US2523461A - Plating with metal carbonyl - Google Patents

Plating with metal carbonyl Download PDF

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US2523461A
US2523461A US654818A US65481846A US2523461A US 2523461 A US2523461 A US 2523461A US 654818 A US654818 A US 654818A US 65481846 A US65481846 A US 65481846A US 2523461 A US2523461 A US 2523461A
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carbonyl
metal
coating
nickel
plating
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John T Young
Olindo R Angelillo
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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
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01CRESISTORS
    • H01C17/00Apparatus or processes specially adapted for manufacturing resistors
    • H01C17/06Apparatus or processes specially adapted for manufacturing resistors adapted for coating resistive material on a base
    • H01C17/20Apparatus or processes specially adapted for manufacturing resistors adapted for coating resistive material on a base by pyrolytic processes

Definitions

  • This invention relates to methods for plating or coating various surfaces with metalsand more particularly relates to coating metal surfaces.
  • One of the important Objects of the invention is to provide a non-porous, continuous coating of metal capable of sealing the capillary channels along the boundaries of the metal grains which make up the surface of the metal body being plated. This object has been attained with carbonyl solutions.
  • a further object of the invention is to provide a process for applying continuous metal coatings of such tenuity that they may be used for plating precision instruments and the like without afiecting the dimensional tolerances permitted, such coatings -atthe same time being uniform and providing complete protection against corrosion.
  • a further object is to provide a process for the coating of metals and other objects with thin metal layers which will not check 'or crack in subsequent use and which at the same time will be so tenaciously bonded to the surface of the articles that such coatings cannot be caused to separate.
  • metal surfaces such as iron, brass and the like, are provided with very thin protective nickel coatings by employing appropriate solutions of nickel carbonyl.
  • Suitable solvents are hydrocarbons which are normally volatile, and therefore not capable of interfering with the plating operation.
  • hydrocarbons which are normally volatile, and therefore not capable of interfering with the plating operation.
  • benzol, toluol, hexane, octane, sulphurfree gasoline and kerosene, and kindred aromatic and aliphatic hydrocarbons may be employed.
  • hydrocarbons of oily nature which are relatively non-volatile will so coat the surfaces of the articles being plated as to prevent deposition of metal upon such surfaces and may not be used.
  • solvents may not be employed having boiling points above about 450 F.
  • the carbonylto be employed according to this invention is preferably nickel :carbonyl .NiQCOM.
  • the coating or plating operation is accomplished by emp loying an indicated solution of nickel carbonyl, as distinguished from nickel carbonyl in gaseous or vapor form, the temperature of the liquid being held at or below about 80 F. for best results.
  • the solution temperature may be about 100 F. or as low as 20 F.
  • the article to be coated is heated preferably to a temperature of around 500 F2, or between about 500 F. and 575 F., and is then quickly dipped into the carbonyl solution, the
  • the article must be heated at least to 450 F.
  • the practical upper temperature limit to which the article may be raised is about 575 F.
  • the apparent absolute upper limit is 625 F., beyond which decomposition appears to be of such nature that proper coating cannot be obtained.
  • the time interval for dipping will vary according to the temperature to which the article is heated and to its size. For example, the time may be from a half second for an object weighing 15 grams to 5 seconds for an object weighing 1000 grams, and correspondingly greater times for heavier articles.
  • the coating phenomenon involves decomposition of the carbonyl, that is the carbonyl radical separates from the nickel so that the nickel deposits upon the article being coated.
  • the coating action is not a. straight line action like that of electroplating, but the nickel moves in all directions and deposits uniformly on all faces. As a consequence, this method of coating is highly satisfactory for plating threaded and other irregular surfaces where a coating of absolutely uniform thickness is required.
  • temperatures within the limits stated is a critical factor, and that time is also an important factor in so far as it concerns maintenance of temperatures within the indicated limits.
