 and spraying means 51, is provided for conducting the heated fluid into the chamber 20 beneath the table 40 over which the strip passes. Heated water, or steam may be employed for this purpose, or other suitable heat exchange means may be utilized which will not hinder the decomposition and deposition of the metal onto the surface of the strip.
After the coating ofthe metal strip is completed, it will be understood that where it is desired, the coating may be further treated as by heating, burnishing, bufiing, or polishing the same to provide the desired luster or brightness of the coating.
It will be understood from the foregoing description that the method and apparatus disclosed herein are susceptible to various changes and modifications without departing from the principle and spirit of this invention and such modifications as are required to adapt the invention to different conditions and uses are contemplated as within the scope of this invention.
Having thus fully described my invention, what I claim as new and desire to secure by Letters Patent is:
1. An apparatus for treating continuous metal lengths in the form of bands, ribbons, or the like, comprising means for conveying said continuous metal lengths through a compartment, means for fluid-sealing said compartment, means comprising a generator for forming a volatile metal compound, and force circulating means and duct means connected with said generator for circulating said volatile metal compound through said compartment and in contact with said metal lengths as the same are moved therethrough, said generator, ducts and force circulating means forming a closed system whereby the volatile compound is circulated in contact with said metal lengths and decomposed and the gaseous decomposition product conducted back to said generator.
2. An apparatus for platingcontinuous metal strips comprising a generator for forming a volatile metal compound, a compartment for receiving volatile metal compound, means for moving said strip through said compartment, means for hermetically sealing said. compartment, means for circulating the volatile metal compound from said generator into said compartment and in contact with said metal strip material, means for decomposing said volatile metal compound to deposit said metal onto the surface of the strip material, and means for conducting the gaseous decomposition products away from said compartment and back to the generator.
:,asasoo 3 said volatile metal substance, means for heating said metal lengths to bring about decomposition of said volatile metal substance to eect the deposition of metal onto said metal lengths, and means comprising a blower for circulating said volatile metal substance through said compartment and in contact with said metal lengths and back to the generator.
FOLSOM E. DRUMMON'D.
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Cited By (49)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2456241A (en) * 1946-11-22 1948-12-14 Farrand Optical Co Inc Method of making optical transmission filters by thermal evaporation
US2475601A (en) * 1946-04-26 1949-07-12 Ohio Commw Eng Co Bonding of metal carbonyl deposits
US2516058A (en) * 1943-09-30 1950-07-18 Bell Telephone Labor Inc Apparatus for plating of metals
US2576289A (en) * 1949-12-02 1951-11-27 Ohio Commw Eng Co Dynamic pyrolytic plating process
US2580976A (en) * 1949-09-07 1952-01-01 Ohio Commw Eng Co Apparatus for plating metal strips
US2599978A (en) * 1949-04-15 1952-06-10 Ohio Commw Eng Co Process of plating carrier particles with a catalytic metal
US2631948A (en) * 1949-05-23 1953-03-17 Ohio Commw Eng Co Method and apparatus for gas plating
US2638423A (en) * 1949-08-25 1953-05-12 Ohio Commw Eng Co Method and apparatus for continuously plating irregularly shaped objects
US2639490A (en) * 1948-08-12 1953-05-26 Joseph B Brennan Formation of metal strip under controlled pressures
US2650564A (en) * 1949-12-02 1953-09-01 Ohio Commw Eng Co Dynamic pyrolytic plating apparatus
