US2921868A - Aluminum gas plating of various substrates - Google Patents

Aluminum gas plating of various substrates Download PDF

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US2921868A
US2921868A US589976A US58997656A US2921868A US 2921868 A US2921868 A US 2921868A US 589976 A US589976 A US 589976A US 58997656 A US58997656 A US 58997656A US 2921868 A US2921868 A US 2921868A
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aluminum
plating
metal
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gas
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Berger Carl
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Union Carbide Corp
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    • CCHEMISTRY; METALLURGY
    • C23COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
    • C23CCOATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; SURFACE TREATMENT OF METALLIC MATERIAL BY DIFFUSION INTO THE SURFACE, BY CHEMICAL CONVERSION OR SUBSTITUTION; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL
    • C23C16/00Chemical coating by decomposition of gaseous compounds, without leaving reaction products of surface material in the coating, i.e. chemical vapour deposition [CVD] processes
    • C23C16/06Chemical 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
    • C23C16/18Chemical 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 metallo-organic compounds
    • C23C16/20Deposition of aluminium only
    • YGENERAL 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
    • Y10TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10TTECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
    • Y10T428/00Stock material or miscellaneous articles
    • Y10T428/12All metal or with adjacent metals
    • Y10T428/12493Composite; i.e., plural, adjacent, spatially distinct metal components [e.g., layers, joint, etc.]
    • Y10T428/12708Sn-base component
    • YGENERAL 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
    • Y10TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10TTECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
    • Y10T428/00Stock material or miscellaneous articles
    • Y10T428/12All metal or with adjacent metals
    • Y10T428/12493Composite; i.e., plural, adjacent, spatially distinct metal components [e.g., layers, joint, etc.]
    • Y10T428/12736Al-base component
    • YGENERAL 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
    • Y10TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10TTECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
    • Y10T428/00Stock material or miscellaneous articles
    • Y10T428/12All metal or with adjacent metals
    • Y10T428/12493Composite; i.e., plural, adjacent, spatially distinct metal components [e.g., layers, joint, etc.]
    • Y10T428/12771Transition metal-base component
    • Y10T428/12861Group VIII or IB metal-base component
    • Y10T428/12903Cu-base component
    • YGENERAL 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
    • Y10TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10TTECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
    • Y10T428/00Stock material or miscellaneous articles
    • Y10T428/12All metal or with adjacent metals
    • Y10T428/12493Composite; i.e., plural, adjacent, spatially distinct metal components [e.g., layers, joint, etc.]
    • Y10T428/12771Transition metal-base component
    • Y10T428/12861Group VIII or IB metal-base component
    • Y10T428/12951Fe-base component

Definitions

  • the present invention is particularly adapted for the deposition of aluminum films on substrata such as glass glass fiber rovings and the like non-metallic material as well as metal such as copper, lead, iron, steel and the like.
  • the invention is also useful in the application of aluminum metal to material such as mica, quartz, graphite and organic plastics such as nylon and similar filaments or fibers.
  • the deposition of aluminum films on natural as well as synthetic fibers or filaments may be accomplished in accordance with this invention.
  • the gas plating of light metal such as aluminum at relatively low temperatures and pressures preferably is carried out by the use of a heat-decomposable gaseous compound in the case of aluminum, making use of aluminum alkyls, for example triisobutyl aluminum, triethyl aluminum, trimethyl aluminum, or mixtures thereof.
  • a heat-decomposable gaseous compound in the case of aluminum making use of aluminum alkyls, for example triisobutyl aluminum, triethyl aluminum, trimethyl aluminum, or mixtures thereof.
  • the material to be plated with aluminum metal is placed in a chamber and the air removed and the atmosphere of the chamber filled with inert gas such as nitrogen, which is dry and free of moisture.
  • the article to be plated or aluminized is initially heated to a temperature sufiicient to cause decomposition of the aluminum compound and deposition of the aluminum metal onto the material or article to be plated.
  • Aluminum metal is thus deposited at relatively low temperatures and pressures, which distinguishes from the prior processes wherein attempts have been made to use volatilized metal and which require high temperatures on the order of 3272 F. to form aluminum metal vapor.
  • the present invention makes it possible to deposit aluminum on the surfaces of various materials, and such as will withstand the temperature used to bring about decomposition of the gaseous heat-decomposable aluminum compound. Making use of such compounds, plating of the light metal onto articles made of steel, iron, copper, magnesium, and alloy metals, as well as molded plastics, glass, wood, paper and the like, as aforementioned may be thus accomplished. Aluminum may also be plated on bearing and machine elements, hardware, cooking utensils and the like to produce products hav ing improved resistance to corrosion.
  • a metal film of one molecule thickness is provided initially which may be further increased as desired.
  • a tenacious metal layer of aluminum is formed in the surface pores of the base material on which the metal is deposited.
  • the process of the invention permits rapid deposition of light metals, e.g., aluminum at relatively low temperatures and pressures as compared to prior processes utilizing volatilized metals.
