US2359401A - Metal powders - Google Patents

Metal powders Download PDF

Info

Publication number
US2359401A
US2359401A US413367A US41336741A US2359401A US 2359401 A US2359401 A US 2359401A US 413367 A US413367 A US 413367A US 41336741 A US41336741 A US 41336741A US 2359401 A US2359401 A US 2359401A
Authority
US
United States
Prior art keywords
powder
alloy
stainless steel
produced
product
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Lifetime
Application number
US413367A
Inventor
Wulff John
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Individual
Original Assignee
Individual
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Individual filed Critical Individual
Priority to US413367A priority Critical patent/US2359401A/en
Priority to US445082A priority patent/US2354727A/en
Priority to US445083A priority patent/US2368282A/en
Application granted granted Critical
Publication of US2359401A publication Critical patent/US2359401A/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Classifications

    • 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
    • C23C4/00Coating by spraying the coating material in the molten state, e.g. by flame, plasma or electric discharge
    • C23C4/04Coating by spraying the coating material in the molten state, e.g. by flame, plasma or electric discharge characterised by the coating material
    • C23C4/06Metallic material
    • C23C4/067Metallic material containing free particles of non-metal elements, e.g. carbon, silicon, boron, phosphorus or arsenic
    • 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
    • Y10STECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10S428/00Stock material or miscellaneous articles
    • Y10S428/922Static electricity metal bleed-off metallic stock
    • Y10S428/9335Product by special process
    • Y10S428/937Sprayed metal
    • 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
    • Y10T29/00Metal working
    • Y10T29/49Method of mechanical manufacture
    • Y10T29/49751Scrap recovering or utilizing
    • Y10T29/49755Separating one material from another

