US2344138A - Coating method - Google Patents
Coating method Download PDFInfo
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- US2344138A US2344138A US374657A US37465741A US2344138A US 2344138 A US2344138 A US 2344138A US 374657 A US374657 A US 374657A US 37465741 A US37465741 A US 37465741A US 2344138 A US2344138 A US 2344138A
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- Prior art keywords
- metal
- strip
- gaseous
- carbonyl
- chamber
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- C—CHEMISTRY; METALLURGY
- C23—COATING 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
- C23C—COATING 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
- C23C16/00—Chemical coating by decomposition of gaseous compounds, without leaving reaction products of surface material in the coating, i.e. chemical vapour deposition [CVD] processes
- C23C16/44—Chemical 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
- C23C16/54—Apparatus specially adapted for continuous coating
- C23C16/545—Apparatus specially adapted for continuous coating for coating elongated substrates
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- C—CHEMISTRY; METALLURGY
- C23—COATING 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
- C23C—COATING 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
- C23C16/00—Chemical coating by decomposition of gaseous compounds, without leaving reaction products of surface material in the coating, i.e. chemical vapour deposition [CVD] processes
- C23C16/04—Coating on selected surface areas, e.g. using masks
- C23C16/042—Coating on selected surface areas, e.g. using masks using masks
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- C—CHEMISTRY; METALLURGY
- C23—COATING 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
- C23C—COATING 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
- C23C16/00—Chemical coating by decomposition of gaseous compounds, without leaving reaction products of surface material in the coating, i.e. chemical vapour deposition [CVD] processes
- C23C16/06—Chemical 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 deposition of metallic material
- C23C16/16—Chemical 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 deposition of metallic material from metal carbonyl compounds
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10T—TECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
- Y10T29/00—Metal working
- Y10T29/49—Method of mechanical manufacture
- Y10T29/4981—Utilizing transitory attached element or associated separate material
- Y10T29/49812—Temporary protective coating, impregnation, or cast layer
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 anv 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 con-v ducting the gaseous product resultant from the de-composition back to a source to regenerate the gaseous metal compound.
- Another object is to provide a simplified method and apparatus for depositing metal by the use of volatile metal compounds and thereafter bumng 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 oi.' the ⁇ arrow;
- Figure 3 is a fragmentary sectional view of a modification of the apparatus shown in Figure 1.
- My invention makes it possible to use the volatile carbonyls of nickel, iron, chromium and the like for depositing metal coatings on the surfaces oi articles. '.I'he method of preparing the metal carbonyls is well-known in the art and forms no part oi this invention.
- the principal step of, coatingmetal strip by my process comprisesy bringing about the separation of the metal from the volatile compound by its 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 adhesion 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 oi alkali or acid electrolyte, whereinthe strip is made the cathode or anode.
- Pickling of the metal strip with hydrochloric, sulphuric, or nitric acid, or a combination oi these acids may be also made as a part of the cleaning process and the strip thoroughly rinsed, or washed, prior to advancing the same through the gaseous carbonyl plating apparatus of this invention.
- a continuous metal strip IB is arranged to be drawn through a tank I2, which is illled with liquid I4, such as water or other liquid, which will form a liquid seal i'or the strip as it passes though 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 Jstrip I0 is moved.
- 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, is generated in a generator 24 and the gaseous metal carbonyl compound is circulated through the conduit 25 into the chamber 20 by means oi the suction fan 28.
- This fan is preferably arranged at one end within the chamber 20 and is partially surrounded by a heat insulating wall portion Il, as shown in Figure 1. It is arranged to move the gaseous metal carbonyl from the generator through the pipe 25 and discharge conduit 3! and into the confining chamber 34 arranged adjacent the surface of the strip I0.
- the products of decomposition pass out at the other end of the confining chamber 34. as at 3
- 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. 'I'he temperature of the metal strip. in the case of Ni(CO)4, for depositing nickel would be above 180 degrees centigrade, or that sufcient to bring amout a temperature in the auxiliary chamber 48 whereby the carbonyl compound is decomposed and the metal deposited onto the surface of the strip l forming a coherent coating thereon.
- an inwardly extended partitioning wall 49 is arranged in the chamber 2li, as shown in Figure 1.
- Guide wall 49 is preferably made of non-metal 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-l-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 CH4) This reaction forms gaseous Ni(CO) 4.
- Ni(CO)4 heated to 180 degrees centigrade causes deposition of pure nickel and liberation of CO whichis 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 4l 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.
- CO carbon monoxide
- the blower for moving the gaseous metal carbonyl compound from the generator into the restricd chamber 4l of the compartment 20 is omitted and suitable means, not shown, is provided in the generator 24 for moving the gas through the conduit 2l and into one end ot the chamber 4l which connes the carbonyl. gas adjacent the surface of the strip l0 as it is moved over the table 40.