US2653879A (en) * 1949-04-06 1953-09-29 Ohio Commw Eng Co Bonding of metal carbonyl deposits
US2656284A (en) * 1949-09-07 1953-10-20 Ohio Commw Eng Co Method of plating rolled sheet metal
US2657457A (en) * 1949-09-10 1953-11-03 Ohio Commw Eng Co Continuous metal production and continuous gas plating
US2671034A (en) * 1950-12-16 1954-03-02 Julian S Steinfeld Method for producing magnetic recording tape
US2682702A (en) * 1949-04-06 1954-07-06 Ohio Commw Eng Co Carbonyl metal plated product
US2685535A (en) * 1951-02-01 1954-08-03 Ohio Commw Eng Co Method and apparatus for deposition of materials by thermal decomposition
US2694651A (en) * 1951-10-08 1954-11-16 Ohio Commw Eng Co Deposition of copper oxides on heat insulating material
US2694377A (en) * 1951-10-08 1954-11-16 Ohio Commw Eng Co System of gas plating
US2700365A (en) * 1951-10-08 1955-01-25 Ohio Commw Eng Co Apparatus for plating surfaces with carbonyls and other volatile metal bearing compounds
US2704727A (en) * 1951-10-08 1955-03-22 Ohio Commw Eng Co Method of deposition of non-conductive copper coatings from vapor phase
US2728321A (en) * 1949-07-14 1955-12-27 Ohio Commw Eng Co Apparatus for gas plating
US2741216A (en) * 1949-09-10 1956-04-10 Ohio Commw Eng Co Apparatus for continuous metal production and continuous gas plating
US2743700A (en) * 1949-09-10 1956-05-01 Ohio Commw Eng Co Continuous metal production and continuous gas plating
US2760261A (en) * 1952-04-17 1956-08-28 Ohio Commw Eng Co Method of bonding articles
US2780553A (en) * 1955-07-07 1957-02-05 Ohio Commw Eng Co Process of providing a controlled atmosphere containing a heat decomposable metal compound
US2785651A (en) * 1951-10-08 1957-03-19 Ohio Commw Eng Co Apparatus for gas plating continuous lengths of material
US2789064A (en) * 1953-03-02 1957-04-16 Schladitz Hermann Process and apparatus for the metallisation of continuously travelling organic and inorganic foils by thermal decomposition of metal compounds
US2847330A (en) * 1954-07-28 1958-08-12 Ohio Commw Eng Co Method and apparatus for gas plating printing circuits
US2853970A (en) * 1956-03-09 1958-09-30 Ohio Commw Eng Co Continuous gas plating apparatus under vacuum seal
US2872342A (en) * 1952-12-09 1959-02-03 Ohio Commw Eng Co Catalytic nickel plating
US3032816A (en) * 1957-11-07 1962-05-08 Polymer Corp Coating process and apparatus
US3198167A (en) * 1961-03-10 1965-08-03 Alloyd Corp Vapor deposition device
US3294059A (en) * 1963-04-15 1966-12-27 Charles R Barnes Deposition of nickel films on the interior surface of polytetrafluoroethylene tubing
US3409469A (en) * 1964-03-05 1968-11-05 United Aircraft Corp Vapor coating conductive filaments utilizing uniform temperature
US3595205A (en) * 1965-10-28 1971-07-27 Dow Chemical Co Coating apparatus
US3900540A (en) * 1970-06-04 1975-08-19 Pfizer Method for making a film of refractory material having bi-directional reinforcing properties
US4123244A (en) * 1976-04-13 1978-10-31 Bfg Glassgroup Process of forming a metal or metal compound coating on a face of a glass substrate and apparatus suitable for use in forming such coating
US4205979A (en) * 1978-10-10 1980-06-03 Hazen Research, Inc. Process for beneficiating oxide ores
US4229209A (en) * 1978-01-27 1980-10-21 Hazen Research, Inc. Process for beneficiating gold
US4239529A (en) * 1979-10-22 1980-12-16 Hazen Research, Inc. Process for beneficiating sulfide ores
US4257881A (en) * 1978-01-10 1981-03-24 Hazen Research, Inc. Process for beneficiating oxide ores
US4276081A (en) * 1978-10-10 1981-06-30 Hazen Research, Inc. Process for beneficiating ores
US4289529A (en) * 1978-10-10 1981-09-15 Hazen Research, Inc. Process for beneficiating sulfide ores
US4289528A (en) * 1978-07-03 1981-09-15 Hazen Research, Inc. Process for beneficiating sulfide ores
US4294193A (en) * 1977-04-04 1981-10-13 Gordon Roy G Apparatus for vapor coating a moving glass substrate
US4380211A (en) * 1980-09-17 1983-04-19 Matsushita Electric Industrial Co., Ltd. Vacuum evaporation system for deposition of thin films
US4469045A (en) * 1975-06-11 1984-09-04 Pilkington Brothers P.L.C. Coating glass
