US3055089A - Gaseous metal product and processes - Google Patents
Gaseous metal product and processes Download PDFInfo
- Publication number
- US3055089A US3055089A US753567A US75356758A US3055089A US 3055089 A US3055089 A US 3055089A US 753567 A US753567 A US 753567A US 75356758 A US75356758 A US 75356758A US 3055089 A US3055089 A US 3055089A
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- United States
- Prior art keywords
- metal
- gaseous
- chamber
- plating
- strip
- Prior art date
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- Expired - Lifetime
Links
- 229910052751 metal Inorganic materials 0.000 title claims description 165
- 239000002184 metal Substances 0.000 title claims description 165
- 238000000034 method Methods 0.000 title claims description 36
- 238000007747 plating Methods 0.000 claims description 59
- 239000010953 base metal Substances 0.000 claims description 33
- 239000007789 gas Substances 0.000 claims description 30
- 150000002736 metal compounds Chemical class 0.000 claims description 24
- 238000000354 decomposition reaction Methods 0.000 claims description 8
- 230000008021 deposition Effects 0.000 claims description 7
- 239000010941 cobalt Substances 0.000 claims description 5
- 229910017052 cobalt Inorganic materials 0.000 claims description 5
- GUTLYIVDDKVIGB-UHFFFAOYSA-N cobalt atom Chemical group [Co] GUTLYIVDDKVIGB-UHFFFAOYSA-N 0.000 claims description 4
- 238000009489 vacuum treatment Methods 0.000 claims description 4
- 238000010438 heat treatment Methods 0.000 description 40
- 238000000576 coating method Methods 0.000 description 23
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 20
- 239000011248 coating agent Substances 0.000 description 20
- 239000011148 porous material Substances 0.000 description 15
- 239000010410 layer Substances 0.000 description 13
- PXHVJJICTQNCMI-UHFFFAOYSA-N Nickel Chemical compound [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 description 11
- 229910002092 carbon dioxide Inorganic materials 0.000 description 11
- 239000001569 carbon dioxide Substances 0.000 description 11
- 238000004140 cleaning Methods 0.000 description 11
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 9
- 125000002915 carbonyl group Chemical group [*:2]C([*:1])=O 0.000 description 9
- 229910052802 copper Inorganic materials 0.000 description 9
- 239000010949 copper Substances 0.000 description 9
- 239000011261 inert gas Substances 0.000 description 9
- 239000000463 material Substances 0.000 description 9
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 8
- 229910000831 Steel Inorganic materials 0.000 description 8
- 229910052759 nickel Inorganic materials 0.000 description 8
- 239000010959 steel Substances 0.000 description 8
- 238000000151 deposition Methods 0.000 description 6
- 238000001465 metallisation Methods 0.000 description 6
- 238000011282 treatment Methods 0.000 description 6
- ZOKXTWBITQBERF-UHFFFAOYSA-N Molybdenum Chemical compound [Mo] ZOKXTWBITQBERF-UHFFFAOYSA-N 0.000 description 5
- 229910052787 antimony Inorganic materials 0.000 description 5
- WATWJIUSRGPENY-UHFFFAOYSA-N antimony atom Chemical compound [Sb] WATWJIUSRGPENY-UHFFFAOYSA-N 0.000 description 5
- -1 e.g. Substances 0.000 description 5
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 5
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 4
- 238000000137 annealing Methods 0.000 description 4
- 239000002585 base Substances 0.000 description 4
- 230000001427 coherent effect Effects 0.000 description 4
- 150000001875 compounds Chemical class 0.000 description 4
- 230000000694 effects Effects 0.000 description 4
- 239000012530 fluid Substances 0.000 description 4
- 229910052734 helium Inorganic materials 0.000 description 4
- 239000001307 helium Substances 0.000 description 4
- SWQJXJOGLNCZEY-UHFFFAOYSA-N helium atom Chemical compound [He] SWQJXJOGLNCZEY-UHFFFAOYSA-N 0.000 description 4
- 239000001257 hydrogen Substances 0.000 description 4
- 229910052739 hydrogen Inorganic materials 0.000 description 4
- 230000004048 modification Effects 0.000 description 4
- 238000012986 modification Methods 0.000 description 4
- 229910052750 molybdenum Inorganic materials 0.000 description 4
- 239000011733 molybdenum Substances 0.000 description 4
- 229910052757 nitrogen Inorganic materials 0.000 description 4
- XEKOWRVHYACXOJ-UHFFFAOYSA-N Ethyl acetate Chemical compound CCOC(C)=O XEKOWRVHYACXOJ-UHFFFAOYSA-N 0.000 description 3
- 239000000470 constituent Substances 0.000 description 3
- 238000010276 construction Methods 0.000 description 3
- 238000001816 cooling Methods 0.000 description 3
- 150000002739 metals Chemical group 0.000 description 3
- 239000000203 mixture Substances 0.000 description 3
- 239000002904 solvent Substances 0.000 description 3
- CSCPPACGZOOCGX-UHFFFAOYSA-N Acetone Chemical compound CC(C)=O CSCPPACGZOOCGX-UHFFFAOYSA-N 0.000 description 2
- XKRFYHLGVUSROY-UHFFFAOYSA-N Argon Chemical compound [Ar] XKRFYHLGVUSROY-UHFFFAOYSA-N 0.000 description 2
- RTZKZFJDLAIYFH-UHFFFAOYSA-N Diethyl ether Chemical compound CCOCC RTZKZFJDLAIYFH-UHFFFAOYSA-N 0.000 description 2
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 2
- 239000002253 acid Substances 0.000 description 2
- 238000007605 air drying Methods 0.000 description 2
- 125000000217 alkyl group Chemical group 0.000 description 2
- 229910052782 aluminium Inorganic materials 0.000 description 2
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 2
- 229910000074 antimony hydride Inorganic materials 0.000 description 2
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 2
- 239000011247 coating layer Substances 0.000 description 2
- 238000007872 degassing Methods 0.000 description 2
- 238000009713 electroplating Methods 0.000 description 2
- 239000004519 grease Substances 0.000 description 2
- 150000004678 hydrides Chemical class 0.000 description 2
- 150000002431 hydrogen Chemical class 0.000 description 2
- 229910052742 iron Inorganic materials 0.000 description 2
- 239000001301 oxygen Substances 0.000 description 2
- 229910052760 oxygen Inorganic materials 0.000 description 2
- 230000035515 penetration Effects 0.000 description 2
- 239000003208 petroleum Substances 0.000 description 2
- 238000002360 preparation method Methods 0.000 description 2
- 238000002203 pretreatment Methods 0.000 description 2
- OUULRIDHGPHMNQ-UHFFFAOYSA-N stibane Chemical compound [SbH3] OUULRIDHGPHMNQ-UHFFFAOYSA-N 0.000 description 2
- 238000003860 storage Methods 0.000 description 2
- 238000005406 washing Methods 0.000 description 2
- 239000004215 Carbon black (E152) Substances 0.000 description 1
- VYZAMTAEIAYCRO-UHFFFAOYSA-N Chromium Chemical compound [Cr] VYZAMTAEIAYCRO-UHFFFAOYSA-N 0.000 description 1
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 1
- FYYHWMGAXLPEAU-UHFFFAOYSA-N Magnesium Chemical compound [Mg] FYYHWMGAXLPEAU-UHFFFAOYSA-N 0.000 description 1
- GRYLNZFGIOXLOG-UHFFFAOYSA-N Nitric acid Chemical compound O[N+]([O-])=O GRYLNZFGIOXLOG-UHFFFAOYSA-N 0.000 description 1
- 241000220010 Rhode Species 0.000 description 1
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 1
- 150000007513 acids Chemical class 0.000 description 1
- 239000003513 alkali Substances 0.000 description 1
- 229910002065 alloy metal Inorganic materials 0.000 description 1
- VRAIHTAYLFXSJJ-UHFFFAOYSA-N alumane Chemical compound [AlH3].[AlH3] VRAIHTAYLFXSJJ-UHFFFAOYSA-N 0.000 description 1
- 229910052786 argon Inorganic materials 0.000 description 1
- 238000005452 bending Methods 0.000 description 1
- DMERAQVOEMBXQU-UHFFFAOYSA-N carbonyl dibromide;osmium Chemical compound [Os].BrC(Br)=O DMERAQVOEMBXQU-UHFFFAOYSA-N 0.000 description 1
- QALZILIGOXJDCX-UHFFFAOYSA-N carbonyl dichloride;ruthenium Chemical compound [Ru].ClC(Cl)=O QALZILIGOXJDCX-UHFFFAOYSA-N 0.000 description 1