  • gas plating metal surfaces for example the metal, after being thoroughly cleaned of foreign matter, is sub- 2 jected to gas plating utilizing a suitable organo-metallie compound of aluminum and which compound is heatdecomposable at temperatures substantially below the vaporization point of the light metal.
  • the decomposition or disassociation of the gaseous metal compound is made to take place in an atmosphere which is inert to the nascent metal, being especially free of oxygen, hydrogen and Water.
  • An atmosphere in the plating chamber of dry nitrogen gas has been found suitable.
  • This inert gas also may be used as a carrier and protecting blanket for the aluminum alkyl compound.
  • gases which are inert and free of oxygen and moisture may be used in place of nitrogen, such as helium, argon, etc.
  • the material to be plated is placed in a closed chamber or container having an inlet and outlet opening. Thereafter the air and water vapor are displaced by forcing dry nitrogen through the chamber under sulficient pressure to displace the air.
  • Aluminum alkyl is then introduced into the plating chamber using nitrogen as a carrier gas and brought in contact with the heated article to be plated with aluminum.
  • suitable means such as electrical resistance coils, are provided, to heat the material to be plated to a temperature high enough to cause the gaseous metal compound, e.g., aluminum triisobutyl, to decompose and aluminum metal to deposit on the surface of the heated material.
  • gaseous metal compound e.g., aluminum triisobutyl
  • heating may be efiected by the use of infra-red lamps.
  • Nichrome resistance wires or ribbons may be wound around the plating chamber which preferably is enclosed in asbestos felt, or the like, and connected to a source of electricity to heat the chamber and material or article therein to bring about decomposition of the aluminum alkyl gaseous compound.
  • Figure 1 is a fiowsheet of the carrying out the invention.
  • FIG 2 illustrates diagrammatically suitable apparatus for plating aluminum, the elements of the apparatusbeing shown partly in section and partly broken away in the interest of clearness.
  • a stream of dry nitrogen is introduced into the system from the tank 10 and bubbled through heptane contained in the reservoir 11, the heptane being indicated as at 12.
  • a temperature of about 80120 C. is maintained in the reservoir 11 by suitable heating means.
  • the purpose of the reservoir 11 which is partially filled with normal heptane is to maintain the fluid level in the distillation container 14 constant. This requires like temperatures in the reservoir 11 and container 14 so that the evaporation rates will be substantially the same.
  • Nitrogen gas is bubbled through the reservoir 11 which is partially filled with heptane, and thence to a distillation container 14, the latter containing a solution of aluminum alkyl in heptane.
  • a solution comprising aluminum triisobutyl in normal heptane is introduced as needed into the distillation container 14 through a stopper closed neck portion 15.
  • a preferred concentration conpreferred method of sists of 25% by volume of the aluminum triisobutyl in normal heptane. Where use is made of other alkyds such as aluminum triethyl or trimethyl, or aluminum diethyl hydride, similar concentrations are preferably used.
  • Aluminum triisobutyl is introduced in a liquid state freed of all moisture and rendered chemically clean
  • the temperature of the heptane solution of aluminum triisobutyl in the distillation container 14 is kept within the range of about 90-l00 C. to avoid extensive alkyl decomposition.
  • a mixture ofaluminum alkyl and nitrogen flows from the distillation container 14 and is conducted to a plating tube '16 which is heated by an electrical resistance element 17 arranged therearound to bring about decomposition of the aluminum alkyl and deposition of aluminum. :Other suitable means may be used for heating the tube 16 if desired.
  • the material or substrate 18 is heated in the tube 16 to approximately 250500 C.
  • aluminurn alkyl plating gas but preferably is-in the neighborhood of 300 C. when using aluminum triisobutyl. This temperature produces a smooth, lustrous gas plated surface of aluminum. With the use of higher temperatures there is a tendency to produce a darker colored plating. On the other hand, at lower temperatures decomposition characteristics of aluminum alkyl are not favorable.
  • Residual heptane and alkyl degradation products formed during the plating process are recovered by the bubbler trap 20.
  • Nitrogen gas and other volatile compounds. pass out through the exit 21 at the top of the bubbler 20 as indicated by the arrow on Figure 2.
  • the exit velocity of the gas is maintained at approximately 0.01. to 1.0 liter per minute, the particular velocity depending upon the'rate of plating desired.
  • the plating tube 16 is enclosed in an oven or heating chamber 23 which is suitably heated by electrical resistance elements and controlled by a .rheostat such as indicated at 24.
  • the reservoir 11 and distillation container 14 are likewise heated by the heating elements 25 and 26, the same being controlled through a rheostat means 29.
  • the surface of the material to be plated with aluminum is initially cleaned of foreign matter and dried to remove moisture. Manual or chemical cleaning means or a suitable combination thereof may be employed for this purpose. Sandblasting, wire brushing or the like are suitable methods to remove solid foreign matter from metal surfaces. Wherethe surface is to be de-greased and cleaned, the same may be washed with petroleum solvent, such as xylol, toluol or the like, and all traces of moisture are removed by heating the material at 250to 300 C. for a time sufiicient to drive ofi any residual moisture.