  • Heating of the articles to be coated may be accomplished in any manner appropriate for the particular operation. Such may be oven heating, induction heating by electric coils, or otherwise as desired.
  • inert atmosphere which is inert under the operating conditions and from which all oxygen and water vapor are excluded, as well as sulphur, chlorine, and other reactants.
  • inert atmospheres are those represented by nitrogen, helium and carbon dioxide.
  • Carbon dioxide is preferred because it is heavier than air and easy to supply.
  • Carbon monoxide liberated by the decomposition of the carbonyl passes into the inert gaseous blanket which in practice is confined, the carbon monoxide being recovered therefrom for the preparation of additional nickel carbonyl.
  • the equivalent of the inert atmosphere may be used, such as pure benzol, kerosene or even water, or a solution containing a deoxidizing agent, such as sodium sulfite, pyrogallic acid, or the like, the
  • the individual coatings produced by the method of this invention are continuous and'of uniform thickness in the order of a few millionths of an inch, or perhaps between about 0.00001 and .000001 inch. Such a coating may represent for example the application of 0.03
  • the present process provides coatings so thin that they do not interfere with the tolerances required in the production of precision instruments. It is further apparent that the characteristic of the process by which the metal coating is uniformly applied regardless of surface irregularities, as contrasted with uneven applications on irregular surfaces by electroplating, isof much importance. Whe1 je increased thickness is required, dippings may be repeated, each successive layer being applied in uniform thickness so that the ultimate coating is uniformly thick.
  • These coatings individually comparable in some respects with molecular layers, thus permit the building of multiple layers to any desired degree in order to insure protection against corrosion without in any way producing undue thickness or overstepping permissible tolerances.
  • Nickel carbonyl for the deposition of nickel coatings of extreme thinness is of great importance, especially from the standpoint of corrosion, inasmuch as pure nickel coatings are of very low porosity.
  • nickel is superior even to chromium and apparently to all other metals and therefore best for this particular purpose.
  • the value of the metal whose carbonyl is employed lies fundamentally in its own porosity. The less porous and more continuous the metal coating, the greater its value in preventing corrosion. Nickel which has been deposited from nickel carbonyl r is considerably more resistant to corrosion than nickel deposited by any other means, this being due probably to higher purity.
  • solutions of other metal carbonyls in appropriate solvents such as the indicated hydrocarbon solvents.
  • These carbonyls might be represented by chromium and tungsten carbonyls, and possibly by molybdenum carbonyl, all of these normally being solids and soluble in appropriate organic solvents.
  • solutions of only very low concentrations need be employed e. g. from about 1% to as low as 0.001% of the metal carbonyl, however, higher concentrations may be used if desired, for example l Inasmuch as the activity of the metal increases asconcentration decreases, coating efficiency is maintained even after the concentration has been lowered to relatively insignificant percentages by repeated dippings.
  • a further advantageous feature which we have discovered is that with a carbonyl such as nickel carbonyl, very low temperatures of the carbonyl solutions are desirable especially where thick coatings are desired.
  • a solution of nickel carbonyl in toluene may be used at 0 F. or as low as 20 F.
  • the result is a much thicker plating than when operating at F., for example around five times as thick, and at the same time greater solution stability is obtained.
  • Such temperatures are quite feasible with nickel carbonyl whose freezing point is 25 F., and coating thicknesses perhaps in the order of 0.00002 inch are obtained. With other carbonyls low temperatures may be employed approaching those at which. the carbonyl freezes out of solution.
  • a coating process comprising: heating an object to a temperature between about 450 F. and 600 F.; dipping the heated object into a solution of a metal carbonyl in a hydrocarbon to deposit a metal coating, the temperature of the carbonyl solution approaching the freezingout point of the carbonyl; removing the object before its surface temperature drops below about 5 400 F.; reheating the object; re-dipping the object to deposit an additional coating of metal; removing the object as before; and cooling.