- 239000012159 carrier gas Substances 0.000 description 1
- 239000003638 chemical reducing agent Substances 0.000 description 1
- 229910052804 chromium Inorganic materials 0.000 description 1
- 239000011651 chromium Substances 0.000 description 1
- AHXGRMIPHCAXFP-UHFFFAOYSA-L chromyl dichloride Chemical compound Cl[Cr](Cl)(=O)=O AHXGRMIPHCAXFP-UHFFFAOYSA-L 0.000 description 1
- 238000004891 communication Methods 0.000 description 1
- 230000006854 communication Effects 0.000 description 1
- 239000004020 conductor Substances 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- VURKTKHHTUWVPW-UHFFFAOYSA-N copper nitroxyl Chemical group [Cu].N=O VURKTKHHTUWVPW-UHFFFAOYSA-N 0.000 description 1
- 238000009826 distribution Methods 0.000 description 1
- 230000005611 electricity Effects 0.000 description 1
- 239000003792 electrolyte Substances 0.000 description 1
- 229910052736 halogen Inorganic materials 0.000 description 1
- 229930195733 hydrocarbon Natural products 0.000 description 1
- 150000002430 hydrocarbons Chemical class 0.000 description 1
- 230000006698 induction Effects 0.000 description 1
- JEIPFZHSYJVQDO-UHFFFAOYSA-N iron(III) oxide Inorganic materials O=[Fe]O[Fe]=O JEIPFZHSYJVQDO-UHFFFAOYSA-N 0.000 description 1
- 229910001338 liquidmetal Inorganic materials 0.000 description 1
- 229910052749 magnesium Inorganic materials 0.000 description 1
- 239000011777 magnesium Substances 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 229910052753 mercury Inorganic materials 0.000 description 1
- 229910001507 metal halide Inorganic materials 0.000 description 1
- 150000005309 metal halides Chemical class 0.000 description 1
- 229910052987 metal hydride Inorganic materials 0.000 description 1
- 150000004681 metal hydrides Chemical class 0.000 description 1
- 239000007769 metal material Substances 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 229910017604 nitric acid Inorganic materials 0.000 description 1
- ODUCDPQEXGNKDN-UHFFFAOYSA-N nitroxyl Chemical class O=N ODUCDPQEXGNKDN-UHFFFAOYSA-N 0.000 description 1
- 230000001590 oxidative effect Effects 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 238000005554 pickling Methods 0.000 description 1
- 150000003839 salts Chemical class 0.000 description 1
- 238000005488 sandblasting Methods 0.000 description 1
- 238000007789 sealing Methods 0.000 description 1
- KXCAEQNNTZANTK-UHFFFAOYSA-N stannane Chemical compound [SnH4] KXCAEQNNTZANTK-UHFFFAOYSA-N 0.000 description 1
- 238000005979 thermal decomposition reaction Methods 0.000 description 1
- 229910000083 tin tetrahydride Inorganic materials 0.000 description 1
- 239000002912 waste gas Substances 0.000 description 1
Images
Classifications
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- D—TEXTILES; PAPER
- D01—NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
- D01D—MECHANICAL METHODS OR APPARATUS IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS
- D01D5/00—Formation of filaments, threads, or the like
- D01D5/04—Dry spinning methods
-
- 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
- C23C16/02—Pretreatment of the material to be coated
- C23C16/0227—Pretreatment of the material to be coated by cleaning or etching
-
- 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
-
- 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
-
- 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
- Y10S—TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10S428/00—Stock material or miscellaneous articles
- Y10S428/922—Static electricity metal bleed-off metallic stock
- Y10S428/9335—Product by special process
- Y10S428/938—Vapor deposition or gas diffusion
-
- 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
- Y10T428/00—Stock material or miscellaneous articles
- Y10T428/12—All metal or with adjacent metals
- Y10T428/12472—Microscopic interfacial wave or roughness
-
- 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
- Y10T428/00—Stock material or miscellaneous articles
- Y10T428/12—All metal or with adjacent metals
- Y10T428/12493—Composite; i.e., plural, adjacent, spatially distinct metal components [e.g., layers, joint, etc.]
- Y10T428/12681—Ga-, In-, Tl- or Group VA metal-base component
-
- 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
- Y10T428/00—Stock material or miscellaneous articles
- Y10T428/12—All metal or with adjacent metals
- Y10T428/12493—Composite; i.e., plural, adjacent, spatially distinct metal components [e.g., layers, joint, etc.]
- Y10T428/12736—Al-base component
- Y10T428/1275—Next to Group VIII or IB metal-base component
-
- 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
- Y10T428/00—Stock material or miscellaneous articles
- Y10T428/12—All metal or with adjacent metals
- Y10T428/12493—Composite; i.e., plural, adjacent, spatially distinct metal components [e.g., layers, joint, etc.]
- Y10T428/12771—Transition metal-base component
- Y10T428/12806—Refractory [Group IVB, VB, or VIB] metal-base component
- Y10T428/12826—Group VIB metal-base component
-
- 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
- Y10T428/00—Stock material or miscellaneous articles
- Y10T428/12—All metal or with adjacent metals
- Y10T428/12493—Composite; i.e., plural, adjacent, spatially distinct metal components [e.g., layers, joint, etc.]
- Y10T428/12771—Transition metal-base component
- Y10T428/12861—Group VIII or IB metal-base component
- Y10T428/12937—Co- or Ni-base component next to Fe-base component
Definitions
- the invention thus makes it possible for the first time to produce a metal coating which is interlocked with the base metal in such a manner as to produce a substantially integral product.
- the product thus distinguishes from so-called wet-plating of metal surfaces, e.g., as in electroplating, in that there the plating produces a substantially laminated product and the plating is not interlocked and deposited in the bottom and wall surfaces of the pores or minute, substantially invisible depressions in the metal surface.
- wet-plating of metal surfaces e.g., as in electroplating
- a product is produced wherein the metal plate is carried out utilizing gaseous heat decomposable metals and whereby the metal to be plated is initially heated to drive off all occluded gases and while thus heated is subjected to vacuum or reduced pressure conditions so as to expunge the metal surface to be plated of all gases and permit the gases containing the gaseous metal to enter the pores and sub-microscopic depressions in the metal surface and deposit the metal therein to thus form an interlocked substantially integral metal product.
- Another object of the invention is to provide an improved method of plating utilizing gaseous metal compounds and wherein the gaseous metal deposition is carried out so as to produce an interlocking of the metal coating with the base metal and thus provide a substantially deeper penetration of the coating metal into the base metal than has heretofore been effected by wet and dry methods of plating.
- FIGURE 1 illustrates diagrammatically and pictorially an apparatus for carrying out the gaseous metal plating in accordance with this invention
- FIGURE 2 is a vertical cross-sectional view taken substantially on the line 22 of FIGURE 1, and looking in the direction of the arrows;
- FIGURE 3 is a similar cross-sectional view as in FIGURE 2, taken substantially on the line 3--3 of FIG- URE 1, and looking in the direction of the arrows;
- FIGURE 4 is a cross-sectional view through the gaseous metal plating chamber, taken substantially on the line 4-4 of FIGURE 3, and looking in the direction of the arrows;
- FIGURE 5 is an enlarged view showing a metal article plated by the wet plating method
- FIGURE 6 is a similar view illustrating a like crosssection of a metal strip plated in accordance with this invention.
