|Publication number||US2881518 A|
|Publication date||Apr 14, 1959|
|Filing date||Nov 23, 1956|
|Priority date||Nov 23, 1956|
|Publication number||US 2881518 A, US 2881518A, US-A-2881518, US2881518 A, US2881518A|
|Inventors||Jr Harry A Toulmin|
|Original Assignee||Ohio Commw Eng Co|
|Export Citation||BiBTeX, EndNote, RefMan|
|Patent Citations (4), Referenced by (5), Classifications (8)|
|External Links: USPTO, USPTO Assignment, Espacenet|
A121] 14, 1959 H. A. TOULMIN, JR ,3
CONTINUOUS GAS PLATED METAL ARTICLE Filed 'Nov. 23, 1956 31: l4 7 "4| 30c 31 A i I INVENTOR. l HARRY A. TOULMIN JR.
BY 7 2 Q ATTORNEYS United States Patent CONTINUOUS GAS PLATED METAL ARTICLE Harry A. Toulmin, Jr., Dayton, Ohio, assignor to The Commonwealth Engineering Company of Ohio, Dayton, Ohio, a corporation of Ohio Application November 23, 1956, Serial No. 624,171
1 Claim. (Cl. 29-527) This application is related to my copending application Serial No. 270,919 filed February 11, 1952, now abandoned, which is a division of my application Serial No. 115,033, filed September 10, 1949, and patented November 3, 1953, as US. Patent No. 2,657,457.
This invention relates to protective metal coatings. More particularly, it relates to the coating of cast metals by deposition of protective metals through decomposition of volatile metal compounds, and apparatus for carrying out the process.
Special types of carbon and alloy steel and non-ferrous alloys have been manufactured heretofore by pouring the molten metal into ingot molds.
Large size ingots while still hot are removed from the molds and shipped to the soaking pits where they are held until the internal and external ingot temperatures equalize.
The soaked ingots then are rolled in blooming mills into billets preparatory to further processing.
Rough billets require more or less surface conditioning because, for example, the steel is particularly prone to form loose scale and become badly oxidized while cooling, thus necessitating the surface treatment.
This process has now been at least partially superseded by the so-called continuous casting process. Continuous casting has been successfully performed upon a commercial scale, both in conjunction with ferrous and non-ferrous alloys.
While the continuous casting process eliminates several expensive steps, such as making and soaking ingots and rolling them on a blooming mill, it does not, for example, prevent scaling, oxidizing, and other surface conditions.
It is an object of the present invention to overcome the limitations and disadvantages of the processes known heretofore.
It is also an object of the present invention to prepare cast metal objects having a protective coating of a nonoxidizing metal.
It is' another object of this invention to prepare cast steel of reduced scaling character.
It is still a further object of this invention to prepare cast steel with ductile protective metal coatings which do not interfere with further processing such as rolling.
It is still another object of this invention to prepare cast metals having protective coatings not depositable by electrolytic methods.
Still another object of the present invention is to produce a simplified method of coating cast steel.
A still further object of this invention is to produce a method wherein continuously cast steel is continuously plated. v I
It is still another object of this invention to produce a method wherein cast steel is plated while not and a protective' layer deposited.
It is also another object of the present invention to provide a method of increased efiic'iency due to the utilization of heat normally dissipated in the cooling operatldl'i.
Other and more specific objects and advantages will be apparent to one skilled in the art as the following description proceeds.
In brief, the process is carried out by casting metals and when the continuous ribbon of hot but solidified metal issues from the mold, bringing the hot metal into contact with vapors of decomposable metal compounds.
In this way at least a portion of the heat in the molded material instead of being wasted is utilized to decompose volatile metal compounds and deposit a protective coatmg.
In sequence the molten metal is poured into a shaping mold and cooled to a solid form. The formed cast metal progresses through an insulating sleeve, where cooling is controlled until the cast metal is reduced to a tempera ture in the range of approximately 300 to 600 F., depending upon the type of metal being cast and the thickness of the casting.
This hot metal then progresses through a plating chamber where the temperature of the metal decomposes vapors of volatile metal compounds continuously fed into contact with the continuously moving cast object.
The metal at this stage is solidified to the point where its speed of movement may be controlled by a roll drive or equivalent mechanism.
The plated cast metal is then cut to desired length by suitable means such as saws, acetylene torches, and the like.
In the plating step the hot cast metal is brought into contact with continuously changing atmosphere which is made up of gaseous material, at least a portion of which is decomposable at the temperature of the continuously moving cast metal to deposit a metal coating.