Definitions

  • the stainless steel powder entering these compacts may economically be produced from stainless steel scrap by suitable heat treatment followed by intergranular corrosion, ball milling or other disintegration treatment and classification.
  • this raw material due to the relatively high percentage of contaminating material, has had no commercial outlet. It has been found that this material may be treated by simple methods to produce a stainless steel or other alloy powder in desirably finely divided form and free from associated contaminants. The product thus produced is particularly useful in certain fields, such as in the spraying of metal powder by the Schoop gun, in which very fine material of the order of 325 mesh is preferred.
  • the raw material which is subjected to treatment according to the present invention consists of grindings, borings, tumings, which contain the usual contaminants. This material contains quite a large percentage of such products as silica,
  • silicon carbide organics (from the bonding agent of the grinding wheels), and the like. In most circumstances this material also contains quite a high percentage of ordinary iron, and sometimes brass.
  • this type of raw material is first heat treated in a special thermal range and under conditions which conduct to the precipitation of carbides in the grain boundaries and which coincidentally eliminates certain of the contaminants.
  • the raw material preferably is heat treated in a rotary kiln furnace between 500 and 900 C. for a period varying from to 24 hours.
  • this heating is done cyclically, that is to say, the temperature is cyclically elevated and lowered within the carbide precipitation range to accelerate carbide precipitation. Due to, this heat treatment carbides are precipitated in the grain boundaries and slip planes; coincidentally, a I considerable amount of contaminants such as sulfur and the like are burnt off.
  • the product produced by the heat treatment is then quenched in a suitable contact corroding medium such as in a spent pickling liquor, from steel pickling, to which liquor has been added of the order of 5% of sodium fluoride and sometimes up to 5% sulphuric acid.
  • a suitable contact corroding medium such as in a spent pickling liquor, from steel pickling, to which liquor has been added of the order of 5% of sodium fluoride and sometimes up to 5% sulphuric acid.
  • a suitable contact corroding medium such as in a spent pickling liquor, from steel pickling, to which liquor has been added of the order of 5% of sodium fluoride and sometimes up to 5% sulphuric acid.
  • the liquor is separated from the solid residue. This may be done in any suitable continuous filtering apparatus or by decanting off the supernatant pickle liquor.
  • the residue from the pickling stage may be washed to remove adherent pickle'and is then screened. It has been found that by a simple screening method a very large proportion of the oxides and abrasives present in the original residue can be removed. Specifically, it has been found that most of these oxides and abrasives are separated from the metallic particles by screening through approximately a or 200 mesh screen and discarding the 100 or 200 mesh material. It has been found, similarly, that much of the low iron alloy content in the original residue will be removed in this screening operation, due to the fact that the low alloy iron is corroded to fines during the pickling, whereas the substantially corrosive-resistant stainless steel particles are unattacked. I
  • the coarse material produced from the above screening operation comprises essentially stainless steel or other high alloy iron powder and is then disintegrated. This may effectively be done by ,crushing the'material in a suitable type of hammer mill and preferably in a micro-pulverizer.
  • This type of machine can be set for a more or less definite degree of disintegration, i. e., for -100, -200, and 300 mesh material.
  • the micro-pulverizer is peculiarly effective for this operation, for the material can be disintegrated at the rate of about 25 to 400 pounds per hour.
  • a series of stellite hammers move through a small distance, of the order of a! of an inch, at extremely high speed.
  • the material to be treated may be fed to the pulverizer either wet or dry or in admixture with any suitable lubricant.
  • the alloys treated due to the cold work applied to the metal, the alloys treated (18-8; 18-8-Mo; 18-8-Ti; etc.) are rendered ma netic.
  • the crushed material produced in the pulverizer step may then be treated in a suitable corrodent, so as to selectively attack the grain boundaries (high in carbides) and for removing imbedded abrasive scale, low alloy iron and the like.
  • the corrodent for this step of the process may comprise a suitable aqueous solution of acid ferric sulphate and sodium fluoride. The period of retention in the corroding solution will vary depending upon the particular product treated, the temperature of the corroding solution, and the like.
  • the crushed and corroded material is now re- 'moved from the corrosion vat and is washed to free it of adherent corrodent.
  • the product is then concentrated, preferably on a Welfiey table, to separate the metal particles from the nonmetallic particles, i. e., abrasive material, oxides, carbides and the very fine unalloyed iron. These latter products are discarded in the tailings and the concentrate is recovered, which contains of the order of 90 to 98% of stainless steel powder.