  • petroleum solvent such as xylol, toluol or the like
  • an organo-aluminum compound e.g., aluminum alkyls such as aluminum triisobutyl is introduced and the gaseous aluminum alkyl brought in contact with the surface of the heated article, the temperature of the latter being high enough to cause the gaseous aluminum alkyl compound coming in contact therewith to decompose or disassociate and deposit aluminum metal onto After a desired thickness of aluminum deposit is obtained, the process is stopped and excess aluminum alkyl returned to storage.
  • Triisobutyl aluminum is supplied in steel pressure bottles, with brass valves.
  • the pressure bottle which is fitted'with a rubber dam is packed to a maximum of 60% of the free volume with triisobutyl aluminum liquid, and the remaining space is pressured to a maximum of 30 pounds/sq. in. gauge with nitrogen.
  • the bottle isprovided with an adapter valve-and tube outlet connection to allow theinternal pressure to push out -the liquid when the bottle is inverted -Fittings.
  • shouldbeopened under a blanket of .for aluminum triisobutyl is kept below 60 nitrogen and receiving containers should be dry and previously flushed with dry nitrogen.
  • a plating of aluminum was deposited upon the glass filaments in the form of a thin film.
  • Example 11 Aluminum plate was deposited on nylon fibers using aluminum triisobutyl heptane solution is in Example I.
  • Example IV V A coating of aluminum was formed on a mica substrate as a thin film to produce an aluminum plated article and as described in Example I.
  • Example V Aluminum plate was deposited on a copper disc using aluminum triethyl dissolved in heptane and as described in Example I.
  • Example V1 aluminum was deposited on a copper disc A plating of diethyl hydride dissolved in heptane as using aluminum in Example I.
  • the minimum flow rate of gas is governed by whether or not the fumes of aluminum alkyl reach and surround the hot metal or article to be plated. If the flow rate is too slow, the fumes either condense on the walls of the connecting tubes of the apparatus or else a heavy layer of white fumes accumulates inthe lower half of the tube and the base metal is covered only partially. Too rapid gas flow carries undecomposed aluminum alkyl out of the plating chamber which, of course, is undesirable. Also too rapid flow rate lowers the temperature inside the plating chamber and break down of the aluminum alkyl tends to occur.
  • the optimum rate of flow has been found to be one that will carry the aluminum alkyl into the decomposition tube or plating chamber without condensation, and which will disperse it over the whole cross section of the plating chamberso as to fill the chamber uniformly.
  • the flow rate in each instance was maintained high enough to keep the tube filled with aluminum alkyl fumes whereby a substantially uniform even deposit of aluminum is formed on the article being plated.
  • the rate of gas flow through the apparatus is thus adjusted whereby it is just enough to keep-the tube or plating chamber filled with aluminum alkyl fumes.
  • the flow sheet in Figure 1 illustrates the coordinated steps of the process using aluminum triisobutyl in heptanewith nitrogen gas as a carrier.
  • the inert gas is used both as a carrier for the aluminum alkyl and to 'move the volatilized heatdecomposable aluminum compound through the plating chamber. Use of vacuum pumps is thus unnecessary which lowers the cost of operating the process.
  • the minimum temperature that will vaporize aluminum triisobutyl at a significant rate under one atmosphere pressure has been observed to be about 90 C.
  • the density of triisobutyl aluminum at 20 C. is 0.8.
  • temperatures of 115 to 120 C. its rate of decomposition is relatively slow so that as a result much of the aluminum alkyl vapor remains undecomposed at this temperature. It has been found by test runs, however, that temperatures between 275 C. and 325 C. give good decomposition of the aluminum alkyl and quality deposits of aluminum.
  • the aluminum deposit on copper metal is of dark bluish color, and a. clear reflecting mirror is formed on the inside of a glass tube used as a plating chamber. When the plating temperature was raised to 400 C., the mirror-like deposit formed was observed to be dark in color and not as good as where a lower temperature was used.
  • the plating materials when of metal substratum may be subjected to an annealing heat treatment after the plating operation to stabilize the metal deposit.
  • a heat treatment may consist of heating the plated article up to 400 C. for one hour.
  • the invention provides a process for plating aluminum metal directly on the surface of articles whereby there" is produced a composite product comprising an outer layer of aluminum or light metal intricately and tenaciously bonded thereto.
  • the thickness of the light metal coating may be controlled by varying the time the metal bearing gas is in contact with the heated material to be plated.
  • a coating of one molecule thickness up to one or more thousandths of an inch may be effected utilizing the process of the invention to thus provide a protective coating of aluminum on various metal surfaces or the like, the invention being especially useful to overcome corrosion problems.
  • the process further makes possible the continuous straight line production of composite products; and long length strips or sheets of material, e.g., such as used in the making of screens and the like which may be gas plated with aluminum.
  • the invention is particularly useful in aluminizing metals where it is desired that aluminum be deposited into the pores and interstices of the base metal surface to form a substantially integral outer shell of the corrosion resistant light metal.
