US3293334A - Preparation of spherical metal powder - Google Patents
Preparation of spherical metal powder Download PDFInfo
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- US3293334A US3293334A US217415A US21741562A US3293334A US 3293334 A US3293334 A US 3293334A US 217415 A US217415 A US 217415A US 21741562 A US21741562 A US 21741562A US 3293334 A US3293334 A US 3293334A
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- 229910052751 metal Inorganic materials 0.000 title claims description 48
- 239000002184 metal Substances 0.000 title claims description 48
- 239000000843 powder Substances 0.000 title claims description 18
- 238000002360 preparation method Methods 0.000 title description 3
- 239000007789 gas Substances 0.000 claims description 40
- 239000002245 particle Substances 0.000 claims description 36
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims description 25
- 239000001301 oxygen Substances 0.000 claims description 25
- 229910052760 oxygen Inorganic materials 0.000 claims description 25
- 230000015572 biosynthetic process Effects 0.000 claims description 19
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 claims description 13
- 238000000034 method Methods 0.000 claims description 13
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 claims description 12
- 239000012798 spherical particle Substances 0.000 claims description 12
- 239000001569 carbon dioxide Substances 0.000 claims description 6
- 229910002092 carbon dioxide Inorganic materials 0.000 claims description 6
- 238000007711 solidification Methods 0.000 claims description 5
- 230000008023 solidification Effects 0.000 claims description 5
- JCXJVPUVTGWSNB-UHFFFAOYSA-N nitrogen dioxide Inorganic materials O=[N]=O JCXJVPUVTGWSNB-UHFFFAOYSA-N 0.000 claims description 4
- 239000010419 fine particle Substances 0.000 claims description 3
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 19
- 229910052782 aluminium Inorganic materials 0.000 description 17
- 238000007254 oxidation reaction Methods 0.000 description 10
- 230000003647 oxidation Effects 0.000 description 9
- 238000004519 manufacturing process Methods 0.000 description 8
- 239000002923 metal particle Substances 0.000 description 7
- 239000011261 inert gas Substances 0.000 description 6
- 229910000838 Al alloy Inorganic materials 0.000 description 4
- FYYHWMGAXLPEAU-UHFFFAOYSA-N Magnesium Chemical compound [Mg] FYYHWMGAXLPEAU-UHFFFAOYSA-N 0.000 description 4
- 238000000889 atomisation Methods 0.000 description 4
- 238000001816 cooling Methods 0.000 description 4
- 229910052749 magnesium Inorganic materials 0.000 description 4
- 239000011777 magnesium Substances 0.000 description 4
- 150000002739 metals Chemical class 0.000 description 4
- 239000000203 mixture Substances 0.000 description 4
- 229910052757 nitrogen Inorganic materials 0.000 description 4
- 230000000750 progressive effect Effects 0.000 description 4
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 3
- 229910045601 alloy Inorganic materials 0.000 description 3
- 239000000956 alloy Substances 0.000 description 3
- 229910052802 copper Inorganic materials 0.000 description 3
- 239000010949 copper Substances 0.000 description 3
- XKRFYHLGVUSROY-UHFFFAOYSA-N Argon Chemical compound [Ar] XKRFYHLGVUSROY-UHFFFAOYSA-N 0.000 description 2
- ATJFFYVFTNAWJD-UHFFFAOYSA-N Tin Chemical compound [Sn] ATJFFYVFTNAWJD-UHFFFAOYSA-N 0.000 description 2
- 239000000919 ceramic Substances 0.000 description 2
- 238000007599 discharging Methods 0.000 description 2
- 230000001590 oxidative effect Effects 0.000 description 2
- 238000012856 packing Methods 0.000 description 2
- 238000005192 partition Methods 0.000 description 2
- 229910052718 tin Inorganic materials 0.000 description 2
- 239000011135 tin Substances 0.000 description 2
- 229910052786 argon Inorganic materials 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 238000005474 detonation Methods 0.000 description 1
- 230000001627 detrimental effect Effects 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 239000001307 helium Substances 0.000 description 1
- 229910052734 helium Inorganic materials 0.000 description 1
- SWQJXJOGLNCZEY-UHFFFAOYSA-N helium atom Chemical compound [He] SWQJXJOGLNCZEY-UHFFFAOYSA-N 0.000 description 1
- 230000001771 impaired effect Effects 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 238000002844 melting Methods 0.000 description 1
- 230000008018 melting Effects 0.000 description 1
- 229910044991 metal oxide Inorganic materials 0.000 description 1
- 150000004706 metal oxides Chemical class 0.000 description 1
- 150000004767 nitrides Chemical class 0.000 description 1
- 150000002927 oxygen compounds Chemical class 0.000 description 1
- 238000004663 powder metallurgy Methods 0.000 description 1
- 230000002028 premature Effects 0.000 description 1
- 230000001737 promoting effect Effects 0.000 description 1
- 239000011253 protective coating Substances 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 229920006395 saturated elastomer Polymers 0.000 description 1
- 239000004449 solid propellant Substances 0.000 description 1
- 238000010301 surface-oxidation reaction Methods 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
Images
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B22—CASTING; POWDER METALLURGY
- B22F—WORKING METALLIC POWDER; MANUFACTURE OF ARTICLES FROM METALLIC POWDER; MAKING METALLIC POWDER; APPARATUS OR DEVICES SPECIALLY ADAPTED FOR METALLIC POWDER