  • the tailings, middlings and concentrate produced in the above concentration step may be further concentrated either by flotation, electrostatic or magnetic separation.
  • the final concentrate which comprises essentially an 18-8 steel powder, is then contacted or washed with a hot nitric acid solution between about and 20% concentration.
  • This treatment serves a number of useful functions, namely, to brighten or shine such powder.
  • the material thus produced is particularly useful for spraying in metal guns of the type mentioned because of its desirably fine mesh, and for such purpose the product can be used directly.
  • the product may also be used for powder metallurgy purposes. However, for this use it is necessary to subject the material to an additional treatment, preferably to a dry hydrogen anneal in a temperature range between about 900 C. and 1200 0.
  • Useful discrete steel powder may be produced from the described source material by first crushing the raw material in a micropulverizer, or similar machine, to such a degree that it passes through a 200 mesh screen. Since these metal particles are already quite severely work hardened (due to the grinding and boring operations which produce them) they are quite brittle and are readily disintegrated. Durina this grinding operation the contaminants in the raw material, 1. e., grinding oil, sulphur, rubber, Bakelite and the like, serve beneficially in the role of lubricants. During this grinding operation the attached or adhered abrasive particles are largely removed from the mesh by impact.
  • the ground product described above is then fed to a screen which classifies the material into two fractions, one of a screen analysis between 200 and -325 mesh and the other a -325 mesh. These two fractions are then each passed through a magnetic separator, or if desired each fraction may be treated by gravity separation methods such as flotation, Welfiey table separation, and the like.
  • the magnetic concentrate, or the concentrate produced by table or flotation, is treated .with a nitric acid solution of suitable concentration.
  • This treatment serves to degrease the product by undercutting and to passivate the stainless steel.
  • the material thus produced is washed and dried and may be briquetted in any suitable manner, so as to be employed in a high alloy steel melt.
  • the product is preferably ball milled either in a wet ball milling operation in contact with a liquid medium such as Varsol or it may 'be dry milled and polished with stearic acid.
  • the material produced is to be used for Y spraying, it may be mixed with a flux or with a of homogeneously incorporating the flux or the low melting metal powder in the stainless steel is to run the mixture through the micro-pulverizer. Another method is to separately grind the fiux or low melting point metal powder so that its particle size will be equal to and preferably less than that of the stainless steel powder, and then mixing the two.
  • a flux or with a of homogeneously incorporating the flux or the low melting metal powder in the stainless steel is to run the mixture through the micro-pulverizer.
  • Another method is to separately grind the fiux or low melting point metal powder so that its particle size will be equal to and preferably less than that of the stainless steel powder, and then mixing the two.
  • low melting calcium-manganesesilicon alloys silver-copper-phosphorus eutectic alloy, term-manganese and the like, may be utilized.
  • Any metallic product compatible with stainless steel powder and which serves to accelerate or facilitate the bonding of thesprayed powder to the base material may be used.
  • the sprayed coating may be wire brushed to secure a desired matte finish, or the material can be abraded fiat and then brushed, and if desired finished bypolishing. Similarly, the sprayed material may be electrolytically polished.
  • Spraying powder of the type above described is useful in a wide variety of fields, as, for example, in the application of corrosion-resistant, relatively fine-sectioned surfaces to more corrodible base metal, and to the building up of steel surfaces, by the sprayin technique, to a desired specification.
  • the applied sprayed coating may be suitably treated, as by flame hardening, or high frequency hardening, to improve the wearing qualities of the applied coat.
  • an alloy steel powder of the 18-8 type particularly suitable for metal spraying which consists essentially of a homogeneous mixtureof preponderant percentage of] 18-8 powder and a minor percentage of a lower melting point metal such lower melting point metal being of a kind which improves the adherence of the sprayed 18-8 powder to the base material on which it is sprayed.
  • the lower melting point'metai powder being of the type which improves the adherence of the sprayed 18-8 powder to the base material on which it is sprayed.
  • a metal spraying powder consisting essentially of 18-8 powder in homogeneous admixture with a low melting alloy powder containing calcium, manganese and silicon.
  • 18-8 powder in homogeneous admixture with a minor percentage of a low melting alloy of silver, copper and phosphorus, and having a screen analysis of --325- mesh.