  • Preheating and drying of the article prior to gas plating preferably is carried out in an inert atmosphere such as nitrogen gas, helium and the like to prevent oxidation. Thereafter the heated and completely dry moisture free article is subjected to gas plating with gaseous aluminum triisobutyl as described.
  • the aluminized metal articles, as plated, are free of oxides, but upon its removal from the plating chamber and subjection to the surrounding atmosphere, an outer coating of aluminum oxide is immediately formed. This, however, does not detract from the process inasmuch as this oxide film on aluminum metal functions to protect the same as is well known.
  • a method of gas plating materials with aluminum metal comprising the steps of arranging the materials to be plated in an enclosure, removing the air from said enclosure and replacing the same with inert gas pre-washed with liquid hydrocarbon the improvement which comprises, introducing a gaseous aluminum organo compound into said enclosure and in contact with the material to be plated with aluminum, and heating the enclosure and material retained therein to a temperature sulficient to cause thermal decomposition of said gaseous aluminum compound and deposition of aluminum metal onto said material.
  • the improvement which comprises the steps of arranging the materials to be plated in an enclosure, removing the air from said enclosure and replacing the same with inert gas pre-washed with liquid hydrocarbon the improvement which comprises, introducing a gaseous aluminum alkyl compound into said enclosure and into contact with material to be plated with aluminum arranged therein, and heating the enclosure and material retained therein to a temperature sufficient to cause decomposition of said gaseous aluminum alkyl compound and deposition of aluminum onto said material, said aluminum alkyl compound being selected from the group consisting of aluminum triisobutyl, aluminum triethyl and aluminum diethyl hydride.

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Description

Jan. 19, 1960 c. BERGER ALUMINUM GAS PLATING OF VARIOUS SUBSTRATES Filed June 7, 1956 Nz lll Attorneys United States Patent ALUMINUM GAS PLATING OF VARIOUS SUBSTRATES Carl Berger, Dayton, Ohio, assignor, by mesne assignments, to Union Carbide Corporation, New York, N.Y., a corporation of New York Application J1me 7, 1956, Serial No. 589,976 3 Claims. 01. 117-107 This invention relates to gas plating of aluminum and to composite bodies produced thereby.
The present invention is particularly adapted for the deposition of aluminum films on substrata such as glass glass fiber rovings and the like non-metallic material as well as metal such as copper, lead, iron, steel and the like.
The invention is also useful in the application of aluminum metal to material such as mica, quartz, graphite and organic plastics such as nylon and similar filaments or fibers. The deposition of aluminum films on natural as well as synthetic fibers or filaments may be accomplished in accordance with this invention.
The gas plating of light metal such as aluminum at relatively low temperatures and pressures, in accordance with this invention, preferably is carried out by the use of a heat-decomposable gaseous compound in the case of aluminum, making use of aluminum alkyls, for example triisobutyl aluminum, triethyl aluminum, trimethyl aluminum, or mixtures thereof. The material to be plated with aluminum metal is placed in a chamber and the air removed and the atmosphere of the chamber filled with inert gas such as nitrogen, which is dry and free of moisture.
The article to be plated or aluminized is initially heated to a temperature sufiicient to cause decomposition of the aluminum compound and deposition of the aluminum metal onto the material or article to be plated. Aluminum metal is thus deposited at relatively low temperatures and pressures, which distinguishes from the prior processes wherein attempts have been made to use volatilized metal and which require high temperatures on the order of 3272 F. to form aluminum metal vapor.
The present invention makes it possible to deposit aluminum on the surfaces of various materials, and such as will withstand the temperature used to bring about decomposition of the gaseous heat-decomposable aluminum compound. Making use of such compounds, plating of the light metal onto articles made of steel, iron, copper, magnesium, and alloy metals, as well as molded plastics, glass, wood, paper and the like, as aforementioned may be thus accomplished. Aluminum may also be plated on bearing and machine elements, hardware, cooking utensils and the like to produce products hav ing improved resistance to corrosion.
Due to the nascent physical state of the aluminum metal, the same being deposited as it is liberated from the gaseous compound, a metal film of one molecule thickness is provided initially which may be further increased as desired. Thus a tenacious metal layer of aluminum is formed in the surface pores of the base material on which the metal is deposited.
The process of the invention permits rapid deposition of light metals, e.g., aluminum at relatively low temperatures and pressures as compared to prior processes utilizing volatilized metals.
In gas plating metal surfaces, for example the metal, after being thoroughly cleaned of foreign matter, is sub- 2 jected to gas plating utilizing a suitable organo-metallie compound of aluminum and which compound is heatdecomposable at temperatures substantially below the vaporization point of the light metal. The decomposition or disassociation of the gaseous metal compound is made to take place in an atmosphere which is inert to the nascent metal, being especially free of oxygen, hydrogen and Water. An atmosphere in the plating chamber of dry nitrogen gas has been found suitable. This inert gas also may be used as a carrier and protecting blanket for the aluminum alkyl compound. Other gases which are inert and free of oxygen and moisture may be used in place of nitrogen, such as helium, argon, etc.