- B22F9/00—Making metallic powder or suspensions thereof
- B22F9/02—Making metallic powder or suspensions thereof using physical processes
- B22F9/06—Making metallic powder or suspensions thereof using physical processes starting from liquid material
- B22F9/08—Making metallic powder or suspensions thereof using physical processes starting from liquid material by casting, e.g. through sieves or in water, by atomising or spraying
- B22F9/082—Making metallic powder or suspensions thereof using physical processes starting from liquid material by casting, e.g. through sieves or in water, by atomising or spraying atomising using a fluid
-
- G—PHYSICS
- G01—MEASURING; TESTING
- G01N—INVESTIGATING OR ANALYSING MATERIALS BY DETERMINING THEIR CHEMICAL OR PHYSICAL PROPERTIES
- G01N33/00—Investigating or analysing materials by specific methods not covered by groups G01N1/00 - G01N31/00
- G01N33/20—Metals
- G01N33/202—Constituents thereof
- G01N33/2022—Non-metallic constituents
- G01N33/2025—Gaseous constituents
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10S—TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10S75/00—Specialized metallurgical processes, compositions for use therein, consolidated metal powder compositions, and loose metal particulate mixtures
- Y10S75/953—Producing spheres
Definitions
- This invention relates to the production of metal powders composed of spherically shaped particles. More particularly, the invention concerns a method for the manufacture of fine spherical aluminum powder.
- Finely divided metal powders such as, for example, aluminum, aluminum alloy, copper, magnesium, and tin powders, have numerous industrial applications, including powder metallurgy, pyrotechnics, flares, and solid fuel components. In these and other applications, it is generally desired to obtain products which are freeflowing, possess a high packing density and smooth surface, and which are spherical in shape.
- the particle initially formed is typically elongated in shape owing to the action of the high velocity gas stream which tears it away from the stream of molten metal issuing from the atomizing nozzle. If the oxygen or moisture is present in sufficient amount, an oxide envelope immediately forms, preventing normal surface tension forces within the molten metal particle from pulling the particle into a spherical shape, the shape having the minimum surface area. If the metal does not form an oxide film, the ini- ⁇ tially formed metal particle will draw itself into a sphere, providing it remains substantially molten and free of external forces for a period of time suflicient to permit sphere formation. Another important consideration is that certain metals from which it is desired to produce.
- the present invention provides a novel technique for the production of metal powder, utilizing conditions which promote the formation of spherical particles (by avoiding interference with the natural forces of surface tension during the critical spherodizing operation), and producing a product which may be safely handled in air.
- fine spherical particles are produced by disintegrating molten metal into fine particles and keeping the particles substantially molten long enough for the effects of surface tension to cause formation of spherical particles, progressively oxidizing the particles to form a protective coating.
- This may be accomplished, for example, by atomizing molten metal with a high velocity stream of gas inert to the metal, spherodizing and cooling the metal particles in an atmosphere having a maximum available oxygen content insufficient to interfere significantly with the forces of surface tension, and continuing the oxidation of the particles in an atmosphere having an amount of free oxygen below that which will support ignition.
- available oxygen means oxygen made available from gaseous oxygen compounds gas generator, a typical exothermic gas composition is:
- the desired sequence of steps may be carried out, in accordance with the invention, by discharging atomized particles of molten metal through a tubular shroud which provides a spherodizing zone, open to the air at the end of the tube opposite to that where the atomized particles .are introduced.
- the shroud may be an elongated tube through which the particles are projected in a continuous stream from the feed end of the tube to the discharge end.
- a gas such as the foregoing composition may be used for the atomizing gas, as well as for the atmosphere of the spherodizing zone; or the atomizing medium may be an inert gas which is substantially free of oxygen and water vapor, with the gas containing about 0.20.3% oxygen being admitted to the spherodizing zone through an independent inlet.
- the atomizing gas employed in accordance with one aspect of the invention is accordingly an inert gas containing a controlled amount of available oxygen, hereinafter referred to as substantially inert gas.
- This gas is discharged into the elongated zone, along with the disintegrated metal, providing within said zone an atmosphere containing available oxygen in an amount insufficient to interfere with normal surface tension forces of the particles causing sphere formation, and limiting the rate of oxide formation during the passage of the particles through the zone in whichsphere formation takes place.