- In this modication means is also provided for heating the metal strip as it passes over the table 40 by means of a fluid spray Il, which is directed on the underside of the strip, as shown in Figure 3.
- Suitable means, comprising-conduit means and spraying means ⁇ i1 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, budlng, or polishing the ⁇ same to provide the desired luster or brightness of the coating.
- a method of coating,long continuous lengths of metal stripping on only one side thereof comprising continuously moving and guiding the stripping through a liquid sealed chamber, circulating gaseous metal carbonyl over the upper surface only of said stripping and in a direction opposite to the movement of said stripping while protecting the underside of said stri-pping from contact with said gaseous metal carbonyl throughout its movement in said chamber, and heating said strip on its underside as it passes through said chamber to decompose said gaseous metal carbonyl and thereby precipitate and de- .posit the pure metal onto the upper surface only of said stripping as it is moved therealong.
- a method of coating long continuous lengths of metal stripping on only one side thereof comregeneration of the metal carbonyl and its decomposition is carried on continuously during the operation of the apparatus.
- the apparatus provides a hermetically sealed device for carrying out the method of this invention without the prising continuously moving and guiding the stripping through a liquid sealed chamber, circulating gaseous nickel carbonyl over the upper surface only of said stripping and in a direction opposite to the movement of said stripping while protecting the underside of said stripping from contact with said gaseous nickel carbonyl throughout its movement in said chamber, and heating said strip on its underside as it passes through said chamber to decompose said gaseous nickel carbonyl and thereby precipitate and deposit the pure nickel onto the upper surface only of said stripping as it is moved therealong.
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- Chemical & Material Sciences (AREA)
- General Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Engineering & Computer Science (AREA)
- Materials Engineering (AREA)
- Mechanical Engineering (AREA)
- Metallurgy (AREA)
- Organic Chemistry (AREA)
- Chemical Vapour Deposition (AREA)
Description
March 14, 1944. F E DRUMMOND 2,344,138
COATING METHOD Original Filed May 20, 1940 `Patented Mar. 14, v1944 2.344.138 comme mamon Folsom E. Drummond, Dayton, Ohio, alsignor, by mesne assignments, to Chemical Developments Corporation, Dayton,
Ohio
Ohio, a corporation of original application May zo, 194e, sel-iai No. 336,191. Divided and this application January 16, 1941, Serial No. 374,857,
2 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.
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 useof 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. l
yIt l's 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 anv 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 con-v ducting the gaseous product resultant from the de-composition back to a source to regenerate the gaseous metal compound.
Another object is to provide a simplified method and apparatus for depositing metal by the use of volatile metal compounds and thereafter bumng and polishing the coated article to provide a bright, smooth coating.
These 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 oi.' the` arrow;
Figure 3 is a fragmentary sectional view of a modification of the apparatus shown in Figure 1.
In general, it has been proposed heretofore to utilize non-volatile carbonyls of iron in the production of very finely divided pure iron, but the use of the volatile metal carbonyls, which are poisonous compounds, have not been employed in processing treatments.
My invention makes it possible to use the volatile carbonyls of nickel, iron, chromium and the like for depositing metal coatings on the surfaces oi articles. '.I'he method of preparing the metal carbonyls is well-known in the art and forms no part oi this invention.
The principal step of, coatingmetal strip by my process comprisesy bringing about the separation of the metal from the volatile compound by its 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 adhesion 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 oi alkali or acid electrolyte, whereinthe strip is made the cathode or anode. Pickling of the metal strip with hydrochloric, sulphuric, or nitric acid, or a combination oi these acids, may be also made as a part of the cleaning process and the strip thoroughly rinsed, or washed, prior to advancing the same through the gaseous carbonyl plating apparatus of this invention.
'I'his application is a division of my copending application, Serial No. 336,191, led May 20.