In carrying out the aluminum metal plating in accordance with the preferred practice of this invention, the material to be plated is placed in a closed chamber or container having an inlet and outlet opening. Thereafter the air and water vapor are displaced by forcing dry nitrogen through the chamber under sulficient pressure to displace the air. Aluminum alkyl is then introduced into the plating chamber using nitrogen as a carrier gas and brought in contact with the heated article to be plated with aluminum.
To bring about decomposition of the aluminum alkyl after the same is introduced into the plating chamber, suitable means, such as electrical resistance coils, are provided, to heat the material to be plated to a temperature high enough to cause the gaseous metal compound, e.g., aluminum triisobutyl, to decompose and aluminum metal to deposit on the surface of the heated material. Where the plating chamber is made of glass or plastic material which will transmit infra-red rays, heating may be efiected by the use of infra-red lamps. Utilizing resistance heater coils, Nichrome resistance wires or ribbons may be wound around the plating chamber which preferably is enclosed in asbestos felt, or the like, and connected to a source of electricity to heat the chamber and material or article therein to bring about decomposition of the aluminum alkyl gaseous compound.
The drawing accompanying this application illustrates a flowsheet of the process and apparatus for carrying out the gas plating of aluminum.
Figure 1 is a fiowsheet of the carrying out the invention.
Figure 2 illustrates diagrammatically suitable apparatus for plating aluminum, the elements of the apparatusbeing shown partly in section and partly broken away in the interest of clearness.
Referring to the drawings, and more particularly to Figure 2, a stream of dry nitrogen is introduced into the system from the tank 10 and bubbled through heptane contained in the reservoir 11, the heptane being indicated as at 12. A temperature of about 80120 C. is maintained in the reservoir 11 by suitable heating means. The purpose of the reservoir 11 which is partially filled with normal heptane is to maintain the fluid level in the distillation container 14 constant. This requires like temperatures in the reservoir 11 and container 14 so that the evaporation rates will be substantially the same.
Nitrogen gas is bubbled through the reservoir 11 which is partially filled with heptane, and thence to a distillation container 14, the latter containing a solution of aluminum alkyl in heptane. A solution comprising aluminum triisobutyl in normal heptane is introduced as needed into the distillation container 14 through a stopper closed neck portion 15. A preferred concentration conpreferred method of sists of 25% by volume of the aluminum triisobutyl in normal heptane. Where use is made of other alkyds such as aluminum triethyl or trimethyl, or aluminum diethyl hydride, similar concentrations are preferably used.
Aluminum triisobutyl is introduced in a liquid state freed of all moisture and rendered chemically clean,
7 the surface of the article.
from a pressurized bottle. It begins to decompose when distilled above 90 C. at one atmosphere. The temperature of the heptane solution of aluminum triisobutyl in the distillation container 14 is kept within the range of about 90-l00 C. to avoid extensive alkyl decomposition. A mixture ofaluminum alkyl and nitrogen flows from the distillation container 14 and is conducted to a plating tube '16 which is heated by an electrical resistance element 17 arranged therearound to bring about decomposition of the aluminum alkyl and deposition of aluminum. :Other suitable means may be used for heating the tube 16 if desired. The material or substrate 18 is heated in the tube 16 to approximately 250500 C. depending upon the substrate and aluminurn alkyl plating gas but preferably is-in the neighborhood of 300 C. when using aluminum triisobutyl. This temperature produces a smooth, lustrous gas plated surface of aluminum. With the use of higher temperatures there is a tendency to produce a darker colored plating. On the other hand, at lower temperatures decomposition characteristics of aluminum alkyl are not favorable. Y
., Residual heptane and alkyl degradation products formed during the plating process are recovered by the bubbler trap 20. Nitrogen gas and other volatile compounds. pass out through the exit 21 at the top of the bubbler 20 as indicated by the arrow on Figure 2. The exit velocity of the gas is maintained at approximately 0.01. to 1.0 liter per minute, the particular velocity depending upon the'rate of plating desired.
The plating tube 16 is enclosed in an oven or heating chamber 23 which is suitably heated by electrical resistance elements and controlled by a .rheostat such as indicated at 24. The reservoir 11 and distillation container 14 are likewise heated by the heating elements 25 and 26, the same being controlled through a rheostat means 29.
The surface of the material to be plated with aluminum is initially cleaned of foreign matter and dried to remove moisture. Manual or chemical cleaning means or a suitable combination thereof may be employed for this purpose. Sandblasting, wire brushing or the like are suitable methods to remove solid foreign matter from metal surfaces. Wherethe surface is to be de-greased and cleaned, the same may be washed with petroleum solvent, such as xylol, toluol or the like, and all traces of moisture are removed by heating the material at 250to 300 C. for a time sufiicient to drive ofi any residual moisture. "After the article has been cleaned thoroughly and the same, while retained'out of contact with air or moisture, is introduced into the plating chamber which is maintained filled with inert gas such as nitrogen, helium or argon, and the article heated asdescribed. While the article is heated in the plating chamber under an atmosphere of nitrogen, an organo-aluminum compound, e.g., aluminum alkyls such as aluminum triisobutyl is introduced and the gaseous aluminum alkyl brought in contact with the surface of the heated article, the temperature of the latter being high enough to cause the gaseous aluminum alkyl compound coming in contact therewith to decompose or disassociate and deposit aluminum metal onto After a desired thickness of aluminum deposit is obtained, the process is stopped and excess aluminum alkyl returned to storage.