- the limited amount of available oxygen in the gas serves as a means of providing controlled and progressive oxidation of the surfaces of the particles as they cool and are swept through the tube toward its exit.
- the method of the invention is adapted for the production of spherical metal particles generally, including such metals as copper, magnesium, and aluminum and aluminum alloys.
- metals as copper, magnesium, and aluminum and aluminum alloys.
- aluminum and aluminum base alloys including alloys with copper, tin, and magnesium.
- the invention permits the production of spherical aluminum and aluminum alloy powders in improved yield, with greater economy, and having desirable characteristics of spherical shape, smooth surface, high packing density, and free-flowing properties.
- a metal such as aluminum or an alloy of aluminum
- gas which is substantially inert to the metal, such as the aforementioned exothermic gas.
- An elongated metal tube may be employed, the diameter of which is small compared with its length, to provide a particle formation and oxidation zone.
- spherical particle formation takes place as the metal particles leave the atomization nozzle at high velocity, carried by a stream of the gas used for the atomization.
- solidification and cooling take place, together with progressive oxidation of the particle surfaces as the particles approach the discharge end of the tube.
- the spherical particles are withdrawn at the open end of the tube, and collected in a suitable collection system.
- the portion of the tube nearest the atomizing nozzle provides a region wherein the spheres are allowed to freeze so as to fix their geometry and also to withdraw most of their heat energy as they pass through it.
- the portion of the tube nearest the exit constitutes an oxidizing and cooling region.
- the metal spheres are swept along the length of the elongated tube by the action of the atomizing gas stream, passing through these two successive regions or sub-zones.
- the apparatus as shown in the drawing comprises an elongated metal tube 1, providing a particle formation and oxidation zone.
- Tube 1 has a feed end, defined by a partition 2, a continuous interior bore and an exit end 3.
- the tube is long in comparison with its diameter, the relative dimensions being exemplified, for instance, by a tube in diameter and 8 feet in length.
- Metal is heated in a pot 11 of a resistance furnace 12, the molten metal being withdrawn through pipe 13 into atomizing nozzle 14, which may be lined with a thin ceramic layer and which is provided with a ceramic tip 15, from which the molten metal is fed into tube 1.
- Surrounding the atomizing nozzle is a jacket 16 through which the atomizing gas is fed under pressure, causing disintegration of the molten metal.
- the gas is supplied through conduit 17, and the materials and nozzle may be heated by means of electrical heating elements shown generally at 18.
- the atomizing assembly projects through partition 2, which acts to seal off the particle .formation zone of the tube.
- the finished metal powder .is blown from the open end 3 of tube 1 and collected by any suitable collection system, not shown.
- the metal temperature will be about 300 to 700 F. above its melting point; and the nozzle temperature is maintained at about 1300l700 F.
- the gas temperature in the spherodizing zone should be not less than about 600 F., and preferably in the range of 6001200 F.
- Example 1 Molten aluminum at about 1840 F. was admitted to the atomizing nozzle and disintegrated by a stream of exothermic gas having the composition previously referred to. A suitable spherodizing zone was created by ejecting the atomizing gas and entrained particles through an elongated tube (as shown in the drawing). The gas was supplied under pressure of p.s.i., at a temperature of about F. Nozzle temperature was approximately 1620 F.
- the proportion of spherical particles was estimated to be about 60%, based upon microscopic examination.
- Example 2 In the manner of Example 1, molten aluminum at a temperature of about 1520 F. was atomized with dry exothermic gas at 60 p.s.i., the nozzle temperature being about 1700 F. Comparable results were obtained.
- Example 3 Following the procedure of Example 1, except that a manifold was added to the tubular shroud adjacent the nozzle and additional exothermic gas was thereby admitted to the spherodizing zone, aluminum at a temperature of about 1600 F. was atomized with gas at 600 F., 90 p.s.i. The use of this manifold arrangement was found to avoid pockets of reduced pressure and consequent turbulence adjacent the nozzle. The nozzle temperature was about 1500 F. and the temperature in the tube, 6 feet from the nozzle, was found to be 600 F.
- Example 4 Using the manifold arrangement and the same atomizing gas temperature and pressure of Example 3, aluminum at a temperature of about 1820 F. was atomized to yield 50% spherical particles. The nozzle temperature was about 1350 F. and the oxygen content in the tubular shroud, 6 feet from the nozzle, was found to be about 0.2%.
- the apparatus embodiment in the drawing shows the tube as cylindrical in configuration, but the tube can be flared outwardly toward the open end if desired.
- the length of the tube depends to some extent upon the pressure of the atomizing gas; and the requisite function it provides is to cause a shrouding of the metal particles with gas having a limited oxygen content.
- the tube cannot be too narrow, however, or the metal particles will coat the interior of the tube.