- FIGURE 7 is a similar view in perspective as in FIG- URE 1, illustrating a modification of the apparatus and process therein, and wherein the metal strip to be coated is heated by means of a closed coil and the deaeration chamber is substantially integral with the gaseous deposition chamber, providing a more compact apparatus;
- FIGURE 8 is a cross sectional view taken on the line 8-8 of FIGURE 1, and looking in the direction of the arrows;
- FIGURE 9 is a somewhat enlarged cross sectional View taken on the line 9-9 of FIGURE 1, and looking in the direction of the arrows;
- FIGURE 10 is a similar sectional view taken substantially on the line 10-10 of FIGURE 9, and looking in the direction of the arrows;
- FIGURE 11 is a similar sectional view on a somewhat enlarged scale taken on the line 1111 of FIGURE 1, and looking in the direction of the arrows.
- the invention is not to be restricted to the shape or size of the base metal to be plated.
- the gaseous metal plating may be carried out as a continuous or discontmuous process.
- a metal strip 10 which may comprise steel, aluminum, magnesium, copper, etc., or alloy metals, and which has been previously cleaned as by electrochemical or sand blasting or the like, is passed over the roll 12 and thence into the cleaning bath 14, being drawn under the spaced rolls 15 arranged in the bottom of the cleaning tank 16.
- the cleaning bath 14 may comprise rinse water, or ganic Volatile solvent, e.g., ethyl acetate, acetone, petroleum solvent, or mixtures thereof, to wash the strip and remove any grease and foreign particles or pro-cleaning solution.
- an air blast 2.2 which preferably comprises hot air as supplied from the blower 24, the air being drawn into the blower 24 through the pipe line 26, as shown in FIGURE 1.
- the heating chamber 20 comprises an elongated compartment having insulated inner walls 34 and a slot opening 36 for the entrance of the metal strip 10, and a similar exit opening 37 at the opposite end, the heating chamber being suitably fabricated from two halves which are bolted together, as at 38, as shown in FIGURES 1 and 2.
- a gas lock gate means 4! Joined to and communicating with the exit opening 37 of the heating chamber 20 is a gas lock gate means 4! which comprises an I-shaped member having a longitudinal slot opening 42 therethrough which is adapted to register with the exit opening 37 so as to accommodate the passage of the metal strip 10.
- Communicating with the opening 42 of the gas lock 40 are tubular conduits 44 and 45 through which is passed the inert gas to provide the gaseous gate interlocked between chamber 253 and the deaerating chamber 47.
- the deaerating chamber 47 preferably comprises an elongated cylindrical chamber which is fitted with a pressure gauge 48 and conduits 50 and 52 for the admission and withdrawal of gas from within the chamber 47.
- a pressure gauge 48 Arranged Within the chamber 47 are cooperating pairs of guide rolls 54 and 56 which are arranged to guide and support the metal strip as the same is drawn therealong through the chamber.
- the conduit 50 is open at its inner end 57 and communicates with the chamber 47, the conduits being connected to a vacuum pump or the like to provide a vacuum or reduced pressure chamber for drawing ofli any occluded gases from the surface of the metal strip before subjecting the same to gaseous metal plating.
- the conduit 52 is provided for introducing inert gas or washing gases, such as nitrogen, helium, carbon dioxide, etc., where it is desired to introduce the same while subjecting the strip to reduced pressure conditions. In this manner a gaseous washing effect may be produced simultaneously with the low pressure conditions as efiected by the vacuum pump.
- a valve 58 is provided in the line 52 so that the same may be sealed off where it is desired to use only the vacuum for low pressure treatment in chamber 47.
- gaseous gate interlock 60 which is of similar construction and operation as gas lock gaseous gate interlock 40.
- the strip is thus passed from the chamber 47 into the gaseous metal plating chamber 65 which is preferably of similar construction as chamber 47, and is provided with a pressure gauge 67 and window 68 for viewing the interior of the plating chamber.
- Conduit 69 which communicates with the plating chamber at one end permits the introduction of the heat decomposable gaseous metal plating compound.
- a conduit 70 is provided at the opposite end. The gaseous metal compound is preferably introduced through the conduit 69 and after circulating through the chamber and in contact with the metal strip is withdrawn through the exit conduit 70.
- the metal strip 10 is passed through the gaseous metal plating chamber 65, it is drawn outward through the exit opening 80 and through the gaseous lock gate 82, which is of similar construction and operation as gas locks 40 and 60, and thence through the heat treating chamber 86 which is constructed and operated similarly as the heating chamber 20. .
- the finished plated strip is reduced pressure.
- the metal strip being treated is passed through a heating chamber 92, which chamber in this instance is heated by the helical coils 94 through which heated fluid, such as steam, hot water or the like fluid, is passed.
- Strip 10 is supported and drawn centrally of the coils 94 so as be evenly heated.
- Conduits 96, 97 are connected to the chamber 92 and the coil 94 for passing heated fluid through the coil.
- the strip 16 After the strip 16 has passed through the pro-heating chamber 94 it is conducted into the vacuum or low pressure chamber 99 and thence into the gas plating chamber 1%, and finally through the post heating or annealing chamber 162, after which the finished gas plated metal strip 10 is rolled up on the storage roll 104.
- the low pressure chamber 99 is provided with a pressure gauge 106, and the conduit 1% which is in communicat-ion with the interior of the chamber is provided, the conduit being connected to a vacuum pump or evacuating prime mover whereby the chamber 99 is kept under Provision is made at the inlet and exit of the stnip for properly sealing the openings.
- the gates iii ⁇ and 111 comprise sponge rubber seals which function as a squeegy to seal the strip as the same moves into and out of the chamber 99.
- Appropriate guide rolls 113 are arranged on the standard 114 and which support and guide the strip 10* through the low pressure chamber.
- conduits 116, 118 are provided through which the heat decomposable gaseous metal compound is introduced and discharged respectively, as shown more clearly in FIGURE 9.
- a pressure gauge 12% is provided for observing the fluid pressure in the gaseous plating chamber.
- baflies 1'12, 123 are spacedly arranged longitudinally of the plating chamber, as illustrated in FIGURE 9.
- the gaseous metal compound is admitted through the conduit 1.16 at one end of the chamber 1% and passes downwardly and upwardly about the baffles 112, 123, as indicated by arrows at 125, the exhaust gases and unused decomposition products are drawn off through the conduit 118 at the opposite end of the gaseous plating chamber.
- the strip 10 after passing through the gaseous metal plating chamber is drawn outwardly through the exit gate 127 and into the post heating chamber 102, and after cooling in the air is .stored on the roll 104.
- An important aspect of applicants invention is the provision of a vacuum or low pressure pretreatment following the heating of the strip or metal article to be gaseous metal plated.
- the vacuum pressures used may vary depending upon the particular metal being plated, in each instance being sufiiciently high to produce a perfectly dry metal surface being free of moisture and water vapor and wherein the pores and sub-microscopic depressions in the metal surface are free of all occluded gases.
- This pre-heating and vacuum or low pressure treatment makes it possible to produce a greater depth of penetration of the gaseous metal plated layer into the surface of the base metal and thus bring about the production of a metal product having a metal coating layer which penetrates into the base metal to provide the same with a layer or metal which is interlocked with the base metal thus forming a substantially integral metal layer therewith.
- the invention accordingly provides a method of dry plating metal articles in a manner to provide the same with a coating metal layer which adheres tenaciously to the base metal forming a coherent, substantially integral body.
- a coating metal layer which adheres tenaciously to the base metal forming a coherent, substantially integral body.
- wet electroplating it has been the practice to apply a flash coating of metal such as copper over the base metal to improve the cohension of the plated metal. Such practice becomes entirely unnecessary with gaseous metal plating in accordance with applicants invention.