Y1040, now Patent No. 2,332,309, granted October Referring to the drawing in detail wherein there is illustrated an apparatus for carrying out the process of this invention, a continuous metal strip IB is arranged to be drawn through a tank I2, which is illled with liquid I4, such as water or other liquid, which will form a liquid seal i'or the strip as it passes though 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 Jstrip 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 2| 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 1 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 oi the suction fan 28. This fan is preferably arranged at one end within the chamber 20 and is partially surrounded by a heat insulating wall portion Il, as shown in Figure 1. It is arranged to move the gaseous metal carbonyl from the generator through the pipe 25 and discharge conduit 3! and into the confining chamber 34 arranged adjacent the surface of the strip I0. 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 3|, and are discharged through the conduit 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. 'I'he temperature of the metal strip. in the case of Ni(CO)4, for depositing nickel would be above 180 degrees centigrade, or that sufcient to bring amout a temperature in the auxiliary chamber 48 whereby the carbonyl compound is decomposed and the metal deposited onto the surface of the strip l 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 2li, as shown in Figure 1. Guide wall 49 is preferably made of non-metal 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-l-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 CH4) This reaction forms gaseous Ni(CO) 4. Ni(CO)4 heated to 180 degrees centigrade causes deposition of pure nickel and liberation of CO whichis 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 4l 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 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 compound from the generator into the restricd chamber 4l of the compartment 20 is omitted and suitable means, not shown, is provided in the generator 24 for moving the gas through the conduit 2l and into one end ot the chamber 4l which connes the carbonyl. gas adjacent the surface of the strip l0 as it is moved over the table 40. In this modication means is also provided for heating the metal strip as it passes over the table 40 by means of a fluid spray Il, which is directed on the underside of the strip, as shown in Figure 3. Suitable means, comprising-conduit means and spraying means` i1, 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 of the metal strip is completed, it will be understood that where it is desired, the coating may be further treated as by heating, burnishing, budlng, 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 dis-` closed herein are susceptible to various changes and modiiications without departing from the principle and spirit of this invention and such modifications as are required to adapt the invention to diierent 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. A method of coating,long continuous lengths of metal stripping on only one side thereof comprising continuously moving and guiding the stripping through a liquid sealed chamber, circulating gaseous metal carbonyl over the upper surface only of said stripping and in a direction opposite to the movement of said stripping while protecting the underside of said stri-pping from contact with said gaseous metal carbonyl throughout its movement in said chamber, and heating said strip on its underside as it passes through said chamber to decompose said gaseous metal carbonyl and thereby precipitate and de- .posit the pure metal onto the upper surface only of said stripping as it is moved therealong.
2. A method of coating long continuous lengths of metal stripping on only one side thereof comregeneration of the metal carbonyl and its decomposition is carried on continuously during the operation of the apparatus. The apparatus provides a hermetically sealed device for carrying out the method of this invention without the prising continuously moving and guiding the stripping through a liquid sealed chamber, circulating gaseous nickel carbonyl over the upper surface only of said stripping and in a direction opposite to the movement of said stripping while protecting the underside of said stripping from contact with said gaseous nickel carbonyl throughout its movement in said chamber, and heating said strip on its underside as it passes through said chamber to decompose said gaseous nickel carbonyl and thereby precipitate and deposit the pure nickel onto the upper surface only of said stripping as it is moved therealong.
FOLSOM E. DRUMMOND.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
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US374657A US2344138A (en) | 1940-05-20 | 1941-01-16 | Coating method |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
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US336191A US2332309A (en) | 1940-05-20 | 1940-05-20 | Gaseous metal deposition |
US374657A US2344138A (en) | 1940-05-20 | 1941-01-16 | Coating method |
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US2344138A true US2344138A (en) | 1944-03-14 |
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US374657A Expired - Lifetime US2344138A (en) | 1940-05-20 | 1941-01-16 | Coating method |
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Cited By (101)
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 |