- Method of producing spherical metal powder which comprises subjecting molten metal to the action of a high velocity stream of exothermic gas containing nitrogen and carbon dioxide, to disintegrate the metal into fine particles, said gas providing available oxygen in an amount insufiicient to interfere with surface tension forces of the particles effecting sphere formation, and passing said gas stream and the particles of molten metal through a spherodizing zone to cause sphere formation and solidification of the spherical particles.
- the method which comprises discharging particles of molten aluminum from an atomizing nozzle, protecting the particles from premature oxidation while promoting the formation of spheres by maintaining said particles substantially in their molten condition within an atmosphere of exothermic gas consisting essentially of a mixture of nitrogen and carbon dioxide containing not more than about 0.3% oxygen by volume, said gas prw viding available oxygen in an amount insufficient to interfere with surface tension forces of the particles effecting sphere formation, and cooling the spherodized particles in said atmosphere to cause solidification of the aluminum and progressive oxidation of the spherical particle surfaces.
- exothermic gas consisting essentially of a mixture of nitrogen and carbon dioxide containing not more than about 0.3% oxygen by volume
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Description
Dec. 20, 1966 L. D. BYLUND ETAL PREPARATION 0F SPHERICAL METAL POWDER Filed Augl 16. 1962 INVENTORS LINTON D. BYLUND FRANClS BPETHWISCH WILLIAM FPWOOSLEY United States Patent s 293 334 PREPARATION OF SPHEIHCAL METAL POWDER Linton D. Bylund, Chesterfield County, and Francis B.
Rethwisch, Goochland County, Va., and William P.
This invention relates to the production of metal powders composed of spherically shaped particles. More particularly, the invention concerns a method for the manufacture of fine spherical aluminum powder.
Finely divided metal powders such as, for example, aluminum, aluminum alloy, copper, magnesium, and tin powders, have numerous industrial applications, including powder metallurgy, pyrotechnics, flares, and solid fuel components. In these and other applications, it is generally desired to obtain products which are freeflowing, possess a high packing density and smooth surface, and which are spherical in shape.
One of the known methods for the production of finely divided spherical metal powders is that of atomizing the molten metal, by means of a gas inert to the metal, into a closed chamber. In metal atomization as thus carried out, considerable stress has been laid on the necessity of avoiding surface oxidation of the molten metal, the thought being that the usefulness of the finished powder was impaired for some applications if the powder particles became excessively oxidized. It was also thought that the production of spherical metal powders, by the atomization of molten metal with inert gases containing small amounts of oxygen or nitrogen, was impeded by formation of metal oxides or nitrides through chemical reaction, causing clogging of the atomizing nozzle and other difficulties. Accordingly, elaborate purification systems have been proposed to remove impurities such as oxygen and nitrogen, especially from helium or argon inert gas, the purified inert gas then being recirculated to the main circulatory system.
In accordance with the present invention, however, it has been found that the presence of small amounts of oxygen during formation of particles from ,molten metal is not detrimental, provided oxidation of the metal is carefully controlled. The use of an atmosphere containing sufiicient available oxygen to achieve some oxidation of the particles can even be advantageous in producing fine powder, since the resulting oxide film affords protection from ignition or detonation of metals which are otherwise difiicult to handle with safety. The amount ofv available oxygen must be controlled very carefully, however, to avoid interference with normal surface tension forces in the particles of molten metal. -A practical upper limit appears to be'from about 0.2% to about 0.3% by volume of available oxygen.
When molten metal is atomized, the particle initially formed is typically elongated in shape owing to the action of the high velocity gas stream which tears it away from the stream of molten metal issuing from the atomizing nozzle. If the oxygen or moisture is present in sufficient amount, an oxide envelope immediately forms, preventing normal surface tension forces within the molten metal particle from pulling the particle into a spherical shape, the shape having the minimum surface area. If the metal does not form an oxide film, the ini-\ tially formed metal particle will draw itself into a sphere, providing it remains substantially molten and free of external forces for a period of time suflicient to permit sphere formation. Another important consideration is that certain metals from which it is desired to produce.
3,293,334 Patented Dec. 20, 1966 spherical powder, notably aluminum and magnesium, are ordinarily pyrophoric in their unoxidized condition. Accordingly, at the earliest practical stage of the production of powder from such metals it is desirable to at least partially oxidize or otherwise protect the particle surfaces, in the interests of safety and for convenience in subsequent handling operations.
The present invention provides a novel technique for the production of metal powder, utilizing conditions which promote the formation of spherical particles (by avoiding interference with the natural forces of surface tension during the critical spherodizing operation), and producing a product which may be safely handled in air.