- inert gas gate locks such as shown at 40- and 60 in FIGURE 2, the inert gas medium used in this instance being carbon dioxide, nitrogen or the like, the pressure being maintained slightly higher than the chamber to be protected so as to cause leakage of the inert vapor into the chamber rather than leakage of the gas outwardly of the chamber.
- gaseous plating atmosphere may be formed by mixing an inert gas with the vapors of a volatile metal compound or by atomizing a liquid metal compound into a blast of hot inert gas or other equivalent method.
- Carbon dioxide, helium, nitrogen, hydrogen, the gaseous product of controlled burning of hydrocarbon gases free of oxygen, and the like, have been utilized as a carrier medium or inert gas medium.
- the use of hydrogen is preferred, as for example, in the cleaning anneal chamber where its ability to act as a reducing agent may be put to advantage to remove the oxide film or rust from iron or metal strip being plated.
- Metals to be deposited may be introduced as gaseous metal carbonyls or vaporized solutions of certain of the metal carbonyls in readily vaporizable solvents (for example, petroleum ether), also nitroxyl compounds, nitrosyl carbonyls, metal hydrides, metal alkyls, metal halides, and the like.
- readily vaporizable solvents for example, petroleum ether
- nitroxyl compounds for example, nitrosyl carbonyls, metal hydrides, metal alkyls, metal halides, and the like.
- Illustrative compounds of the carbonyl type are nickel, iron, chromium, molybdenum, cobalt, and mixed carbonyls.
- Illustrative compounds of other groups are the nitroxyls, such as copper nitroxyl; nitrosyl carbonyls, for example cobalt nitrosyl carbonyl; hydrides, such as antimony hydride, tin hydride; metal alkyls, such as chromyl chloride; and carbonyl halogens, for example osmium carbonyl bromide, ruthenium carbonyl chloride, and the like.
- nitroxyls such as copper nitroxyl
- nitrosyl carbonyls for example cobalt nitrosyl carbonyl
- hydrides such as antimony hydride, tin hydride
- metal alkyls such as chromyl chloride
- carbonyl halogens for example osmium carbonyl bromide, ruthenium carbonyl chloride, and the like.
- Each material from which a metal may be plated has a temperature at which decomposition is complete. However, decomposition may take place slowly at a lower temperature or While the vapors are being raised in temperature through some particular range. For example, nickel carbonyl completely decomposes at a temperature in the range of 375 F. to 400 F. However, nickel carbonyl starts to decompose slowly at about 175 F. and therefore decomposition continues during the time of heating from 200 F. to 380 F.
- a large number of the metal carbonyls and hydrides may be effectively and efliciently decomposed at a temperature in the range of 350 F. to 450 F.
- the hot strip upon cooling to the plating temperature range after deaeration may be led directly to plating chamber with or without an annealing stage therebetween. If an anneal is desired, the operation within the apparatus may be carried out in a manner similar to that used When starting with cold metal.
- the metal strip may be raised to and maintained at desired temperatures by causing the metal to conduct electricity or by induction heating.
- the temperature in preheating and post heating chamhers is considerably higher than plating temperatures, i.e., in the range of 400 to 1200 F.
- the metallic material may be cleaned by employing conventional methods used in the art, comprising electro-chemically cleaning by moving the same through a bath of alkali or acid electrolyte wherein the strip is made the cathode or anode.
- Pickling of the metal with hydrochloric, sulfuric or nitric acid, or a combination of acids may also be made as a part of the cleaning process, and the strip thoroughly rinsed or Washed prior to introduction into the plating apparatus.
- the metal strip is in good condition a cleaning anneal may suffice, in which event the strip may be heated just prior to entering the vacuum treatment chamber.
- the post heat treatment of the gaseous plated metal may be omitted if desired, but is preferred in most cases to produce a more even textured and smoother plating film or coating.
- the post heat treatment also is advantageous in preventing the entrainment of moisture.
- the post heating temperatures employed will vary for difierent metal platings and base metals treated as aforementioned. Generally the post temperature is the same or somewhat higher than the pre-plating heat treatment, the latter being governed by the temperature required to eifect substantially complete removal of gas occlusions in the surface depressions of the base metal under the reduced pressure conditions.
- the post heating of the plated product in addition to degassing the strip may be controlled to effect annealing of the strip.
- the duration of heating in both pre-heating chamber and post heating chamber may be suitably varied to provide for a heat treatment of from ten to twenty minutes as desired.
- EXAMPLE I Nickel-Coated Steel Strip A steel strip which is to be coated and which has been chemically cleaned in the conventional manner is passed through the rinsing bath and air dried by hot air blast. The strip is then moved along through the pre-heating chamber and subjected to a temperature of 525 F., the strip being moved along at a uniform rate and such that the plating time allowed is approximately two to three minutes. The heated strip then passes directly into the low pressure or vacuum chamber where it is subjected to a vacuum of approximately 1 mm. Hg after which the strip is passed along and through the gaseous metal plating chamber. Nickel carbonyl in the form of vapor and admixed with carbon dioxide carrier gas is fed to the plating chamber.
- the metal carbonyl being present in the mixture of vapor is nickel carbonyl and carbon dioxide in the proportionate amount of about five ozs. of carbonyl per cubic foot of carbon dioxide.
- the temperature in the plating chamber and strip is approximately 400 F. For a plating exposure of twoaud one-half minutes, this provides a coating of nickel of approximately 0.002 inch which interlocked and penetrated into the micropore surfaces of the metal is provided. After gaseous plating the strip is moved from the plating chamber through the post heating chamber where it is subjected to a temperature of approximately 700 F. in the presence of carbon dioxide.
- EXAMPLE II Nickel Coated Aluminum Aluminum metal strip is substituted for steel strip material and processed as in Example I, except that both pre-heating and postheating treatments are carried out at about 500 F.
- EXAMPLE III Cobalt Coated Steel Antimony Coated Copper Metal Copper sheet is coated with antimony by first preheating copper strip material free of foreign matter in an atmosphere of helium at 525 F. The heat treated strip is then passed into a vacuum chamber where the hot metal strip is subjected to a vacuum pressure of 50 mm. Hg and in an atmosphere of carbon dioxide. The strip is then immediately passed to the gaseous metal plating chamber where it is subjected to a gaseous atmosphere of antimony hydride heated to 400 F. to effect decomposition and plating out of antimony metal onto the copper strip. The post heat treatment is carried out at a temperature of 475 F. to produce a final coherent antimony coating on the copper metal base strip, being integrally united with the copper metal.
- EXAMPLE V A steel sheet isgas plated with molybdenum metal similarly as described in Example I, and using molybdenum carbonyl in place of nickel carbonyl. A temperature of approximately 450 F. is used in the gas plating chamber.
- the essence of the invention is the provision of a' pre-treatment so as to deaerate or de-gas the metal to be gaseous plated so as to provide a perfectly dry, Water-vapor and hydrogen free metal surface for receiving the gaseous metal plating.
- the process provides a finished product as aforementioned, wherein the plating or metal coat is interlocked with the base metal so as to form a substantially integral metal product.
- FIGURES and 6 illustrate in enlarged section, the essential difference in structure between wet plated metal products and gaseous or dry plated metal products.
- metal coating is applied over conventional treated metal as generally indicated by the reference character 150 which is wet plated by a metal coating as indicated at 151, there is invariably a discontinuous layer or plurality of microscopic gas pockets or bubbles 152 in between the metal coating layer 151 and base metal 150. In extreme cases where these gas occlusions become large enough or continuous, the metal coating peels away from the base metal.
- FIGURE 6 there is illustrated in .enlarged section a gaseous metal coated structure as prd **d in accordance with this invention.
- the base metal and metal coating 156 are interlocked to provide a substantially integral structure.
- the microscopic pores at the surface of the metal are freed of gas occlusions and gaseous metal allowed to enter and thus penetrate into the body of the base metal, deposition of metal taking place to thus provide an interlocking of the metal coating or plating with the base metal.