Description

Patented Get. 3, 19
No Drawing. Application October 2, 1941, Serial No. 413,367
7 Claims. (Cl. 75-05) In the production of stainlesssteel, and par-' ticularly in the alloy steel casting industry, there is a considerable amount ofborings, turnings, and grinding residues availablel whi. ntain not an inconsiderable percentage of stainless steel. These residues are produced, for the most part, by grinding stainless steel or other high alloy castings" with an abrasive wheel. The product or grinding residues produced is in quite finely divided form, but due to its contaminaton with the abrasive and bonding materialof the wheel, it has heretofore attained nocommercial market.
In the field of powder metallurgy, stainless steel powder in various meshes has a considerable potential use. It has been found, as is more particularly explained in my copending application, Serial No. 383,875, filed March 1'7, 1941, that this powder may be compacted under suitable pressures to produce a self-sustaining compact which, with the proper technique, may be sintered to produce an ultimate article of very satisfactory physical characteristics.
As explained in that prior application, the stainless steel powder entering these compacts may economically be produced from stainless steel scrap by suitable heat treatment followed by intergranular corrosion, ball milling or other disintegration treatment and classification.
It has now been found that a particularly useful and economical source material for stainless steel powder or other high alloy iron powders are the swing grinding residues produced by the final surfacing of alloy castings and similar alloy steel objects. Y
In the past this raw material, due to the relatively high percentage of contaminating material, has had no commercial outlet. It has been found that this material may be treated by simple methods to produce a stainless steel or other alloy powder in desirably finely divided form and free from associated contaminants. The product thus produced is particularly useful in certain fields, such as in the spraying of metal powder by the Schoop gun, in which very fine material of the order of 325 mesh is preferred.
The raw material which is subjected to treatment according to the present invention consists of grindings, borings, tumings, which contain the usual contaminants. This material contains quite a large percentage of such products as silica,
silicon carbide, organics (from the bonding agent of the grinding wheels), and the like. In most circumstances this material also contains quite a high percentage of ordinary iron, and sometimes brass.
In carrying out the invention this type of raw material is first heat treated in a special thermal range and under conditions which conduce to the precipitation of carbides in the grain boundaries and which coincidentally eliminates certain of the contaminants. In this step of the process the raw material preferably is heat treated in a rotary kiln furnace between 500 and 900 C. for a period varying from to 24 hours. Preferably this heating is done cyclically, that is to say, the temperature is cyclically elevated and lowered within the carbide precipitation range to accelerate carbide precipitation. Due to, this heat treatment carbides are precipitated in the grain boundaries and slip planes; coincidentally, a I considerable amount of contaminants such as sulfur and the like are burnt off.
The product produced by the heat treatment is then quenched in a suitable contact corroding medium such as in a spent pickling liquor, from steel pickling, to which liquor has been added of the order of 5% of sodium fluoride and sometimes up to 5% sulphuric acid. In thus quenching the hot material a considerable amount of the adherent abrasive is detached from the metal particles by exfoliation. Due to the contact with the pickling liquor additional amounts of the abras ves are detached by reason of the under-cutting effect of the pickle. Since the heat treated material is quenched in the pickle liquor the temperature of the latter is quickly elevated and the pickle is extremely active.
After the quenched product has been retained in the pickle liquor for a predetermined period of time, usually from about 30 minutes or more, the liquor is separated from the solid residue. This may be done in any suitable continuous filtering apparatus or by decanting off the supernatant pickle liquor.
The residue from the pickling stage may be washed to remove adherent pickle'and is then screened. It has been found that by a simple screening method a very large proportion of the oxides and abrasives present in the original residue can be removed. Specifically, it has been found that most of these oxides and abrasives are separated from the metallic particles by screening through approximately a or 200 mesh screen and discarding the 100 or 200 mesh material. It has been found, similarly, that much of the low iron alloy content in the original residue will be removed in this screening operation, due to the fact that the low alloy iron is corroded to fines during the pickling, whereas the substantially corrosive-resistant stainless steel particles are unattacked. I
The coarse material produced from the above screening operation comprises essentially stainless steel or other high alloy iron powder and is then disintegrated. This may effectively be done by ,crushing the'material in a suitable type of hammer mill and preferably in a micro-pulverizer. This type of machine, as is known, can be set for a more or less definite degree of disintegration, i. e., for -100, -200, and 300 mesh material. The micro-pulverizer is peculiarly effective for this operation, for the material can be disintegrated at the rate of about 25 to 400 pounds per hour. In this type of apparatus, as those skilled in the art recognize, a series of stellite hammers. move through a small distance, of the order of a! of an inch, at extremely high speed. It will be understood that in this disintegrating operation the material to be treated may be fed to the pulverizer either wet or dry or in admixture with any suitable lubricant. During this disintegrating operation, due to the cold work applied to the metal, the alloys treated (18-8; 18-8-Mo; 18-8-Ti; etc.) are rendered ma netic.
The crushed material produced in the pulverizer step may then be treated in a suitable corrodent, so as to selectively attack the grain boundaries (high in carbides) and for removing imbedded abrasive scale, low alloy iron and the like. The corrodent for this step of the process may comprise a suitable aqueous solution of acid ferric sulphate and sodium fluoride. The period of retention in the corroding solution will vary depending upon the particular product treated, the temperature of the corroding solution, and the like.