US4685030A (en) * 1985-04-29 1987-08-04 Energy Conversion Devices, Inc. Surface mounted circuits including hybrid circuits, having CVD interconnects, and method of preparing the circuits
US4759950A (en) * 1986-09-26 1988-07-26 Advance Technology Materials, Inc. Method for metallizing filaments

Cited By (49)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2516058A (en) * 1943-09-30 1950-07-18 Bell Telephone Labor Inc Apparatus for plating of metals
US2475601A (en) * 1946-04-26 1949-07-12 Ohio Commw Eng Co Bonding of metal carbonyl deposits
US2456241A (en) * 1946-11-22 1948-12-14 Farrand Optical Co Inc Method of making optical transmission filters by thermal evaporation
US2639490A (en) * 1948-08-12 1953-05-26 Joseph B Brennan Formation of metal strip under controlled pressures
US2653879A (en) * 1949-04-06 1953-09-29 Ohio Commw Eng Co Bonding of metal carbonyl deposits
US2682702A (en) * 1949-04-06 1954-07-06 Ohio Commw Eng Co Carbonyl metal plated product
US2599978A (en) * 1949-04-15 1952-06-10 Ohio Commw Eng Co Process of plating carrier particles with a catalytic metal
US2631948A (en) * 1949-05-23 1953-03-17 Ohio Commw Eng Co Method and apparatus for gas plating
US2728321A (en) * 1949-07-14 1955-12-27 Ohio Commw Eng Co Apparatus for gas plating
US2638423A (en) * 1949-08-25 1953-05-12 Ohio Commw Eng Co Method and apparatus for continuously plating irregularly shaped objects
US2580976A (en) * 1949-09-07 1952-01-01 Ohio Commw Eng Co Apparatus for plating metal strips
US2656284A (en) * 1949-09-07 1953-10-20 Ohio Commw Eng Co Method of plating rolled sheet metal
US2657457A (en) * 1949-09-10 1953-11-03 Ohio Commw Eng Co Continuous metal production and continuous gas plating
US2743700A (en) * 1949-09-10 1956-05-01 Ohio Commw Eng Co Continuous metal production and continuous gas plating
US2741216A (en) * 1949-09-10 1956-04-10 Ohio Commw Eng Co Apparatus for continuous metal production and continuous gas plating
US2576289A (en) * 1949-12-02 1951-11-27 Ohio Commw Eng Co Dynamic pyrolytic plating process
US2650564A (en) * 1949-12-02 1953-09-01 Ohio Commw Eng Co Dynamic pyrolytic plating apparatus
US2671034A (en) * 1950-12-16 1954-03-02 Julian S Steinfeld Method for producing magnetic recording tape
US2685535A (en) * 1951-02-01 1954-08-03 Ohio Commw Eng Co Method and apparatus for deposition of materials by thermal decomposition
US2700365A (en) * 1951-10-08 1955-01-25 Ohio Commw Eng Co Apparatus for plating surfaces with carbonyls and other volatile metal bearing compounds
US2704727A (en) * 1951-10-08 1955-03-22 Ohio Commw Eng Co Method of deposition of non-conductive copper coatings from vapor phase
US2694377A (en) * 1951-10-08 1954-11-16 Ohio Commw Eng Co System of gas plating
US2694651A (en) * 1951-10-08 1954-11-16 Ohio Commw Eng Co Deposition of copper oxides on heat insulating material
US2785651A (en) * 1951-10-08 1957-03-19 Ohio Commw Eng Co Apparatus for gas plating continuous lengths of material
US2760261A (en) * 1952-04-17 1956-08-28 Ohio Commw Eng Co Method of bonding articles
US2872342A (en) * 1952-12-09 1959-02-03 Ohio Commw Eng Co Catalytic nickel plating
US2789064A (en) * 1953-03-02 1957-04-16 Schladitz Hermann Process and apparatus for the metallisation of continuously travelling organic and inorganic foils by thermal decomposition of metal compounds
US2847330A (en) * 1954-07-28 1958-08-12 Ohio Commw Eng Co Method and apparatus for gas plating printing circuits
US2780553A (en) * 1955-07-07 1957-02-05 Ohio Commw Eng Co Process of providing a controlled atmosphere containing a heat decomposable metal compound
US2853970A (en) * 1956-03-09 1958-09-30 Ohio Commw Eng Co Continuous gas plating apparatus under vacuum seal
US3032816A (en) * 1957-11-07 1962-05-08 Polymer Corp Coating process and apparatus
US3198167A (en) * 1961-03-10 1965-08-03 Alloyd Corp Vapor deposition device
US3294059A (en) * 1963-04-15 1966-12-27 Charles R Barnes Deposition of nickel films on the interior surface of polytetrafluoroethylene tubing
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