Description

Patented Sept. 26, 1950 UNITED STATES PATENT OFFICE J ohnT. Young-and Olind'oiR. Angelillo, :Los .Angeles, Calif.
NoTDrawing Application March 15, 1946, "Serial N0.'7654,'81'8 2-Olaims. 1
This invention relates to methods for plating or coating various surfaces with metalsand more particularly relates to coating metal surfaces. One of the important Objects of the invention is to provide a non-porous, continuous coating of metal capable of sealing the capillary channels along the boundaries of the metal grains which make up the surface of the metal body being plated. This object has been attained with carbonyl solutions.
The ultimate object accomplished by such coating of metals is the complete avoidance of corrosion of the coated metals.- The thorough sealin of the pores of a readily corrodible metal by a continuous coating of a suitable metal such as nickel, chromium, and the like, apparently prevents aspiration, or breathing of the base metal, thereby preventing corrosion. Also, the formation of fungus growths on metal surfaces, has also been prevented in accomplishing the objects of the present invention.
A further object of the invention is to provide a process for applying continuous metal coatings of such tenuity that they may be used for plating precision instruments and the like without afiecting the dimensional tolerances permitted, such coatings -atthe same time being uniform and providing complete protection against corrosion.
A further object is to provide a process for the coating of metals and other objects with thin metal layers which will not check 'or crack in subsequent use and which at the same time will be so tenaciously bonded to the surface of the articles that such coatings cannot be caused to separate.
Accordin to the principal embodiment of this invention, metal surfaces, such as iron, brass and the like, are provided with very thin protective nickel coatings by employing appropriate solutions of nickel carbonyl.
Suitable solvents are hydrocarbons which are normally volatile, and therefore not capable of interfering with the plating operation. For example, benzol, toluol, hexane, octane, sulphurfree gasoline and kerosene, and kindred aromatic and aliphatic hydrocarbons may be employed. However, hydrocarbons of oily nature which are relatively non-volatile will so coat the surfaces of the articles being plated as to prevent deposition of metal upon such surfaces and may not be used. In other words solvents may not be employed having boiling points above about 450 F. Also hydrocarbons contaminated with oxygen, sulphur, chlorine and other halogens, and
the like, are not acceptable because they usually result-in the formation of black deposits instead 'of the desired pure metal deposits. In other words, :so far as isnow known, only substantially pure hydrocarbons within the indicated ranges of volatility :are acceptable.
The carbonylto be employed according to this invention is preferably nickel :carbonyl .NiQCOM.
"tent must be avoided because the carbonyl is extreme'ly unstable in the presence of water.
The coating or plating operation is accomplished by emp loying an indicated solution of nickel carbonyl, as distinguished from nickel carbonyl in gaseous or vapor form, the temperature of the liquid being held at or below about 80 F. for best results. For example, the solution temperature may be about 100 F. or as low as 20 F. The article to be coated is heated preferably to a temperature of around 500 F2, or between about 500 F. and 575 F., and is then quickly dipped into the carbonyl solution, the
time of contact being so short that the temperatureof the object being coated will not fall below about 450 F. or in any event not below 400 F. I Otherwise, instead of obtaining a lbright nickel metal surface, black stains or streaks are formed, thereby resulting in an improper coating not providing a continuous uniform metal seal. Thus, the article must be heated at least to 450 F. The practical upper temperature limit to which the article may be raised is about 575 F. The apparent absolute upper limit is 625 F., beyond which decomposition appears to be of such nature that proper coating cannot be obtained. The time interval for dipping will vary according to the temperature to which the article is heated and to its size. For example, the time may be from a half second for an object weighing 15 grams to 5 seconds for an object weighing 1000 grams, and correspondingly greater times for heavier articles.
The coating phenomenon involves decomposition of the carbonyl, that is the carbonyl radical separates from the nickel so that the nickel deposits upon the article being coated. The coating action is not a. straight line action like that of electroplating, but the nickel moves in all directions and deposits uniformly on all faces. As a consequence, this method of coating is highly satisfactory for plating threaded and other irregular surfaces where a coating of absolutely uniform thickness is required.
It is to be noted that temperature within the limits stated is a critical factor, and that time is also an important factor in so far as it concerns maintenance of temperatures within the indicated limits. However, as the stated limits indicate, there is a considerable choice of temperatures to which articles to be coated may be heated. Heating of the articles to be coated may be accomplished in any manner appropriate for the particular operation. Such may be oven heating, induction heating by electric coils, or otherwise as desired.
It is, of course, necessary to provide above the plating solution an atmosphere which is inert under the operating conditions and from which all oxygen and water vapor are excluded, as well as sulphur, chlorine, and other reactants. Appropriate inert atmospheres are those represented by nitrogen, helium and carbon dioxide. Carbon dioxide is preferred because it is heavier than air and easy to supply. Carbon monoxide liberated by the decomposition of the carbonyl passes into the inert gaseous blanket which in practice is confined, the carbon monoxide being recovered therefrom for the preparation of additional nickel carbonyl.