- a method of producing a metal article having a layer of metal interlocked with the base metal and forming a substantially integral body of metal which comprises thoroughly cleaning the surface of the base metal including rinsing and air drying to remove foreign matter, heating the metal and while thus heated subjecting the same to reduced atmospheric pressure conditions to deaerate the pores of the metal surface of occluded gases, and then subjecting the resultant deaerated metal to gaseous metal deposition by intimately contacting said deaerated metal with a heat-decomposable metal compound of molybdenum and circulating said gaseous metal compound about said article in a helical shaped path to cause said metal compound to penetrate deeply into the surface of said article and diffuse in the pores and then thermally decomposed to cause deposition of the metal constituent thereof into the pores and sub-microscopic depressions of the base metal to produce a molybdenum metal plated product having integrally united layers of metal, said heating of the metal in a reduced atmosphere being conducted in the presence of non-oxidizing conditions.
- a method of producing a metal article having a base metal and continuous layer of metal interlocked with said base metal and forming a substantially integral body of metal comprising cleaning the surface of the base metal including rinsing and air drying to remove foreign matter, heating the metal and while thus heated subjecting the same to reduced atmospheric pressure conditions to deaerate the pores of the metal surface of occluded gases and produce a dry, deaerated base metal surface, subjecting the thus deaerated metal to gaseous metal deposition by contacting said deaerated metal with a heat-decomposable gaseous metal compound at a temperature suflicient to cause thermal decomposition of the gaseous metal compound and circulating said gaseous metal compound about said article in a helical shaped path to cause said metal compound to penetrate deeply into the surface of said article and dilfuse in the pores and then thermally decomposed to cause deposition of the metal constituent thereof into the pores and sub-microscopic depressions of the base metal, and thereafter heating the plated material to a temperature
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Description
Sept. 25, 1962 F. E. DRUMMOND 3,055,089
GASEOUS METAL PRODUCT AND PROCESSES Filed Aug. 6, 1958 2 Sheets-Sheet 1 INVENTOR FOLSOM DRl/MNONO A'YTORNEYS Sept. 25, 1962 F. E. DRUMMOND GASEOUS METAL PRODUCT AND PROCESSES 2 Sheets$heet 2 Filed Aug. 6, 1958 ATTORNEYS United States Patent 3,055,089 GASEOUS METAL PRODUCT AND PROCESSES Folsom E. Drummond, Washington, D.C., assignor, by mesne assignments, to Union Carbide Corporation, New York, NFL, a corporation of New York Filed Aug. 6, 1958, Ser. No. 753,567 7 Claims. ((31. 29196) This invention relates to the art of gaseous deposition of metals. The invention more particularly is concerned with the preparation of gaseous plated metal products and improved processes for carrying out gaseous metal deposition.
In the preparation of coatings as obtained for example by gaseous metal deposition of metal carbonyls, it has been proposed to produce such metal coatings by treating the base metal, in the form of a strip or other article, which has been mechanically or chemically cleaned, to gaseous metal deposition by heating the material in an atmosphere containing the heat-decomposable gaseous metal compound and thereafter subjecting the gaseous metal treated article to heating to produce a relatively smooth, uniform, coherent continuous metal coating. The present invention distinguishes from the prior processes in that the metal base or material to be plated is subjected to a pre-treatment to produce a dry, deaerated metal surface for receiving the gaseous metal coating.
The invention thus makes it possible for the first time to produce a metal coating which is interlocked with the base metal in such a manner as to produce a substantially integral product. The product thus distinguishes from so-called wet-plating of metal surfaces, e.g., as in electroplating, in that there the plating produces a substantially laminated product and the plating is not interlocked and deposited in the bottom and wall surfaces of the pores or minute, substantially invisible depressions in the metal surface. Heretofore it has been known that such pores and submicroscopic depressions of the surface metal could not be plated utilizing the so-called wet processes, wherein solutions containing the salts of the metal to be plated are utilized with or without electrical means.
By the present invention a product is produced wherein the metal plate is carried out utilizing gaseous heat decomposable metals and whereby the metal to be plated is initially heated to drive off all occluded gases and while thus heated is subjected to vacuum or reduced pressure conditions so as to expunge the metal surface to be plated of all gases and permit the gases containing the gaseous metal to enter the pores and sub-microscopic depressions in the metal surface and deposit the metal therein to thus form an interlocked substantially integral metal product.
It is the principal object of the present invention to produce a gaseous metal coated product wherein the metal product produced is made up of a metal base and a coating which is substantially integral therewith.
Another object of the invention is to provide an improved method of plating utilizing gaseous metal compounds and wherein the gaseous metal deposition is carried out so as to produce an interlocking of the metal coating with the base metal and thus provide a substantially deeper penetration of the coating metal into the base metal than has heretofore been effected by wet and dry methods of plating.
It is another object of the invention to provide an improved method of producing metal coatings which can withstand elevated temperatures and bending stresses without causing blistering or peeling of the metal coating.
It is a further object of the invention to provide a method of producing metal coated articles having a coice herent interlocked metal surface coating over the metal base.
It is a still further object of the invention to provide a product comprising a base metal material which is coated with iuniformly deposited metal wherein the metal coated with uniformly deposited metal wherein the metal and diffuse therein so as to become substantially integral with the base metal.
These and other objects and advantages will become apparent as the description proceeds, and taken in conjunction with the drawings forming a part of this specification, wherein- FIGURE 1 illustrates diagrammatically and pictorially an apparatus for carrying out the gaseous metal plating in accordance with this invention;
FIGURE 2 is a vertical cross-sectional view taken substantially on the line 22 of FIGURE 1, and looking in the direction of the arrows;
FIGURE 3 is a similar cross-sectional view as in FIGURE 2, taken substantially on the line 3--3 of FIG- URE 1, and looking in the direction of the arrows;
FIGURE 4 is a cross-sectional view through the gaseous metal plating chamber, taken substantially on the line 4-4 of FIGURE 3, and looking in the direction of the arrows;
FIGURE 5 is an enlarged view showing a metal article plated by the wet plating method;
FIGURE 6 is a similar view illustrating a like crosssection of a metal strip plated in accordance with this invention;
FIGURE 7 is a similar view in perspective as in FIG- URE 1, illustrating a modification of the apparatus and process therein, and wherein the metal strip to be coated is heated by means of a closed coil and the deaeration chamber is substantially integral with the gaseous deposition chamber, providing a more compact apparatus;
FIGURE 8 is a cross sectional view taken on the line 8-8 of FIGURE 1, and looking in the direction of the arrows;
FIGURE 9 is a somewhat enlarged cross sectional View taken on the line 9-9 of FIGURE 1, and looking in the direction of the arrows;
FIGURE 10 is a similar sectional view taken substantially on the line 10-10 of FIGURE 9, and looking in the direction of the arrows; and
FIGURE 11 is a similar sectional view on a somewhat enlarged scale taken on the line 1111 of FIGURE 1, and looking in the direction of the arrows.
In the preferred process of the invention, and which will be described with particular reference to the plating of a continuous length metal strip, it is understood that the invention is not to be restricted to the shape or size of the base metal to be plated. For example, the gaseous metal plating may be carried out as a continuous or discontmuous process.
In the embodiment shown in FIGURES 1-4 of the the drawings, a metal strip 10, which may comprise steel, aluminum, magnesium, copper, etc., or alloy metals, and which has been previously cleaned as by electrochemical or sand blasting or the like, is passed over the roll 12 and thence into the cleaning bath 14, being drawn under the spaced rolls 15 arranged in the bottom of the cleaning tank 16.
The cleaning bath 14 may comprise rinse water, or ganic Volatile solvent, e.g., ethyl acetate, acetone, petroleum solvent, or mixtures thereof, to wash the strip and remove any grease and foreign particles or pro-cleaning solution. As the metal strip 10 is drawn upwardly and over the roll 18 it is subjected to an air blast 2.2 which preferably comprises hot air as supplied from the blower 24, the air being drawn into the blower 24 through the pipe line 26, as shown in FIGURE 1.