In accordance with this invention, fine spherical particles are produced by disintegrating molten metal into fine particles and keeping the particles substantially molten long enough for the effects of surface tension to cause formation of spherical particles, progressively oxidizing the particles to form a protective coating. This may be accomplished, for example, by atomizing molten metal with a high velocity stream of gas inert to the metal, spherodizing and cooling the metal particles in an atmosphere having a maximum available oxygen content insufficient to interfere significantly with the forces of surface tension, and continuing the oxidation of the particles in an atmosphere having an amount of free oxygen below that which will support ignition.
As employed herein, the term available oxygen means oxygen made available from gaseous oxygen compounds gas generator, a typical exothermic gas composition is:
CO 11-12% by volume.
H O Saturated at discharge tempera ture.
Combustib'les (CO+H +CH 0.5% max.
0 No more than 0.3% (typically N Balance.
The desired sequence of steps may be carried out, in accordance with the invention, by discharging atomized particles of molten metal through a tubular shroud which provides a spherodizing zone, open to the air at the end of the tube opposite to that where the atomized particles .are introduced. The shroud may be an elongated tube through which the particles are projected in a continuous stream from the feed end of the tube to the discharge end.
A gas such as the foregoing composition may be used for the atomizing gas, as well as for the atmosphere of the spherodizing zone; or the atomizing medium may be an inert gas which is substantially free of oxygen and water vapor, with the gas containing about 0.20.3% oxygen being admitted to the spherodizing zone through an independent inlet.
The atomizing gas employed in accordance with one aspect of the invention is accordingly an inert gas containing a controlled amount of available oxygen, hereinafter referred to as substantially inert gas. This gas is discharged into the elongated zone, along with the disintegrated metal, providing within said zone an atmosphere containing available oxygen in an amount insufficient to interfere with normal surface tension forces of the particles causing sphere formation, and limiting the rate of oxide formation during the passage of the particles through the zone in whichsphere formation takes place. Thereafter, the limited amount of available oxygen in the gas serves as a means of providing controlled and progressive oxidation of the surfaces of the particles as they cool and are swept through the tube toward its exit.
The method of the invention is adapted for the production of spherical metal particles generally, including such metals as copper, magnesium, and aluminum and aluminum alloys. For purposes of illustration of the novel principles of the invention, reference will be made to aluminum and aluminum base alloys, including alloys with copper, tin, and magnesium.
The invention permits the production of spherical aluminum and aluminum alloy powders in improved yield, with greater economy, and having desirable characteristics of spherical shape, smooth surface, high packing density, and free-flowing properties.
In the practice of the invention, a metal such as aluminum or an alloy of aluminum, is melted in a resistance furnace and atomized by means of gas which is substantially inert to the metal, such as the aforementioned exothermic gas. An elongated metal tube may be employed, the diameter of which is small compared with its length, to provide a particle formation and oxidation zone. In this elongated zone, spherical particle formation takes place as the metal particles leave the atomization nozzle at high velocity, carried by a stream of the gas used for the atomization. As the stream of particles moves rapidly down the length of the tube, solidification and cooling take place, together with progressive oxidation of the particle surfaces as the particles approach the discharge end of the tube. Finally the spherical particles are withdrawn at the open end of the tube, and collected in a suitable collection system.
Thus, the portion of the tube nearest the atomizing nozzle provides a region wherein the spheres are allowed to freeze so as to fix their geometry and also to withdraw most of their heat energy as they pass through it.
The portion of the tube nearest the exit constitutes an oxidizing and cooling region. The metal spheres are swept along the length of the elongated tube by the action of the atomizing gas stream, passing through these two successive regions or sub-zones.
The method of the invention may be more readily understood by reference to the accompanying drawing, which is a length-wise view of the apparatus in cross-section, showing the metal supply, atomizing system, and tube arrangement.
The apparatus as shown in the drawing comprises an elongated metal tube 1, providing a particle formation and oxidation zone. Tube 1 has a feed end, defined by a partition 2, a continuous interior bore and an exit end 3. The tube :is long in comparison with its diameter, the relative dimensions being exemplified, for instance, by a tube in diameter and 8 feet in length. Metal is heated in a pot 11 of a resistance furnace 12, the molten metal being withdrawn through pipe 13 into atomizing nozzle 14, which may be lined with a thin ceramic layer and which is provided with a ceramic tip 15, from which the molten metal is fed into tube 1. Surrounding the atomizing nozzle is a jacket 16 through which the atomizing gas is fed under pressure, causing disintegration of the molten metal. The gas is supplied through conduit 17, and the materials and nozzle may be heated by means of electrical heating elements shown generally at 18. The atomizing assembly projects through partition 2, which acts to seal off the particle .formation zone of the tube. The finished metal powder .is blown from the open end 3 of tube 1 and collected by any suitable collection system, not shown.