When an article has been dipped and withdrawn from the solution, it should be retained in the inert atmosphere above the bath until the surface temperature has dropped below about 300 F. whereby to avoid oxidation of the freshly deposited metal. For this cooling function, the equivalent of the inert atmosphere may be used, such as pure benzol, kerosene or even water, or a solution containing a deoxidizing agent, such as sodium sulfite, pyrogallic acid, or the like, the
article being plunged into such liquid until the required cooling is efiected. However, an inert atmosphere must be maintained above the cooling liquid such as that maintained above the plating solution. Although water vapor must be excluded from the inert atmosphere above the solutions, in order to prevent the nickel from turning black, water may nevertheless be .employed as a cooling agent since it does not appear to affect the metal coating due to the very quick cooling of the article when plunged into water. However, in using water, it is preferable that it contain a deoxidizing agent as above indicated.
The individual coatings produced by the method of this invention are continuous and'of uniform thickness in the order of a few millionths of an inch, or perhaps between about 0.00001 and .000001 inch. Such a coating may represent for example the application of 0.03
milligram per square inch of coated surface. It
is thus apparent that the present process provides coatings so thin that they do not interfere with the tolerances required in the production of precision instruments. It is further apparent that the characteristic of the process by which the metal coating is uniformly applied regardless of surface irregularities, as contrasted with uneven applications on irregular surfaces by electroplating, isof much importance. Whe1 je increased thickness is required, dippings may be repeated, each successive layer being applied in uniform thickness so that the ultimate coating is uniformly thick. These coatings, individually comparable in some respects with molecular layers, thus permit the building of multiple layers to any desired degree in order to insure protection against corrosion without in any way producing undue thickness or overstepping permissible tolerances.
Employment of preferred nickel carbonyl according to the process of this invention for the deposition of nickel coatings of extreme thinness is of great importance, especially from the standpoint of corrosion, inasmuch as pure nickel coatings are of very low porosity. In this respect nickel is superior even to chromium and apparently to all other metals and therefore best for this particular purpose. The value of the metal whose carbonyl is employed lies fundamentally in its own porosity. The less porous and more continuous the metal coating, the greater its value in preventing corrosion. Nickel which has been deposited from nickel carbonyl r is considerably more resistant to corrosion than nickel deposited by any other means, this being due probably to higher purity.
For some purposes it may also be possible to employ solutions of other metal carbonyls in appropriate solvents, such as the indicated hydrocarbon solvents. These carbonyls might be represented by chromium and tungsten carbonyls, and possibly by molybdenum carbonyl, all of these normally being solids and soluble in appropriate organic solvents. As previously indicated, solutions of only very low concentrations need be employed e. g. from about 1% to as low as 0.001% of the metal carbonyl, however, higher concentrations may be used if desired, for example l Inasmuch as the activity of the metal increases asconcentration decreases, coating efficiency is maintained even after the concentration has been lowered to relatively insignificant percentages by repeated dippings.
A further advantageous feature which we have discovered is that with a carbonyl such as nickel carbonyl, very low temperatures of the carbonyl solutions are desirable especially where thick coatings are desired. Thus, a solution of nickel carbonyl in toluene may be used at 0 F. or as low as 20 F. The result is a much thicker plating than when operating at F., for example around five times as thick, and at the same time greater solution stability is obtained. Such temperatures are quite feasible with nickel carbonyl whose freezing point is 25 F., and coating thicknesses perhaps in the order of 0.00002 inch are obtained. With other carbonyls low temperatures may be employed approaching those at which. the carbonyl freezes out of solution.
Since variations in the generic process herein disclosed will become apparent to those skilled in the art to which this improvement relates, it is intended to'cover all such modifications as fall within the scope of the claims.
We claim as our invention:
1. A coating process comprising: heating an object to a temperature between about 450 F. and 600 F.; dipping the heated object into a solution of a metal carbonyl in a hydrocarbon to deposit a metal coating, the temperature of the carbonyl solution approaching the freezingout point of the carbonyl; removing the object before its surface temperature drops below about 5 400 F.; reheating the object; re-dipping the object to deposit an additional coating of metal; removing the object as before; and cooling.
2. A process as in claim 1 wherein the carbonyl is nickel carbonyl and the temperature of the solution is in the order of 0 F. to 20 F.
JOHN T. YOUNG. OLINDO R. ANGELILLO.
REFERENCES CITED The following references are of record in the file of this patent:
Number 10 Number Great Britain Dec. 9, 1936