After passing the metal strip through the tank 16, it is drawn upwardly and over the roll 18% and thence into the heating chamber 20, the strip being moved along and centrally between the vertically spaced electrical heating elements, or resistance coils 30. The heating elements 30 are connected to a source of electrical current by suitable conductors 32. The heating chamber 20 comprises an elongated compartment having insulated inner walls 34 and a slot opening 36 for the entrance of the metal strip 10, and a similar exit opening 37 at the opposite end, the heating chamber being suitably fabricated from two halves which are bolted together, as at 38, as shown in FIGURES 1 and 2.
Joined to and communicating with the exit opening 37 of the heating chamber 20 is a gas lock gate means 4! which comprises an I-shaped member having a longitudinal slot opening 42 therethrough which is adapted to register with the exit opening 37 so as to accommodate the passage of the metal strip 10. Communicating with the opening 42 of the gas lock 40 are tubular conduits 44 and 45 through which is passed the inert gas to provide the gaseous gate interlocked between chamber 253 and the deaerating chamber 47. V,
The deaerating chamber 47, as shown, preferably comprises an elongated cylindrical chamber which is fitted with a pressure gauge 48 and conduits 50 and 52 for the admission and withdrawal of gas from within the chamber 47. Arranged Within the chamber 47 are cooperating pairs of guide rolls 54 and 56 which are arranged to guide and support the metal strip as the same is drawn therealong through the chamber. As illustrated, the conduit 50 is open at its inner end 57 and communicates with the chamber 47, the conduits being connected to a vacuum pump or the like to provide a vacuum or reduced pressure chamber for drawing ofli any occluded gases from the surface of the metal strip before subjecting the same to gaseous metal plating. The conduit 52 is provided for introducing inert gas or washing gases, such as nitrogen, helium, carbon dioxide, etc., where it is desired to introduce the same while subjecting the strip to reduced pressure conditions. In this manner a gaseous washing effect may be produced simultaneously with the low pressure conditions as efiected by the vacuum pump. A valve 58 is provided in the line 52 so that the same may be sealed off where it is desired to use only the vacuum for low pressure treatment in chamber 47.
From the deaerating chamber 47 strip 10 passes through the gaseous gate interlock 60 which is of similar construction and operation as gas lock gaseous gate interlock 40.
The strip is thus passed from the chamber 47 into the gaseous metal plating chamber 65 which is preferably of similar construction as chamber 47, and is provided with a pressure gauge 67 and window 68 for viewing the interior of the plating chamber. Conduit 69 which communicates with the plating chamber at one end permits the introduction of the heat decomposable gaseous metal plating compound. At the opposite end a conduit 70 is provided. The gaseous metal compound is preferably introduced through the conduit 69 and after circulating through the chamber and in contact with the metal strip is withdrawn through the exit conduit 70.
To assist in the even distribution and circulation of the gaseous metal compound in the chamber 65, the same is provided with helical-shaped bafiles 74 and 76'. Guide rolls 78 and 79 are arranged in the chamber 65 and adapted to support and guide the strip 10 therealong similarly as guide rolls 54 and 56 of chamber 47. 7
After the metal strip 10 is passed through the gaseous metal plating chamber 65, it is drawn outward through the exit opening 80 and through the gaseous lock gate 82, which is of similar construction and operation as gas locks 40 and 60, and thence through the heat treating chamber 86 which is constructed and operated similarly as the heating chamber 20. .The finished plated strip is reduced pressure.
4 drawn from the heat treatment chamber 86, and after cooling in the air, is wound up on the storage roll 88, as illustrated in FIGURE 1.
In a modification shown in FIGURES 7-11, the metal strip being treated, as shown at 10, is passed through a heating chamber 92, which chamber in this instance is heated by the helical coils 94 through which heated fluid, such as steam, hot water or the like fluid, is passed. Strip 10 is supported and drawn centrally of the coils 94 so as be evenly heated. Conduits 96, 97 are connected to the chamber 92 and the coil 94 for passing heated fluid through the coil.
After the strip 16 has passed through the pro-heating chamber 94 it is conducted into the vacuum or low pressure chamber 99 and thence into the gas plating chamber 1%, and finally through the post heating or annealing chamber 162, after which the finished gas plated metal strip 10 is rolled up on the storage roll 104.
The low pressure chamber 99 is provided with a pressure gauge 106, and the conduit 1% which is in communicat-ion with the interior of the chamber is provided, the conduit being connected to a vacuum pump or evacuating prime mover whereby the chamber 99 is kept under Provision is made at the inlet and exit of the stnip for properly sealing the openings. In this instance the gates iii} and 111 comprise sponge rubber seals which function as a squeegy to seal the strip as the same moves into and out of the chamber 99. Appropriate guide rolls 113 are arranged on the standard 114 and which support and guide the strip 10* through the low pressure chamber.
in the gaseous plating chamber 100, conduits 116, 118 are provided through which the heat decomposable gaseous metal compound is introduced and discharged respectively, as shown more clearly in FIGURE 9. A pressure gauge 12% is provided for observing the fluid pressure in the gaseous plating chamber.
In order to circulate the gaseous metal compound in contact with the moving sheet or strip 10, suitable baflies 1'12, 123 are spacedly arranged longitudinally of the plating chamber, as illustrated in FIGURE 9. The gaseous metal compound is admitted through the conduit 1.16 at one end of the chamber 1% and passes downwardly and upwardly about the baffles 112, 123, as indicated by arrows at 125, the exhaust gases and unused decomposition products are drawn off through the conduit 118 at the opposite end of the gaseous plating chamber.
The strip 10 after passing through the gaseous metal plating chamber is drawn outwardly through the exit gate 127 and into the post heating chamber 102, and after cooling in the air is .stored on the roll 104.
An important aspect of applicants invention is the provision of a vacuum or low pressure pretreatment following the heating of the strip or metal article to be gaseous metal plated.
The vacuum pressures used may vary depending upon the particular metal being plated, in each instance being sufiiciently high to produce a perfectly dry metal surface being free of moisture and water vapor and wherein the pores and sub-microscopic depressions in the metal surface are free of all occluded gases. This pre-heating and vacuum or low pressure treatment makes it possible to produce a greater depth of penetration of the gaseous metal plated layer into the surface of the base metal and thus bring about the production of a metal product having a metal coating layer which penetrates into the base metal to provide the same with a layer or metal which is interlocked with the base metal thus forming a substantially integral metal layer therewith.
The invention accordingly provides a method of dry plating metal articles in a manner to provide the same with a coating metal layer which adheres tenaciously to the base metal forming a coherent, substantially integral body. As is well known, in wet electroplating it has been the practice to apply a flash coating of metal such as copper over the base metal to improve the cohension of the plated metal. Such practice becomes entirely unnecessary with gaseous metal plating in accordance with applicants invention.
In carrying out the gaseous metal plating in accordance with applicants process, leakage of gas from one compartment to another is effectively prevented by the use of inert gas gate locks, such as shown at 40- and 60 in FIGURE 2, the inert gas medium used in this instance being carbon dioxide, nitrogen or the like, the pressure being maintained slightly higher than the chamber to be protected so as to cause leakage of the inert vapor into the chamber rather than leakage of the gas outwardly of the chamber.
In this process a stream of gaseous material is conducted into the gaseous plating chamber and circulated about the heated metal strip. The gaseous plating atmosphere may be formed by mixing an inert gas with the vapors of a volatile metal compound or by atomizing a liquid metal compound into a blast of hot inert gas or other equivalent method.
Carbon dioxide, helium, nitrogen, hydrogen, the gaseous product of controlled burning of hydrocarbon gases free of oxygen, and the like, have been utilized as a carrier medium or inert gas medium.