Specific operating conditions will vary 'with such factors as the particular metal being atomized, the orifice size of the nozzle, and temperature and pressure of the atomizing gas. For purposes of illustration, however, using aluminumas an example, the metal temperature will be about 300 to 700 F. above its melting point; and the nozzle temperature is maintained at about 1300l700 F.
The gas temperature in the spherodizing zone should be not less than about 600 F., and preferably in the range of 6001200 F.
The following examples are illustrative of suitable operating conditions in the atomizing of commercial purity aluminum: I
Example 1 Molten aluminum at about 1840 F. was admitted to the atomizing nozzle and disintegrated by a stream of exothermic gas having the composition previously referred to. A suitable spherodizing zone was created by ejecting the atomizing gas and entrained particles through an elongated tube (as shown in the drawing). The gas was supplied under pressure of p.s.i., at a temperature of about F. Nozzle temperature was approximately 1620 F.
The proportion of spherical particles was estimated to be about 60%, based upon microscopic examination.
Example 2 In the manner of Example 1, molten aluminum at a temperature of about 1520 F. was atomized with dry exothermic gas at 60 p.s.i., the nozzle temperature being about 1700 F. Comparable results were obtained.
Example 3 Following the procedure of Example 1, except that a manifold was added to the tubular shroud adjacent the nozzle and additional exothermic gas was thereby admitted to the spherodizing zone, aluminum at a temperature of about 1600 F. was atomized with gas at 600 F., 90 p.s.i. The use of this manifold arrangement was found to avoid pockets of reduced pressure and consequent turbulence adjacent the nozzle. The nozzle temperature was about 1500 F. and the temperature in the tube, 6 feet from the nozzle, was found to be 600 F.
Example 4 Using the manifold arrangement and the same atomizing gas temperature and pressure of Example 3, aluminum at a temperature of about 1820 F. was atomized to yield 50% spherical particles. The nozzle temperature was about 1350 F. and the oxygen content in the tubular shroud, 6 feet from the nozzle, was found to be about 0.2%.
The apparatus embodiment in the drawing shows the tube as cylindrical in configuration, but the tube can be flared outwardly toward the open end if desired. The length of the tube depends to some extent upon the pressure of the atomizing gas; and the requisite function it provides is to cause a shrouding of the metal particles with gas having a limited oxygen content. The tube cannot be too narrow, however, or the metal particles will coat the interior of the tube.
While present preferred embodiments of the invention have been illustrated and described, it will be appreciated that the invention may be otherwise variously embodied and practiced within the scope of the following claims.
What is claimed is:
1. Method of producing spherical metal powder, which comprises subjecting molten metal to the action of a high velocity stream of exothermic gas containing nitrogen and carbon dioxide, to disintegrate the metal into fine particles, said gas providing available oxygen in an amount insufiicient to interfere with surface tension forces of the particles effecting sphere formation, and passing said gas stream and the particles of molten metal through a spherodizing zone to cause sphere formation and solidification of the spherical particles.
ture of nitrogen and carbon dioxide containing a small amount of oxygen not exceeding about 0.3% by volume, said gas providing available oxygen in an amount insufiicient to interfere with surface tension forces of the particles effecting sphere formation, passing said particles and gas stream through a tubular spherodizin-g zone open to air at the end opposite the feeding end, causing solidification of spherical particles in said Zone and progressive -oxidation of the spherical particle surfaces, and collecting ing the finished particles at the open end of the zone.
3. The method of claim 2, in which the metal is a member selected from the group consisting of aluminum and aluminum alloys.
4. In the atomizing of molten aluminum to produce aluminum powder, the method which comprises discharging particles of molten aluminum from an atomizing nozzle, protecting the particles from premature oxidation while promoting the formation of spheres by maintaining said particles substantially in their molten condition within an atmosphere of exothermic gas consisting essentially of a mixture of nitrogen and carbon dioxide containing not more than about 0.3% oxygen by volume, said gas prw viding available oxygen in an amount insufficient to interfere with surface tension forces of the particles effecting sphere formation, and cooling the spherodized particles in said atmosphere to cause solidification of the aluminum and progressive oxidation of the spherical particle surfaces.
5. The method of claim 4, in which said exothermic gas contains about 11-12% carbon dioxide, about 0.2% oxygen, balance substantially nitrogen.
6. The method of claim 4, in which said exothermic gas contains not more than about 0.5% combustibles,
7. The method of claim 1, in which said exothermic gas contains about 1112% carbon dioxide, balance substantially nitrogen.
References Cited by the Examiner UNITED STATES PATENTS 2,529,466 11/1950 Weldon l847.2 2,538,345 1/1951 Whaley 1847.2 2,638,630 5/1953 Golwynee 264-12 3,070,837 1/ 1963 Loertscher et a1 182.7 3,071,804 1/1963 Meek 182.7
ROBERT F. WHITE, Primary Examiner.