Triisobutyl aluminum is supplied in steel pressure bottles, with brass valves. The pressure bottle which is fitted'with a rubber dam is packed to a maximum of 60% of the free volume with triisobutyl aluminum liquid, and the remaining space is pressured to a maximum of 30 pounds/sq. in. gauge with nitrogen. To remove the contents, the bottle isprovided with an adapter valve-and tube outlet connection to allow theinternal pressure to push out -the liquid when the bottle is inverted -Fittings. shouldbeopened under a blanket of .for aluminum triisobutyl is kept below 60 nitrogen and receiving containers should be dry and previously flushed with dry nitrogen. Storage temperatures C. and preferably 0 C. to'10 C.
The following examples illustrate typical runs of gas plating with aluminum using different substrates.
Example I 7 Glass rovings in the form of filaments were gas plated with aluminum and employing a solution of normal heptane containing 25% by volume of aluminum triisobutyl. The temperature and rate of flow were as follows- C. Reservoir 11 95 Distillation container 14 93 Plating tube 300 Substrate v 300 Flow 'rate=0.1 literper minute.
A plating of aluminum was deposited upon the glass filaments in the form of a thin film.
Example 11 Aluminum plate was deposited on nylon fibers using aluminum triisobutyl heptane solution is in Example I.
Example IV V A coating of aluminum was formed on a mica substrate as a thin film to produce an aluminum plated article and as described in Example I.
Example V Aluminum plate was deposited on a copper disc using aluminum triethyl dissolved in heptane and as described in Example I.
Example V1 aluminum was deposited on a copper disc A plating of diethyl hydride dissolved in heptane as using aluminum in Example I.
The minimum flow rate of gas is governed by whether or not the fumes of aluminum alkyl reach and surround the hot metal or article to be plated. If the flow rate is too slow, the fumes either condense on the walls of the connecting tubes of the apparatus or else a heavy layer of white fumes accumulates inthe lower half of the tube and the base metal is covered only partially. Too rapid gas flow carries undecomposed aluminum alkyl out of the plating chamber which, of course, is undesirable. Also too rapid flow rate lowers the temperature inside the plating chamber and break down of the aluminum alkyl tends to occur.
The optimum rate of flow has been found to be one that will carry the aluminum alkyl into the decomposition tube or plating chamber without condensation, and which will disperse it over the whole cross section of the plating chamberso as to fill the chamber uniformly. The flow rate in each instance was maintained high enough to keep the tube filled with aluminum alkyl fumes whereby a substantially uniform even deposit of aluminum is formed on the article being plated. The rate of gas flow through the apparatus is thus adjusted whereby it is just enough to keep-the tube or plating chamber filled with aluminum alkyl fumes. The flow sheet in Figure 1 illustrates the coordinated steps of the process using aluminum triisobutyl in heptanewith nitrogen gas as a carrier. The inert gas is used both as a carrier for the aluminum alkyl and to 'move the volatilized heatdecomposable aluminum compound through the plating chamber. Use of vacuum pumps is thus unnecessary which lowers the cost of operating the process.
The minimum temperature that will vaporize aluminum triisobutyl at a significant rate under one atmosphere pressure has been observed to be about 90 C. The density of triisobutyl aluminum at 20 C. is 0.8. At temperatures of 115 to 120 C. its rate of decomposition is relatively slow so that as a result much of the aluminum alkyl vapor remains undecomposed at this temperature. It has been found by test runs, however, that temperatures between 275 C. and 325 C. give good decomposition of the aluminum alkyl and quality deposits of aluminum. At 350 C. the aluminum deposit on copper metal is of dark bluish color, and a. clear reflecting mirror is formed on the inside of a glass tube used as a plating chamber. When the plating temperature was raised to 400 C., the mirror-like deposit formed was observed to be dark in color and not as good as where a lower temperature was used.
The plating materials when of metal substratum, if desired, may be subjected to an annealing heat treatment after the plating operation to stabilize the metal deposit. Such a heat treatment may consist of heating the plated article up to 400 C. for one hour.
The invention provides a process for plating aluminum metal directly on the surface of articles whereby there" is produced a composite product comprising an outer layer of aluminum or light metal intricately and tenaciously bonded thereto.
The thickness of the light metal coating may be controlled by varying the time the metal bearing gas is in contact with the heated material to be plated. A coating of one molecule thickness up to one or more thousandths of an inch may be effected utilizing the process of the invention to thus provide a protective coating of aluminum on various metal surfaces or the like, the invention being especially useful to overcome corrosion problems.
The process further makes possible the continuous straight line production of composite products; and long length strips or sheets of material, e.g., such as used in the making of screens and the like which may be gas plated with aluminum. The invention is particularly useful in aluminizing metals where it is desired that aluminum be deposited into the pores and interstices of the base metal surface to form a substantially integral outer shell of the corrosion resistant light metal.