In some instances the use of hydrogen is preferred, as for example, in the cleaning anneal chamber where its ability to act as a reducing agent may be put to advantage to remove the oxide film or rust from iron or metal strip being plated.
Metals to be deposited may be introduced as gaseous metal carbonyls or vaporized solutions of certain of the metal carbonyls in readily vaporizable solvents (for example, petroleum ether), also nitroxyl compounds, nitrosyl carbonyls, metal hydrides, metal alkyls, metal halides, and the like.
Illustrative compounds of the carbonyl type are nickel, iron, chromium, molybdenum, cobalt, and mixed carbonyls.
Illustrative compounds of other groups are the nitroxyls, such as copper nitroxyl; nitrosyl carbonyls, for example cobalt nitrosyl carbonyl; hydrides, such as antimony hydride, tin hydride; metal alkyls, such as chromyl chloride; and carbonyl halogens, for example osmium carbonyl bromide, ruthenium carbonyl chloride, and the like.
Each material from which a metal may be plated has a temperature at which decomposition is complete. However, decomposition may take place slowly at a lower temperature or While the vapors are being raised in temperature through some particular range. For example, nickel carbonyl completely decomposes at a temperature in the range of 375 F. to 400 F. However, nickel carbonyl starts to decompose slowly at about 175 F. and therefore decomposition continues during the time of heating from 200 F. to 380 F.
A large number of the metal carbonyls and hydrides may be effectively and efliciently decomposed at a temperature in the range of 350 F. to 450 F. When working with most metal carbonyls We prefer to operate in a temperature in the general decomposition range of the volatile compounds.
If the metal is, for example, hot drawn strip, the hot strip upon cooling to the plating temperature range after deaeration may be led directly to plating chamber with or without an annealing stage therebetween. If an anneal is desired, the operation within the apparatus may be carried out in a manner similar to that used When starting with cold metal. The metal strip may be raised to and maintained at desired temperatures by causing the metal to conduct electricity or by induction heating.
The temperature in preheating and post heating chamhers is considerably higher than plating temperatures, i.e., in the range of 400 to 1200 F.
Preparatory to coating the strip, the metallic material may be cleaned by employing conventional methods used in the art, comprising electro-chemically cleaning by moving the same through a bath of alkali or acid electrolyte wherein the strip is made the cathode or anode.
Pickling of the metal with hydrochloric, sulfuric or nitric acid, or a combination of acids may also be made as a part of the cleaning process, and the strip thoroughly rinsed or Washed prior to introduction into the plating apparatus.
However, if the metal strip is in good condition a cleaning anneal may suffice, in which event the strip may be heated just prior to entering the vacuum treatment chamber.
In a cleaning anneal any grease and the like Will be burned away by bringing the strip to red heat.
The invention will be more clearly understood from the following description of one embodiment of the apparatus and its mode of operation.
By subjecting the metal to be plated to a pre-heatin g treatment prior to the vacuum or low pressure treatment, occluded gases are more readily removed and at a lower vacuum pressure. This vacuum deaeration treatment prior to gaseous metal plating constitutes an essential step of the process in order to produce an absolutely dry metal surface. The presence of hydrogen, oxygen or water vapor entrapped or occluded in the pores or irregularities over the surface of the metal is avoided by the present process and a thoroughly coherent metal coating produced.
The post heat treatment of the gaseous plated metal may be omitted if desired, but is preferred in most cases to produce a more even textured and smoother plating film or coating. The post heat treatment also is advantageous in preventing the entrainment of moisture. To further assist in this, it is preferable to carry out the post heat treatment in the presence of inert gas, e.g., helium, argon, nitrogen, carbon dioxide or the like. This may also be accomplished by allowing a controlled amount of gas leakage of waste gas to take place from the plating chamber or by circulating a small amount of the relatively spent or inert gases through the post heating chamber.
The post heating temperatures employed will vary for difierent metal platings and base metals treated as aforementioned. Generally the post temperature is the same or somewhat higher than the pre-plating heat treatment, the latter being governed by the temperature required to eifect substantially complete removal of gas occlusions in the surface depressions of the base metal under the reduced pressure conditions. The post heating of the plated product in addition to degassing the strip may be controlled to effect annealing of the strip. The duration of heating in both pre-heating chamber and post heating chamber may be suitably varied to provide for a heat treatment of from ten to twenty minutes as desired.
The following examples are illustrative but not limitative of the invention.
EXAMPLE I Nickel-Coated Steel Strip A steel strip which is to be coated and which has been chemically cleaned in the conventional manner is passed through the rinsing bath and air dried by hot air blast. The strip is then moved along through the pre-heating chamber and subjected to a temperature of 525 F., the strip being moved along at a uniform rate and such that the plating time allowed is approximately two to three minutes. The heated strip then passes directly into the low pressure or vacuum chamber where it is subjected to a vacuum of approximately 1 mm. Hg after which the strip is passed along and through the gaseous metal plating chamber. Nickel carbonyl in the form of vapor and admixed with carbon dioxide carrier gas is fed to the plating chamber. Approximately five cubic feet of nickel carbonyl-carbon dioxide mixture per hour is fed through the plating chamber, the metal carbonyl being present in the mixture of vapor is nickel carbonyl and carbon dioxide in the proportionate amount of about five ozs. of carbonyl per cubic foot of carbon dioxide. The temperature in the plating chamber and strip is approximately 400 F. For a plating exposure of twoaud one-half minutes, this provides a coating of nickel of approximately 0.002 inch which interlocked and penetrated into the micropore surfaces of the metal is provided. After gaseous plating the strip is moved from the plating chamber through the post heating chamber where it is subjected to a temperature of approximately 700 F. in the presence of carbon dioxide.
. EXAMPLE II Nickel Coated Aluminum Aluminum metal strip is substituted for steel strip material and processed as in Example I, except that both pre-heating and postheating treatments are carried out at about 500 F.
EXAMPLE III Cobalt Coated Steel Antimony Coated Copper Metal Copper sheet is coated with antimony by first preheating copper strip material free of foreign matter in an atmosphere of helium at 525 F. The heat treated strip is then passed into a vacuum chamber where the hot metal strip is subjected to a vacuum pressure of 50 mm. Hg and in an atmosphere of carbon dioxide. The strip is then immediately passed to the gaseous metal plating chamber where it is subjected to a gaseous atmosphere of antimony hydride heated to 400 F. to effect decomposition and plating out of antimony metal onto the copper strip. The post heat treatment is carried out at a temperature of 475 F. to produce a final coherent antimony coating on the copper metal base strip, being integrally united with the copper metal.
EXAMPLE V A steel sheet isgas plated with molybdenum metal similarly as described in Example I, and using molybdenum carbonyl in place of nickel carbonyl. A temperature of approximately 450 F. is used in the gas plating chamber.
While the foregoing examples are given to more particularly point out how the invention may be practiced, it will be understood that the invention is not to be specifically limited thereby. The essence of the invention is the provision of a' pre-treatment so as to deaerate or de-gas the metal to be gaseous plated so as to provide a perfectly dry, Water-vapor and hydrogen free metal surface for receiving the gaseous metal plating. The process provides a finished product as aforementioned, wherein the plating or metal coat is interlocked with the base metal so as to form a substantially integral metal product.
In this connection, FIGURES and 6 illustrate in enlarged section, the essential difference in structure between wet plated metal products and gaseous or dry plated metal products. As illustrated in FIGURE 5, metal coating is applied over conventional treated metal as generally indicated by the reference character 150 which is wet plated by a metal coating as indicated at 151, there is invariably a discontinuous layer or plurality of microscopic gas pockets or bubbles 152 in between the metal coating layer 151 and base metal 150. In extreme cases where these gas occlusions become large enough or continuous, the metal coating peels away from the base metal.