The crushed and corroded material is now re- 'moved from the corrosion vat and is washed to free it of adherent corrodent. The product is then concentrated, preferably on a Welfiey table, to separate the metal particles from the nonmetallic particles, i. e., abrasive material, oxides, carbides and the very fine unalloyed iron. These latter products are discarded in the tailings and the concentrate is recovered, which contains of the order of 90 to 98% of stainless steel powder.
If desired, the tailings, middlings and concentrate produced in the above concentration step may be further concentrated either by flotation, electrostatic or magnetic separation.
The final concentrate, which comprises essentially an 18-8 steel powder, is then contacted or washed with a hot nitric acid solution between about and 20% concentration. This treatment serves a number of useful functions, namely, to brighten or shine such powder. The material thus produced, as noted previously, is particularly useful for spraying in metal guns of the type mentioned because of its desirably fine mesh, and for such purpose the product can be used directly.
The product. may also be used for powder metallurgy purposes. However, for this use it is necessary to subject the material to an additional treatment, preferably to a dry hydrogen anneal in a temperature range between about 900 C. and 1200 0.
As will be appreciated by those skilled in the art, the heretofore waste material, namely, the,"
grinding residues, may be processed to produce valuable alloy steel powder by modifications of the above method. Useful discrete steel powder may be produced from the described source material by first crushing the raw material in a micropulverizer, or similar machine, to such a degree that it passes through a 200 mesh screen. Since these metal particles are already quite severely work hardened (due to the grinding and boring operations which produce them) they are quite brittle and are readily disintegrated. Durina this grinding operation the contaminants in the raw material, 1. e., grinding oil, sulphur, rubber, Bakelite and the like, serve beneficially in the role of lubricants. During this grinding operation the attached or adhered abrasive particles are largely removed from the mesh by impact.
The ground product described above is then fed to a screen which classifies the material into two fractions, one of a screen analysis between 200 and -325 mesh and the other a -325 mesh. These two fractions are then each passed through a magnetic separator, or if desired each fraction may be treated by gravity separation methods such as flotation, Welfiey table separation, and the like.
The magnetic concentrate, or the concentrate produced by table or flotation, is treated .with a nitric acid solution of suitable concentration. This treatment serves to degrease the product by undercutting and to passivate the stainless steel. If the product is to be used for a remelting addition agent, in lieu of passivation,'it may be treated with a typical pickling solution which serves to dissolve the sulphur and levigate the extreme fines of abrasives, oxides, carbides, Bakelite, and the like. This scum may then be removed from the top of the pickle bath.
The material thus produced is washed and dried and may be briquetted in any suitable manner, so as to be employed in a high alloy steel melt.
If the product is to be used as a pigment, for example, in paints, it is preferably ball milled either in a wet ball milling operation in contact with a liquid medium such as Varsol or it may 'be dry milled and polished with stearic acid.
It is to be observed that if the product from the magnetic separator or other concentrator is too high in iron the nitric acid treatment or the pickling is continued so as to dissolve ordinary iron and steel.
If the material produced is to be used for Y spraying, it may be mixed with a flux or with a of homogeneously incorporating the flux or the low melting metal powder in the stainless steel is to run the mixture through the micro-pulverizer. Another method is to separately grind the fiux or low melting point metal powder so that its particle size will be equal to and preferably less than that of the stainless steel powder, and then mixing the two. For 18-8 spraying powders, in
addition to copper and the iron eutectic powder.
mentioned the low melting calcium-manganesesilicon alloys, silver-copper-phosphorus eutectic alloy, term-manganese and the like, may be utilized. Any metallic product compatible with stainless steel powder and which serves to accelerate or facilitate the bonding of thesprayed powder to the base material may be used.
After spraying the improved powder on the base material, for example on a low carbon steel base, the sprayed coating may be wire brushed to secure a desired matte finish, or the material can be abraded fiat and then brushed, and if desired finished bypolishing. Similarly, the sprayed material may be electrolytically polished.
In some circumstances, where an extremely tenacious bond between the sprayed surface and the base plate is desired, it is advantageous to anneal the article under bright annealing conditions.
Spraying powder of the type above described is useful in a wide variety of fields, as, for example, in the application of corrosion-resistant, relatively fine-sectioned surfaces to more corrodible base metal, and to the building up of steel surfaces, by the sprayin technique, to a desired specification. In the event that highly wearresistant coatings are desired, the applied sprayed coating may be suitably treated, as by flame hardening, or high frequency hardening, to improve the wearing qualities of the applied coat.
I claim:
1. As a new article of manufacture an alloy steel powder of the 18-8 type particularly suitable for metal spraying which consists essentially of a homogeneous mixtureof preponderant percentage of] 18-8 powder and a minor percentage of a lower melting point metal such lower melting point metal being of a kind which improves the adherence of the sprayed 18-8 powder to the base material on which it is sprayed.
- the lower melting point'metai powder being of the type which improves the adherence of the sprayed 18-8 powder to the base material on which it is sprayed. g
5. As an article of manufacture a metal spraying powder consisting essentially of 18-8 powder in homogeneous admixture with a low melting alloy powder containing calcium, manganese and silicon.
6. As a spraying powder, 18-8 powder in homogeneous admixture with a minor percentage of a low melting alloy of silver, copper and phosphorus.
7. As a spraying powder, 18-8 powder in homogeneous admixture with a minor percentage of a low melting alloy of silver, copper and phosphorus, and having a screen analysis of --325- mesh.
JOHN WUII'F.
US413367A 1941-10-02 1941-10-02 Metal powders Expired - Lifetime US2359401A (en)