Preheating and drying of the article prior to gas plating preferably is carried out in an inert atmosphere such as nitrogen gas, helium and the like to prevent oxidation. Thereafter the heated and completely dry moisture free article is subjected to gas plating with gaseous aluminum triisobutyl as described.
The aluminized metal articles, as plated, are free of oxides, but upon its removal from the plating chamber and subjection to the surrounding atmosphere, an outer coating of aluminum oxide is immediately formed. This, however, does not detract from the process inasmuch as this oxide film on aluminum metal functions to protect the same as is well known.
It will be understood that while there has been described and set forth certain specific embodiments of this invention, it is not intended that the invention be thus limited thereto and it is manifest that various substitutions and changes may be made by those skilled in the art and to which the invention is readily susceptible without departing from the spirit and scope of this disclosure and as more particularly set forth in the appended claims.
What is claimed is:
1. In a method of gas plating materials with aluminum metal, the improvement which comprises the steps of arranging the materials to be plated in an enclosure, removing the air from said enclosure and replacing the same with inert gas pre-washed with liquid hydrocarbon the improvement which comprises, introducing a gaseous aluminum organo compound into said enclosure and in contact with the material to be plated with aluminum, and heating the enclosure and material retained therein to a temperature sulficient to cause thermal decomposition of said gaseous aluminum compound and deposition of aluminum metal onto said material.
2. In a method of gas plating materials with aluminum metal, the improvement which comprises the steps of arranging the materials to be plated in an enclosure, removing the air from said enclosure and replacing the same with inert gas pre-washed with liquid hydrocarbon the improvement which comprises, introducing a gaseous aluminum alkyl compound into said enclosure and into contact with material to be plated with aluminum arranged therein, and heating the enclosure and material retained therein to a temperature sufficient to cause decomposition of said gaseous aluminum alkyl compound and deposition of aluminum onto said material, said aluminum alkyl compound being selected from the group consisting of aluminum triisobutyl, aluminum triethyl and aluminum diethyl hydride.
3. As an article of manufacture, an article plated with aluminum metal in accordance with the process of claim 1.
References Cited in the file of this patent UNITED STATES PATENTS 2,516,058 Lander July 18, 1950 2,656,284 Toulmin Oct. 20, 1953 2,694,651 Pawlyk Nov. 16, 1954 2,711,973 Wainer et al. June 28, 1955 2,749,255 Nack et al. June 5, 1956 2,759,855 Medcalf et al. Aug. 21, 1956 2,847,320 Bullofi Aug. 12, 1958 FOREIGN PATENTS 633,701 Great Britain Dec. 19, 1949 OTHER REFERENCES The Journal of Chemical Physics, Yeddanapalli et al., vol. 14, No. 1, January 1946, pp. l-7.

Claims (1)

1. IN A METHOD OF GAS PLATING MATERIALS WITH ALUMINUM METAL, THE IMPROVEMENT WHIC COMPRISES THE STEPS OF ARRANGING THE MATERIALS TO BE PLATED IN AN ENCLOSURE, REMOVING THE AIR FROM SAID ENCLOSURE AND REPLACING THE SAME WITH INERT GAS PRE-WASHED WITH LIQUID HYDROCARBON THE IMPROVEMENT WHICH COMPRISES, INTRODUCING A GASEOUS ALUMINUM ORGANO COMPOUND INTO SAID ENCLOSURE AND IN CONTACT WITH THE MATERIAL TO BE PLATED WITH ALUMINUM, AND HEATING THE ENCLOSURE AND MATERIAL RETAINED THEREIN TO A TEMPERATURE SUFFICIENT TO CAUSE THERMAL DECOMPOSITION OF SAID GASEOUS ALUMINUM COMPOUND AND DEPOSITION OF ALUMINUM METAL ONTO SAID MATERIAL.