MORRIS LIEBMAN, ALEXANDER H. BRODMER- KEL, C. B. HAMBURG, .I. R. HALL, Examiners,
Claims (1)
1. METHOD OF PRODUCING SPHERICAL METAL POWDER, WHICH COMPRISES SUBJECTING MOLTEN METAL TO THE ACTION OF A HIGH VELOCITY STREAM OF EXOTHERMIC GAS CONTAINING NITROGEN AND CARBON DIOXIDE, TO DISINTEGRATE THE METAL INTO FINE PARTICLES, SAID GAS PROVIDING AVAILABLE OXYGEN IN AN AMOUNT INSUFFICIENT TO INTERFERE WITH SURFACE TENSION FORCES OF THE PARTICLES EFFECTING SPHERE FORMATION, AND PASSING SAID GAS STREAM AND THE PARTICLES OF MOLTEN METAL THROUGH A SPHERODIZING ZONE TO CAUSE SPHERE FORMATION AND SOLIDIFICATION OF THE SPHERICAL PARTICLES.
Priority Applications (2)
Application Number | Priority Date | Filing Date | Title |
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US217415A US3293334A (en) | 1962-08-16 | 1962-08-16 | Preparation of spherical metal powder |
US559011A US3344469A (en) | 1962-08-16 | 1966-02-07 | Apparatus for production of fine spherical metal particles |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
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US217415A US3293334A (en) | 1962-08-16 | 1962-08-16 | Preparation of spherical metal powder |
Publications (1)
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US3293334A true US3293334A (en) | 1966-12-20 |
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US217415A Expired - Lifetime US3293334A (en) | 1962-08-16 | 1962-08-16 | Preparation of spherical metal powder |
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Cited By (30)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
FR2532209A1 (en) * | 1982-08-31 | 1984-03-02 | Aluminum Co Of America | PROCESS AND DEVICE FOR OBTAINING ATOMIZED METAL POWDER |
US4449902A (en) * | 1982-11-12 | 1984-05-22 | Aluminum Company Of America | Apparatus for control of particle size in the production of atomized metal |
US4457881A (en) * | 1982-09-10 | 1984-07-03 | Aluminum Company Of America | Method for collection of atomized metal particles |
US4464103A (en) * | 1982-08-31 | 1984-08-07 | Aluminum Company Of America | Apparatus for the production of atomized metal particles |
US4466786A (en) * | 1982-08-31 | 1984-08-21 | Aluminum Company Of America | Apparatus for production of atomized powder |
US4468182A (en) * | 1982-08-31 | 1984-08-28 | Aluminum Company Of America | Apparatus for control of powder production |
US4468183A (en) * | 1982-08-31 | 1984-08-28 | Aluminum Company Of America | Apparatus for the production of particulate metal |
WO1985000884A1 (en) * | 1983-08-12 | 1985-02-28 | Kenney George B | Device and method for in-process multi-element analysis of molten metal and other liquid materials |
US4548768A (en) * | 1982-08-31 | 1985-10-22 | Aluminum Company Of America | Method for the production of atomized metal particles |
US4576767A (en) * | 1982-08-31 | 1986-03-18 | Aluminum Company Of America | Method for controlling powder production |
US4585601A (en) * | 1982-08-31 | 1986-04-29 | Aluminum Company Of America | Method for controlling the production of atomized powder |
US4606869A (en) * | 1984-08-27 | 1986-08-19 | The New Jersey Zinc Company | Method of making air atomized spherical zinc powder |
US4631013A (en) * | 1984-02-29 | 1986-12-23 | General Electric Company | Apparatus for atomization of unstable melt streams |
US4919854A (en) * | 1985-09-24 | 1990-04-24 | Dr.-Ing. Luder Gerking | Method for producing superfine powder in spherical form |
US20180180279A1 (en) * | 2014-06-03 | 2018-06-28 | Siemens Aktiengesellschaft | Pumpless Metal Atomization And Combustion Using Vacuum Generation And Suitable Material Flow Control |
US10639712B2 (en) | 2018-06-19 | 2020-05-05 | Amastan Technologies Inc. | Process for producing spheroidized powder from feedstock materials |
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US11311938B2 (en) | 2019-04-30 | 2022-04-26 | 6K Inc. | Mechanically alloyed powder feedstock |
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US11611130B2 (en) | 2019-04-30 | 2023-03-21 | 6K Inc. | Lithium lanthanum zirconium oxide (LLZO) powder |
US11717886B2 (en) | 2019-11-18 | 2023-08-08 | 6K Inc. | Unique feedstocks for spherical powders and methods of manufacturing |
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US12042861B2 (en) | 2021-03-31 | 2024-07-23 | 6K Inc. | Systems and methods for additive manufacturing of metal nitride ceramics |
US12094688B2 (en) | 2022-08-25 | 2024-09-17 | 6K Inc. | Plasma apparatus and methods for processing feed material utilizing a powder ingress preventor (PIP) |