Priority Applications (3)

Application Number Priority Date Filing Date Title
US413367A US2359401A (en) 1941-10-02 1941-10-02 Metal powders
US445082A US2354727A (en) 1941-10-02 1942-05-29 Metal powder
US445083A US2368282A (en) 1941-10-02 1942-05-29 Steel powder

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US413367A US2359401A (en) 1941-10-02 1941-10-02 Metal powders

Publications (1)

Publication Number Publication Date
US2359401A true US2359401A (en) 1944-10-03

Family

ID=23636958

Family Applications (1)

Application Number Title Priority Date Filing Date
US413367A Expired - Lifetime US2359401A (en) 1941-10-02 1941-10-02 Metal powders

Country Status (1)

Country Link
US (1) US2359401A (en)

Cited By (13)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2425919A (en) * 1943-07-28 1947-08-19 Cutler Hammer Inc Method of making metal molding material
US2451422A (en) * 1945-03-24 1948-10-12 Linde Air Prod Co Thermochemical removal of metal with a flux-forming powder in the oxygen cutting stream
US2538990A (en) * 1945-08-22 1951-01-23 Buel Metals Company Electrolytic process for producing iron products
US2543406A (en) * 1949-04-01 1951-02-27 Ethyl Corp Process for recovery of an alkaline earth metal in admixture with an alkali metal
US2666696A (en) * 1950-01-31 1954-01-19 Rca Corp Method of treating metal powders
US2721378A (en) * 1951-06-11 1955-10-25 Birmingham Small Arms Co Ltd Process for manufacture of porous structure
US2725287A (en) * 1952-11-26 1955-11-29 Raytheon Mfg Co Molybdenum solder powder
US2826805A (en) * 1954-01-13 1958-03-18 Federal Mogul Corp Sintered stainless steel metal alloy
US2925619A (en) * 1956-03-15 1960-02-23 Republic Steel Corp Apparatus for pressing consumable electrode billets
US3254970A (en) * 1960-11-22 1966-06-07 Metco Inc Flame spray clad powder composed of a refractory material and nickel or cobalt
US3332752A (en) * 1963-08-22 1967-07-25 Raybestos Manhattan Inc Composite flame spraying wire
US4115076A (en) * 1977-05-24 1978-09-19 Bethlehem Steel Corporation Abrasive material suitable for manually blast cleaning ferrous metals prior to painting
US4118459A (en) * 1973-08-01 1978-10-03 Dynamit Nobel Aktiengesellschaft Chemically removing iron from grits