Inasmuch as the cast metal is progressing continuously through this chamber, one of the factors important to the successful operation is control of gas pressure not only within the plating chamber itself, but in each of the surrounding annular spaces, of design which will be hereafter explained.
In order to insure against leakage of plating gases which are toxic from the plating chamber and still have openings in the partition Walls for the continuous passage of the cast metal, it is necessary to maintain a metal-vapor free gas atmosphere at a slightly higher gas pressure in the annular spaces surrounding the plating chamber.
The leakage of inert gas into a plating chamber is limited to small quantities by having apertures in the partition Walls of a configuration providing a loose sliding fit with the object passing therethrough or enlarged holes with shims encircling the moving object in close proximity to these holes and by keeping the pressure differential small.
It will be recognized that the inert gas leaking into the plating chamber is not a harmful operation because the metal-bearing gases are usually diluted with an inert gaseous medium and the gas decomposing reaction in the plating chamber produces relatively inert decomposition products.
The stream of gaseous material brought into contact with the hot cast metal 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.
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, ni-- 3 trosyl 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 carbonyls halogens, for example, osmium cirbonyl bromide, ruthenium carbonyl chloride, and the 1' e.
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, nickle 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 efiiciently 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 range of 375 F. to 425 F.
The process is illustrated without provision for annealing the deposited coating in order to increase their adhesion and ductility. If such an operation is desired provision can be made for an anneal in the inert gas filled annular space, as will be more definitely explained.
Annealing temperatures are higher than plating temperatures and generally in the range of 800 to 1200 F. An anneal may be carried out, for example, by induction heating as shown diagramamtically at 43 in Figure 2.
The invention will be more clearly understood from the following description taken in connection with the drawing which:
Figure 1 is a diagrammatic elevational view of a complete unit for continuously casting and plating metals; and
Figure 2 is an enlarged sectional view of the plating equipment.
Referring to the drawings, there is illustrated a continuous method of casting and plating as utilized in connection with steel manufacture without any intention that the invention be limited thereto.
In Figure 1 there is shown the supporting framework of a multi-story building. On the top floor of said building framework 10 supports tracks 11 for a movable overhead crane 12.
A ladle 13 is suspended from crane 12 by suitable cables 14. Ladle 13 is shown suspended over a heated holding ladle 15. Ladle 15 is actuated for tipping and pouring by suitable means 16 such as pulleys or levers.
Adjacent the ladle 15 is a liquid-cooled mold 17 in which ladle 15 is adapted to empty. A cast steel tube 18 is shown issuing from the mold 17 and moving downward through an insulating sleeve 19 within which there is generally maintained an atmosphere of hydrogen.
Steel tube 18 moves downward from the sleeve 19 through a unit 20 designed to accurately maintain and control the temperature of the steel tube. Steel tube 18 passes on downward through a plating unit 21 which will be described in more detail.
Plated steel tube is drawn downward at a predetermined rate, generally in the range of 3 to 7 feet per minute for a tube of about 3 inch radius, by squeeze rolls 22.
The coated steel tube is cut into predetermined lengths by an acetylene torch 23 and the tubular units lowered to the horizontal by suitable cradle means 24.
Referring to Figure 2, it will be seen that the plating unit 21 consists of an inner wall member 30 and outer wall members 31 and 32, which enclose annular spaces or chambers 33 and 34, respectively.
Each of the wall members is provided with two aligned ports indicated as a and b, respectively, of size adapted for close sliding fit with the steel tube 18 passing vertically downward therethrough. The closure of each chamber may be tightened by use of shims indicated as c and d.
The inner chamber is provided with gas inlet and outlet means 35 and 36, respectively. Chamber 33 is provided with gas inlet and outlet means 37 and 38, respectively. Chamber 34 is provided with inlet and outlet means 39 and 40, respectively. Outlet means 40 is adapted with an exhaust means 41, such as a fan, for maintaining less than atmospheric pressure in annular space 34.
Operation of the equipment is as follows:
Hot molten metal is poured at a temperature in excess of 2000 F. In the primary mold the temperature is reduced to that necessary to set the cast metal, for carbon steel this is in a temperature range of 1200 F. to 1600' F.
In the insulating sleeve or after cooler the temperature is reduced to a temperature in the range of approximately 300 to 600 F. and preferably to 350 to 450 F. in an atmosphere of hydrogen.
The hot metal then travels through the plating unit. In this unit, the inner chamber is the plating chamber, where the hot metal contacts an atmosphere, preferably of carbon dioxide and vapors of a volatile metal compound. These vapors may be maintained under a variety of pressures, ranging from a pressure below to pressures above atmospheric pressures and generally in the range of 6 inches of water vacuum to 6 inches of water positive pressure.