Claims (1)

1. A COATING PROCESS COMPRISING: HEATING AN OBJECT TO AN TEMPERATURE BETWEEN ABOUT 450*F. AND 600*F.; DIPPING THE HEATED OBJECT INTO A SOLUTION OF A METAL CARBONYL IN A HYDROCARBON TO DEPOSIT A METAL COATING, THE TEMPERATURE OF THE CARBONYL SOLUTION APPROACHING THE FREEZINGOUT POINT OF THE CARBONYL; REMOVING THE OBJECT BEFORE ITS SURFACE TEMPERATURE DROPS BELOW ABOUT 400*F.; REHEATING THE OBJECT; RE-DIPPING THE OBJECT TO DEPOSIT AN ADDITIONAL COATING OF METAL; REMOVING THE OBJECT AS BEFORE; AND COOLING.
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Cited By (20)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2698810A (en) * 1950-08-25 1955-01-04 Nat Res Corp Coating process
US2742691A (en) * 1950-04-18 1956-04-24 Ohio Commw Eng Co Method of making corrosion resistant clad steel
US2753800A (en) * 1952-03-24 1956-07-10 Ohio Commw Eng Co Production of printing plates
US2760261A (en) * 1952-04-17 1956-08-28 Ohio Commw Eng Co Method of bonding articles
US2829170A (en) * 1954-07-26 1958-04-01 Texas Co Process for decobalting a liquid carbonylate
US2881094A (en) * 1953-07-16 1959-04-07 Thomas B Hoover Process of coating with nickel by the decomposition of nickel carbonyl
US2886468A (en) * 1953-07-16 1959-05-12 Thomas B Hoover Nickel plating process
US2918392A (en) * 1957-01-04 1959-12-22 Gen Aniline & Film Corp Method of depositing metal in the pores of a porous body
US3041197A (en) * 1959-06-01 1962-06-26 Berger Carl Coating surfaces with aluminum
US3075858A (en) * 1958-01-21 1963-01-29 Union Carbide Corp Deposition of composite coatings by vapor phase plating method
US3155532A (en) * 1960-11-10 1964-11-03 Union Carbide Corp Metal plating process
US3214288A (en) * 1961-12-14 1965-10-26 Nat Steel Corp Process for the deposition of metallic aluminum
US3251712A (en) * 1962-09-21 1966-05-17 Berger Carl Metal plating with a heated hydrocarbon solution of a group via metal carbonyl
US3449150A (en) * 1965-03-31 1969-06-10 Continental Oil Co Coating surfaces with aluminum
US3464844A (en) * 1967-03-02 1969-09-02 Continental Oil Co Aluminum plating of surfaces
US3508977A (en) * 1967-01-11 1970-04-28 Union Carbide Corp Process for producing metal borides on the surface of metals
US3549412A (en) * 1968-04-29 1970-12-22 Ethyl Corp Metal plating particulated substrates
US3652322A (en) * 1970-09-03 1972-03-28 Continental Oil Co Method for controlling the heating of a metal immersed in a plating solution
US4373162A (en) * 1980-03-10 1983-02-08 Control Data Corporation Low frequency electronically steerable cylindrical slot array radar antenna
US4457957A (en) * 1980-01-16 1984-07-03 American Glass Research, Inc. Method for applying an inorganic titanium coating to a glass surface

Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US1561900A (en) * 1925-11-17 Frederick m
GB491948A (en) * 1935-12-28 1938-09-12 Carl Trenzen Process for the production of hard resistant surfaces on metals
US2197622A (en) * 1937-04-22 1940-04-16 American Rolling Mill Co Process for galvanizing sheet metal
US2265467A (en) * 1939-02-23 1941-12-09 Gen Motors Corp Control of nickel-dip solutions
US2304182A (en) * 1939-06-19 1942-12-08 Sigmund Cohn Method of forming metallic films
US2344138A (en) * 1940-05-20 1944-03-14 Chemical Developments Corp Coating method

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US1561900A (en) * 1925-11-17 Frederick m
GB491948A (en) * 1935-12-28 1938-09-12 Carl Trenzen Process for the production of hard resistant surfaces on metals
US2197622A (en) * 1937-04-22 1940-04-16 American Rolling Mill Co Process for galvanizing sheet metal
US2265467A (en) * 1939-02-23 1941-12-09 Gen Motors Corp Control of nickel-dip solutions
US2304182A (en) * 1939-06-19 1942-12-08 Sigmund Cohn Method of forming metallic films
US2344138A (en) * 1940-05-20 1944-03-14 Chemical Developments Corp Coating method

Cited By (20)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2742691A (en) * 1950-04-18 1956-04-24 Ohio Commw Eng Co Method of making corrosion resistant clad steel
US2698810A (en) * 1950-08-25 1955-01-04 Nat Res Corp Coating process
US2753800A (en) * 1952-03-24 1956-07-10 Ohio Commw Eng Co Production of printing plates
US2760261A (en) * 1952-04-17 1956-08-28 Ohio Commw Eng Co Method of bonding articles
US2881094A (en) * 1953-07-16 1959-04-07 Thomas B Hoover Process of coating with nickel by the decomposition of nickel carbonyl
US2886468A (en) * 1953-07-16 1959-05-12 Thomas B Hoover Nickel plating process
US2829170A (en) * 1954-07-26 1958-04-01 Texas Co Process for decobalting a liquid carbonylate
US2918392A (en) * 1957-01-04 1959-12-22 Gen Aniline & Film Corp Method of depositing metal in the pores of a porous body
US3075858A (en) * 1958-01-21 1963-01-29 Union Carbide Corp Deposition of composite coatings by vapor phase plating method
US3041197A (en) * 1959-06-01 1962-06-26 Berger Carl Coating surfaces with aluminum
US3155532A (en) * 1960-11-10 1964-11-03 Union Carbide Corp Metal plating process
US3214288A (en) * 1961-12-14 1965-10-26 Nat Steel Corp Process for the deposition of metallic aluminum
US3251712A (en) * 1962-09-21 1966-05-17 Berger Carl Metal plating with a heated hydrocarbon solution of a group via metal carbonyl
US3449150A (en) * 1965-03-31 1969-06-10 Continental Oil Co Coating surfaces with aluminum
US3508977A (en) * 1967-01-11 1970-04-28 Union Carbide Corp Process for producing metal borides on the surface of metals
US3464844A (en) * 1967-03-02 1969-09-02 Continental Oil Co Aluminum plating of surfaces
US3549412A (en) * 1968-04-29 1970-12-22 Ethyl Corp Metal plating particulated substrates
US3652322A (en) * 1970-09-03 1972-03-28 Continental Oil Co Method for controlling the heating of a metal immersed in a plating solution
US4457957A (en) * 1980-01-16 1984-07-03 American Glass Research, Inc. Method for applying an inorganic titanium coating to a glass surface
US4373162A (en) * 1980-03-10 1983-02-08 Control Data Corporation Low frequency electronically steerable cylindrical slot array radar antenna

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