Cited By (13)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2425919A (en) * 1943-07-28 1947-08-19 Cutler Hammer Inc Method of making metal molding material
US2451422A (en) * 1945-03-24 1948-10-12 Linde Air Prod Co Thermochemical removal of metal with a flux-forming powder in the oxygen cutting stream
US2538990A (en) * 1945-08-22 1951-01-23 Buel Metals Company Electrolytic process for producing iron products
US2543406A (en) * 1949-04-01 1951-02-27 Ethyl Corp Process for recovery of an alkaline earth metal in admixture with an alkali metal
US2666696A (en) * 1950-01-31 1954-01-19 Rca Corp Method of treating metal powders
US2721378A (en) * 1951-06-11 1955-10-25 Birmingham Small Arms Co Ltd Process for manufacture of porous structure
US2725287A (en) * 1952-11-26 1955-11-29 Raytheon Mfg Co Molybdenum solder powder
US2826805A (en) * 1954-01-13 1958-03-18 Federal Mogul Corp Sintered stainless steel metal alloy
US2925619A (en) * 1956-03-15 1960-02-23 Republic Steel Corp Apparatus for pressing consumable electrode billets
US3254970A (en) * 1960-11-22 1966-06-07 Metco Inc Flame spray clad powder composed of a refractory material and nickel or cobalt
US3332752A (en) * 1963-08-22 1967-07-25 Raybestos Manhattan Inc Composite flame spraying wire
US4118459A (en) * 1973-08-01 1978-10-03 Dynamit Nobel Aktiengesellschaft Chemically removing iron from grits
US4115076A (en) * 1977-05-24 1978-09-19 Bethlehem Steel Corporation Abrasive material suitable for manually blast cleaning ferrous metals prior to painting

Similar Documents

Publication Publication Date Title
US2359401A (en) Metal powders
JPH0321630B2 (en)
US2354727A (en) Metal powder
US2368282A (en) Steel powder
US4115076A (en) Abrasive material suitable for manually blast cleaning ferrous metals prior to painting
Hallbauer, DK & Joughin The size distribution and morphology of gold particles in Witwatersrand reefs and their crushed products
US2080346A (en) Metallic paint
US2407862A (en) Method of producing metal powders of high alloy content
US6764557B2 (en) Method for producing angular, stainless shot-blasting abrasives based on an fe-cr-c alloy
US1954462A (en) Metallic paint
US2892697A (en) Method of producing powdered titanium and titanium alloys
US2356807A (en) High-grade alloy powder production
US2271264A (en) Process for the conversion of metals and metal alloys in finely divided form for themanufacture of dental amalgams
US2381022A (en) Iron and iron alloy powders
US2368489A (en) Production of metal powder
US2895816A (en) Steel grit and method for manufacturing same
US2448243A (en) Process of producing magnesium powder by cold rolling and grinding
US2070134A (en) Preparation and use of iron as a precipitant
US6848973B2 (en) Method for blast cleaning using ilmenite tailing particles
US2527611A (en) Method of producing metal powders
US2426659A (en) Producing electrical contact material
CN111546246A (en) High-hardness sand blasting material for surface treatment and preparation method thereof
US2373158A (en) Brass powders
US2765988A (en) Reduction of iron ores
WO1997014760A1 (en) Method for processing iron-containing materials and products produced thereby