In the outer annular space there is maintained an atmosphere of inert gas. The gas is maintained under a pressure generally slightly under atmospheric in order that all gas, either that inert introduced or atmospheric air leaking into this annular space 34, will be removed by the exhaust fan and there will be no tendency for gas to leak out, contaminating the atmosphere which must be frequented by workmen.
In the intermediate annular space 33 there is maintained an inert gas atmosphere under a pressure generally higher than is maintained in either the inner chamber or the outer annular space. While other arrangements could be used, the high pressure is preferred for the intermediate annular space because gas flow is then inward into the plating chamber through the free space around the traveling rod.
In the plating of nickel, by way of specific example, upon a 3 inch diameter rod of cast steel, the following conditions may be maintained:
The steel may be poured at the rate of approximately 400 pounds per minute, which rate will supply continuously cooled rod traveling at a rate of approximately 5 feet per minute.
The temperature of the rod entering the plating chamber may be controlled to be approximately 425 F.
The rate of flow of gaseous medium to the plating chamber may be approximately 20 cubic feet per hour per cubic foot of chamber space, with nickel carbonyl.
vapors being present in the ratio of approximately 10 ounces of carbonyl per cubic foot of carbon dioxide gas passed through the plating chamber.
The rate of flow of carbon dioxide gas through the intermediate annular space 33 may be maintained at approximately 30 cubic feet of gas per hour per cubic foot of chamber space.
The rate of flow of gas in the outer annular space 34 may be at the rate of 5 cubic feet per hour per cubic foot of chamber space, and the actual pressure maintained on the space by the exhaust equipment being 2 inches of water vacuum. p
It will be understood that while the method and apparatus disclosed and described herein illustrate a preferred form of the invention, modification can be made without departing from the spirit of the invention, and
that all modifications that fall within the scope of the appended claim are intended to be included herein.
What is claimed is:
In a continuous process of the character described, the improvement which comprises establishing an alkyl metal vapor atmosphere, continuously casting a hot metal shape at a temperature high enough for such shape readily to acqure an oxide scale in air, cooling the hot cast shape to a temperature range of 300 to 600 F., thereafter introducing said cast hot metal shape into said alkyl metal vapor atmosphere, maintaining the hot cast shape in said atmosphere while the same is at a temperature to cause thermal decomposition of said metal vapor until it is substantially completely coated by an adhering film of the product resulting from thermal decomposition of said vapor by contact thereof with the hot cast shape, subjecting the resultant plated metal shape to a temperature of 800 to 1200 F. to increase the adhesion and ductility of the coating whereby the surface of the hot cast shape is protected from oxidation by a protective coating of 20 metal.
References Cited in the file of this patent UNITED STATES PATENTS OTHER REFERENCES Pages 55, 98 and 114 of The Working of Metals, published in 1937, by The American Society for Metals, Cleveland, Ohio.
Pages 121 and 122, Metalwork Technology and Practice, by Oswald A. Ludwig, M.A., revised 1947 edition, McKnight & McKnight, Bloomington, Illinois.
Pages 426, 464 and 1511, Tool Engineers Handbook, first edition, 1949, published by McGraw-Hill Book Co. Inc., New York, NY.
|Cited Patent||Filing date||Publication date||Applicant||Title|
|US2619433 *||Jul 14, 1949||Nov 25, 1952||Ohio Commw Eng Co||Method of gas plating|
|US2638423 *||Aug 25, 1949||May 12, 1953||Ohio Commw Eng Co||Method and apparatus for continuously plating irregularly shaped objects|
|US2657457 *||Sep 10, 1949||Nov 3, 1953||Ohio Commw Eng Co||Continuous metal production and continuous gas plating|
|US2762115 *||Jan 29, 1952||Sep 11, 1956||American Brass Co||Protecting hot extruded metal|
|Citing Patent||Filing date||Publication date||Applicant||Title|
|US3120001 *||Dec 8, 1958||Jan 28, 1964||Ibm||Magnetic transducer|
|US3191251 *||Aug 16, 1962||Jun 29, 1965||Allan Olsson Erik||Process for treating continuously cast material|
|US3202530 *||Nov 30, 1961||Aug 24, 1965||Olin Mathieson||Method of forming a composite metal article|
|US3209446 *||Aug 19, 1964||Oct 5, 1965||Krueger Brewing Company G||Method of installing a pump lever in a pump body|
|US4938999 *||Jul 11, 1988||Jul 3, 1990||Jenkin William C||Process for coating a metal substrate by chemical vapor deposition using a metal carbonyl|
|U.S. Classification||164/477, 164/268, 427/252, 427/251, 29/527.3|