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US3028261A (en) * 1958-04-24 1962-04-03 Chromalloy Corp Chromizing metals
US3194824A (en) * 1961-12-11 1965-07-13 Ethyl Corp Preparation of cyclopentadienyl group vb metal tetracarbonyls
US3202537A (en) * 1962-05-01 1965-08-24 Ethyl Corp Method of metal plating by fluidized bed
US3288829A (en) * 1961-01-19 1966-11-29 Ethyl Corp Process for preparing cyclopentadienyl group vb and vib metal hydrides
US3376173A (en) * 1960-05-02 1968-04-02 Ethyl Corp Encapsulation of light metal hydrides as rocket propellants
US3449144A (en) * 1965-09-29 1969-06-10 Continental Oil Co Method of aluminum plating with diethylaluminum hydride
US3511703A (en) * 1963-09-20 1970-05-12 Motorola Inc Method for depositing mixed oxide films containing aluminum oxide
US3969555A (en) * 1972-03-30 1976-07-13 The Dow Chemical Company Aluminum plating corrosion resistance
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FR2426745A1 (en) * 1978-05-25 1979-12-21 Itt METAL COATING PROCESS BY DEPOSIT IN THE FORM OF VAPORS, FOR THE FORMATION OF CONDUCTIVE TRAILS ON A SEMICONDUCTOR BODY
FR2426743A1 (en) * 1978-05-25 1979-12-21 Itt METHOD AND DEVICE FOR METAL COATING BY DEPOSIT IN THE FORM OF VAPORS
US4433012A (en) * 1980-07-10 1984-02-21 Itt Industries, Inc. Process for the pyrolytic deposition of aluminum from TIBA
EP0349044A2 (en) * 1988-07-01 1990-01-03 Centre De Recherche Et De Promotion Du Magnesium C E P R O M A G Process for the production of a protective film on a magnesium-based substrate, application to the protection of magnesium alloys, substrates thus obtained
US20030168088A1 (en) * 2001-12-04 2003-09-11 Kaori Watanabe Chemical solution treatment apparatus for semiconductor substrate

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US2516058A (en) * 1943-09-30 1950-07-18 Bell Telephone Labor Inc Apparatus for plating of metals
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US2711973A (en) * 1949-06-10 1955-06-28 Thompson Prod Inc Vapor phase coating of molybdenum articles
US2749255A (en) * 1952-05-24 1956-06-05 Ohio Commw Eng Co Method of producing metalized glass fiber rovings
US2759855A (en) * 1953-08-24 1956-08-21 Eagle Picher Co Coated electronic device and method of making same
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US2516058A (en) * 1943-09-30 1950-07-18 Bell Telephone Labor Inc Apparatus for plating of metals
GB633701A (en) * 1946-10-22 1949-12-19 Metal Gas Company Ltd Improvements in and relating to the coating of metals and alloys with metals
US2711973A (en) * 1949-06-10 1955-06-28 Thompson Prod Inc Vapor phase coating of molybdenum articles
US2656284A (en) * 1949-09-07 1953-10-20 Ohio Commw Eng Co Method of plating rolled sheet metal
US2694651A (en) * 1951-10-08 1954-11-16 Ohio Commw Eng Co Deposition of copper oxides on heat insulating material
US2749255A (en) * 1952-05-24 1956-06-05 Ohio Commw Eng Co Method of producing metalized glass fiber rovings
US2759855A (en) * 1953-08-24 1956-08-21 Eagle Picher Co Coated electronic device and method of making same
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Cited By (16)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3028261A (en) * 1958-04-24 1962-04-03 Chromalloy Corp Chromizing metals
US3376173A (en) * 1960-05-02 1968-04-02 Ethyl Corp Encapsulation of light metal hydrides as rocket propellants
US3288829A (en) * 1961-01-19 1966-11-29 Ethyl Corp Process for preparing cyclopentadienyl group vb and vib metal hydrides
US3194824A (en) * 1961-12-11 1965-07-13 Ethyl Corp Preparation of cyclopentadienyl group vb metal tetracarbonyls
US3202537A (en) * 1962-05-01 1965-08-24 Ethyl Corp Method of metal plating by fluidized bed
US3511703A (en) * 1963-09-20 1970-05-12 Motorola Inc Method for depositing mixed oxide films containing aluminum oxide
US3449144A (en) * 1965-09-29 1969-06-10 Continental Oil Co Method of aluminum plating with diethylaluminum hydride
US3969555A (en) * 1972-03-30 1976-07-13 The Dow Chemical Company Aluminum plating corrosion resistance
DE2920384A1 (en) * 1978-05-25 1979-11-29 Itt Ind Gmbh Deutsche Aluminium coating or conductive trace prodn. - by thermal decomposition of tri:isobutyl aluminium, e.g. on semiconductor substrate
FR2426745A1 (en) * 1978-05-25 1979-12-21 Itt METAL COATING PROCESS BY DEPOSIT IN THE FORM OF VAPORS, FOR THE FORMATION OF CONDUCTIVE TRAILS ON A SEMICONDUCTOR BODY
FR2426743A1 (en) * 1978-05-25 1979-12-21 Itt METHOD AND DEVICE FOR METAL COATING BY DEPOSIT IN THE FORM OF VAPORS
US4433012A (en) * 1980-07-10 1984-02-21 Itt Industries, Inc. Process for the pyrolytic deposition of aluminum from TIBA
EP0349044A2 (en) * 1988-07-01 1990-01-03 Centre De Recherche Et De Promotion Du Magnesium C E P R O M A G Process for the production of a protective film on a magnesium-based substrate, application to the protection of magnesium alloys, substrates thus obtained
EP0349044A3 (en) * 1988-07-01 1990-03-07 Cepromag Ct Rech Promo Magnes Process for the production of a protective film on a magnesium-based substrate, application to the protection of magnesium alloys, substrates thus obtained
US20030168088A1 (en) * 2001-12-04 2003-09-11 Kaori Watanabe Chemical solution treatment apparatus for semiconductor substrate
US6877518B2 (en) * 2001-12-04 2005-04-12 Nec Electronics Corporation Chemical solution treatment apparatus for semiconductor substrate

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