Referring to FIGURE 6, there is illustrated in .enlarged section a gaseous metal coated structure as prd duced in accordance with this invention. In this instance, as shown, the base metal and metal coating 156 are interlocked to provide a substantially integral structure. The microscopic pores at the surface of the metal are freed of gas occlusions and gaseous metal allowed to enter and thus penetrate into the body of the base metal, deposition of metal taking place to thus provide an interlocking of the metal coating or plating with the base metal.
The foregoing description of a method of gaseous metal plating and product obtained thereby is accordingly distinguished from conventional wet plated products and methods. Whereas the method and apparatus disclosed herein are susceptible to various changes and modifications without departing from the principle and spirit of this invention, it is intended that such modifications as are required to adapt the invention to different conditions and uses are contemplated as within the scope of the invention except as restricted in the appended claims.
This application is a continuation-in-part of my application Serial No. 439,075 filed June 24, 1954.
What is claimed is:
l. A method of producing metal articles having a layer of metal interlocked with the surface of the article by the deposition of metal from heat-decomposable metal compounds wherein the article to be plated is pretreated to clean and deaerated and moved along through a plating chamber containing a heat-decomposable gaseous metal compound, and wherein the temperature within the plating chamber is sufficient to cause decomposition of the heat-decomposable metal compound and plating out of the metal onto the article, the improvement which consists in the step of subjecting the cleaned metal article to be plated to a pre-heat and vacuum treatment to deaerate the pores of the surface of the article to remove occluded gases, and immediately thereafter subjecting the same to gaseous metal plating, and circulating said gaseous metal compound about said article in a helical shaped path to cause said metal compound to penetrate deeply into the surface of said article and diffuse in the pores and then thermally decomposed to cause the metal constituent to be deposited intosaid pores, said vacuum treatment being conducted at a temperature between about 400 to 1000" F.
2. A method of producing a metal article having a layer of metal interlocked with the base metal and forming a substantially integral body of metal, which comprises thoroughly cleaning the surface of the base metal including rinsing and air drying to remove foreign matter, heating the metal and while thus heated subjecting the same to reduced atmospheric pressure conditions to deaerate the pores of the metal surface of occluded gases, and then subjecting the resultant deaerated metal to gaseous metal deposition by intimately contacting said deaerated metal with a heat-decomposable metal compound of molybdenum and circulating said gaseous metal compound about said article in a helical shaped path to cause said metal compound to penetrate deeply into the surface of said article and diffuse in the pores and then thermally decomposed to cause deposition of the metal constituent thereof into the pores and sub-microscopic depressions of the base metal to produce a molybdenum metal plated product having integrally united layers of metal, said heating of the metal in a reduced atmosphere being conducted in the presence of non-oxidizing conditions.
3. A method of producing a metal article having a base metal and continuous layer of metal interlocked with said base metal and forming a substantially integral body of metal, said method comprising cleaning the surface of the base metal including rinsing and air drying to remove foreign matter, heating the metal and while thus heated subjecting the same to reduced atmospheric pressure conditions to deaerate the pores of the metal surface of occluded gases and produce a dry, deaerated base metal surface, subjecting the thus deaerated metal to gaseous metal deposition by contacting said deaerated metal with a heat-decomposable gaseous metal compound at a temperature suflicient to cause thermal decomposition of the gaseous metal compound and circulating said gaseous metal compound about said article in a helical shaped path to cause said metal compound to penetrate deeply into the surface of said article and dilfuse in the pores and then thermally decomposed to cause deposition of the metal constituent thereof into the pores and sub-microscopic depressions of the base metal, and thereafter heating the plated material to a temperature between about 475 F. and 700 F. to effect degassing and annealing of said plated material and produce a finished product, said last-mentioned heating being conducted in the presence of inert carbon dioxide gas.
4. A product made in accordance with the method of claim 1, wherein the 'base metal is aluminum and the outer metal layer is nickel.
5. A product made in accordance with the method of claim 1, wherein the base metal is steel and the outer metal layer is cobalt.
6. A product made in accordance with the method of 10 claim 1, wherein the base metal is copper and the outer metal layer is antimony.
7. A product made in accordance with the method of claim 1, wherein the base metal is steel and the outer metal layer is molybdenum.
References Cited in the file of this patent UNITED STATES PATENTS 2,344,138 Drummond Mar. 14, 1944 2,432,657 Colbert Dec. 16, 1947 2,602,033 Lander July 1, 1952 2,654,946 Rhodes Oct. 13, 1953 2,656,284 Toulmin Oct. 20, 1953 2,665,224 Clough Jan. 5, 1954 2,685,124 Toulmin Aug. 3, 1954 2,783,164 Hill Feb. 26, 1957 2,793,423 Stumbock May 28, 1957 2,815,299 Raymond Dec. 3, 1957 2,881,514 Drummond Apr. 14, 1959 2,887,984 Drummond May 26, 1959 FOREIGN PATENTS 758,924 Great Britain Oct. 10, 1956 570,161 Canada Feb. 3, 1959
Claims (2)
1. A METHOD OF PRODUCING METAL ARTICLES HAVING A LAYER OF METAL INTERLOCKED WITH THE SURFACE OF THE ARTICLE BY THE DEPOSITION OF METAL FROM HEAT-DECOMPOSABLE METAL COMPOUNDS WHEREIN THE ARTICLE TO BE PLATED IS PRETREATED TO CLEAN AND DEAREATED AND MOVED ALONG THROUGH A PLATING CHAMBER CONTAIING A HEAT-DECOMPOSABLE GASEOUS METAL COMPOUND, AND WHEREIN THE TEMPERATURE WITHIN THE PLATING CHAMBER IS SUFFICIENT TO CAUSE DECOMPOSITION OF THE HEAT-DECOMPOSABLE METAL COMPOUND AND PLATING OUT OF THE METAL ONTO THE ARTICLE, THE IMPROVEMENT WHICH CONSISTS IN THE STEP OF SUBJECTING THE CLEANED METAL ARTICLE TO BE PLATED TO A PRE-HEATED AND VACUUM TREATMENT TO DEAERATE THE PORES OF THE SURFACE OF THE ARTICLE TO REMOVE OCCLUDED GASES, AND IMMEDIATELY THEREAFTER SUBJECTING THE SAME TO GASEOUS METAL PLATING, AND CIRCULATING SAID GASEOUS METAL
5. A PRODUCT MADE IN ACCORDANCE WITH THE METHOD OF CLAIM 1, WHEREBY THE BASE METAL IS STEEL AND THE OUTER METAL LAYER IS COBALT.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
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US753567A US3055089A (en) | 1958-08-06 | 1958-08-06 | Gaseous metal product and processes |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
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US753567A US3055089A (en) | 1958-08-06 | 1958-08-06 | Gaseous metal product and processes |
CH6863459A CH379869A (en) | 1959-01-22 | 1959-01-22 | Process for manufacturing plated metal objects, metal object obtained by this process and installation for implementing this process |
Publications (1)
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US3055089A true US3055089A (en) | 1962-09-25 |
Family
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US753567A Expired - Lifetime US3055089A (en) | 1958-08-06 | 1958-08-06 | Gaseous metal product and processes |
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US3339588A (en) * | 1964-06-13 | 1967-09-05 | Centre Nat Rech Metall | Continuous casting mold |
US3342564A (en) * | 1965-01-22 | 1967-09-19 | Martin Metals Company | Composite castings |
US3639177A (en) * | 1969-03-27 | 1972-02-01 | Craig S Tedmon Jr | Ferrous metal substrate with dense, black glossy oxide coating and process for coating preparation |
US4042163A (en) * | 1974-08-23 | 1977-08-16 | Schladitz Hermann J | Method for the manufacture of a heat exchanger or heat transfer element |
WO2004057053A2 (en) * | 2002-12-23 | 2004-07-08 | Pirelli Pneumatici S.P.A. | Methods for producing coated metal wire |
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US20060123862A1 (en) * | 2002-12-23 | 2006-06-15 | Federico Pavan | Metal wire coated with a layer of metal material intended to reinforce elastomeric materials and methods for producing the same |
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