US2508509A (en) * | 1945-01-13 | 1950-05-23 | Bell Telephone Labor Inc | Apparatus for coating hollow objects |
US2516058A (en) * | 1943-09-30 | 1950-07-18 | Bell Telephone Labor Inc | Apparatus for plating of metals |
US2523461A (en) * | 1946-03-15 | 1950-09-26 | John T Young | Plating with metal carbonyl |
US2576289A (en) * | 1949-12-02 | 1951-11-27 | Ohio Commw Eng Co | Dynamic pyrolytic plating process |
US2587036A (en) * | 1946-03-12 | 1952-02-26 | Bell Telephone Labor Inc | Process and apparatus for semicontinuous plating |
US2602033A (en) * | 1950-01-18 | 1952-07-01 | Bell Telephone Labor Inc | Carbonyl process |
US2604395A (en) * | 1945-11-19 | 1952-07-22 | Fansteel Metallurgical Corp | Method of producing metallic bodies |
US2622041A (en) * | 1948-08-03 | 1952-12-16 | Nat Res Corp | Deposition of metal on a nonmetallic support |
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 |
US2656283A (en) * | 1949-08-31 | 1953-10-20 | Ohio Commw Eng Co | Method of plating wire |
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 |
US2665228A (en) * | 1950-07-19 | 1954-01-05 | Nat Res Corp | Apparatus and process for vapor coating |
US2685121A (en) * | 1949-05-07 | 1954-08-03 | Ohio Commw Eng Co | Method and apparatus for manufacture of metal films |
US2685124A (en) * | 1951-04-30 | 1954-08-03 | Ohio Commw Eng Co | Method for hi-vac alloying and coated product |
US2685532A (en) * | 1951-10-08 | 1954-08-03 | Ohio Commw Eng Co | Gas plating with chromium hexacarbonyl |
US2690980A (en) * | 1951-03-14 | 1954-10-05 | Bell Telephone Labor Inc | Carbonyl process |
US2694651A (en) * | 1951-10-08 | 1954-11-16 | Ohio Commw Eng Co | Deposition of copper oxides on heat insulating material |
US2700365A (en) * | 1951-10-08 | 1955-01-25 | Ohio Commw Eng Co | Apparatus for plating surfaces with carbonyls and other volatile metal bearing compounds |
US2701901A (en) * | 1952-04-03 | 1955-02-15 | Ohio Commw Eng Co | Method of manufacturing thin nickel foils |
US2704728A (en) * | 1951-10-08 | 1955-03-22 | Ohio Commw Eng Co | Gas plating metal objects with copper acetylacetonate |
US2704727A (en) * | 1951-10-08 | 1955-03-22 | Ohio Commw Eng Co | Method of deposition of non-conductive copper coatings from vapor phase |
US2719094A (en) * | 1951-06-16 | 1955-09-27 | Nat Res Corp | Coating device and method |
US2719095A (en) * | 1951-06-13 | 1955-09-27 | American Electro Metal Corp | Production of corrosion-resistant coatings on copper infiltrated ferrous skeleton bodies |
US2738762A (en) * | 1951-10-08 | 1956-03-20 | Ohio Commw Eng Co | Apparatus for the deposition of nonconductive copper coatings from vapor phase |
US2742691A (en) * | 1950-04-18 | 1956-04-24 | Ohio Commw Eng Co | Method of making corrosion resistant clad steel |
US2749255A (en) * | 1952-05-24 | 1956-06-05 | Ohio Commw Eng Co | Method of producing metalized glass fiber rovings |
US2753800A (en) * | 1952-03-24 | 1956-07-10 | Ohio Commw Eng Co | Production of printing plates |
US2763576A (en) * | 1949-05-23 | 1956-09-18 | Ohio Commw Eng Co | Method for gas plating |
US2768098A (en) * | 1950-09-12 | 1956-10-23 | Siemens Ag | Method and apparatus for precipitating metal from the vaporous state onto plates, particularly for the production of selenium coated rectifier plates |
US2780553A (en) * | 1955-07-07 | 1957-02-05 | Ohio Commw Eng Co | Process of providing a controlled atmosphere containing a heat decomposable metal compound |
US2789922A (en) * | 1952-05-24 | 1957-04-23 | Stewart Warner Corp | Method and apparatus for applying a thin film of liquid |
US2790731A (en) * | 1953-12-14 | 1957-04-30 | Ohio Commw Eng Co | Method and apparatus for the production of electrically resistant films |
US2812272A (en) * | 1954-08-02 | 1957-11-05 | Ohio Commw Eng Co | Apparatus and method for the production of metallized materials |
US2817141A (en) * | 1953-04-14 | 1957-12-24 | Ohio Commw Eng Co | Composite metal structure |
US2818351A (en) * | 1952-12-09 | 1957-12-31 | Ohio Commw Eng Co | Process of plating glass fiber rovings with iron metal |
US2856312A (en) * | 1953-07-03 | 1958-10-14 | Nowak Rudolf | Treating metal surfaces |
US2859130A (en) * | 1954-06-16 | 1958-11-04 | Ohio Commw Eng Co | Method for gas plating synthetic fibers |
US2872342A (en) * | 1952-12-09 | 1959-02-03 | Ohio Commw Eng Co | Catalytic nickel plating |
US2883553A (en) * | 1955-10-21 | 1959-04-21 | John H Birden | Fabrication of neutron sources |
US2907626A (en) * | 1958-01-15 | 1959-10-06 | Bjorksten Res Lab Inc | Metal coating of glass fibers at high speeds |
US2956909A (en) * | 1956-06-11 | 1960-10-18 | Sprague Electric Co | Process for producing a conductive layer on heat sensitive dielectric material |
US3055087A (en) * | 1954-06-07 | 1962-09-25 | Union Carbide Corp | Carbonyl metal plated product |
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US20070032082A1 (en) * | 2005-08-08 | 2007-02-08 | Applied Materials, Inc. | Semiconductor substrate process using an optically writable carbon-containing mask |
US20070032095A1 (en) * | 2005-08-08 | 2007-02-08 | Applied Materials, Inc. | Copper conductor annealing process employing high speed optical annealing with a low temperature-deposited optical absorber layer |
US20070032004A1 (en) * | 2005-08-08 | 2007-02-08 | Applied Materials, Inc. | Copper barrier reflow process employing high speed optical annealing |
US20070032054A1 (en) * | 2005-08-08 | 2007-02-08 | Applied Materials, Inc. | Semiconductor substrate process using a low temperature deposited carbon-containing hard mask |
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