US12195338B2 (en) | 2022-12-15 | 2025-01-14 | 6K Inc. | Systems, methods, and device for pyrolysis of methane in a microwave plasma for hydrogen and structured carbon powder production |
US12261023B2 (en) | 2022-05-23 | 2025-03-25 | 6K Inc. | Microwave plasma apparatus and methods for processing materials using an interior liner |
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Cited By (43)
Publication number | Priority date | Publication date | Assignee | Title |
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US4548768A (en) * | 1982-08-31 | 1985-10-22 | Aluminum Company Of America | Method for the production of atomized metal particles |
US4464103A (en) * | 1982-08-31 | 1984-08-07 | Aluminum Company Of America | Apparatus for the production of atomized metal particles |
US4576767A (en) * | 1982-08-31 | 1986-03-18 | Aluminum Company Of America | Method for controlling powder production |
US4466786A (en) * | 1982-08-31 | 1984-08-21 | Aluminum Company Of America | Apparatus for production of atomized powder |
US4468182A (en) * | 1982-08-31 | 1984-08-28 | Aluminum Company Of America | Apparatus for control of powder production |
US4468183A (en) * | 1982-08-31 | 1984-08-28 | Aluminum Company Of America | Apparatus for the production of particulate metal |
US4585601A (en) * | 1982-08-31 | 1986-04-29 | Aluminum Company Of America | Method for controlling the production of atomized powder |
FR2532209A1 (en) * | 1982-08-31 | 1984-03-02 | Aluminum Co Of America | PROCESS AND DEVICE FOR OBTAINING ATOMIZED METAL POWDER |
US4457881A (en) * | 1982-09-10 | 1984-07-03 | Aluminum Company Of America | Method for collection of atomized metal particles |
US4449902A (en) * | 1982-11-12 | 1984-05-22 | Aluminum Company Of America | Apparatus for control of particle size in the production of atomized metal |
US4578022A (en) * | 1983-08-12 | 1986-03-25 | Kenney George B | Apparatus for in-process multi-element analysis of molten metal and other liquid materials |
WO1985000884A1 (en) * | 1983-08-12 | 1985-02-28 | Kenney George B | Device and method for in-process multi-element analysis of molten metal and other liquid materials |
US4636339A (en) * | 1983-08-12 | 1987-01-13 | Metallurgical Instruments, Inc. | Method for in-process multi-element analysis of molten metal and other liquid materials |
EP0135097A3 (en) * | 1983-08-12 | 1987-04-15 | George B. Kenney | Device and method for in-process, multi-element analysis of molten metal and other liquid materials |
AU577540B2 (en) * | 1983-08-12 | 1988-09-29 | George B. Kenney | Multi-element molten metal analysis molten metal and other liquid materials |
US4631013A (en) * | 1984-02-29 | 1986-12-23 | General Electric Company | Apparatus for atomization of unstable melt streams |
US4606869A (en) * | 1984-08-27 | 1986-08-19 | The New Jersey Zinc Company | Method of making air atomized spherical zinc powder |
US4919854A (en) * | 1985-09-24 | 1990-04-24 | Dr.-Ing. Luder Gerking | Method for producing superfine powder in spherical form |
US20180180279A1 (en) * | 2014-06-03 | 2018-06-28 | Siemens Aktiengesellschaft | Pumpless Metal Atomization And Combustion Using Vacuum Generation And Suitable Material Flow Control |
US10987735B2 (en) | 2015-12-16 | 2021-04-27 | 6K Inc. | Spheroidal titanium metallic powders with custom microstructures |
US12214420B2 (en) | 2015-12-16 | 2025-02-04 | 6K Inc. | Spheroidal titanium metallic powders with custom microstructures |
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US11577314B2 (en) | 2015-12-16 | 2023-02-14 | 6K Inc. | Spheroidal titanium metallic powders with custom microstructures |
US11839919B2 (en) | 2015-12-16 | 2023-12-12 | 6K Inc. | Spheroidal dehydrogenated metals and metal alloy particles |
US11273491B2 (en) | 2018-06-19 | 2022-03-15 | 6K Inc. | Process for producing spheroidized powder from feedstock materials |
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US10639712B2 (en) | 2018-06-19 | 2020-05-05 | Amastan Technologies Inc. | Process for producing spheroidized powder from feedstock materials |
US11311938B2 (en) | 2019-04-30 | 2022-04-26 | 6K Inc. | Mechanically alloyed powder feedstock |
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US11633785B2 (en) | 2019-04-30 | 2023-04-25 | 6K Inc. | Mechanically alloyed powder feedstock |
US11717886B2 (en) | 2019-11-18 | 2023-08-08 | 6K Inc. | Unique feedstocks for spherical powders and methods of manufacturing |
US11590568B2 (en) | 2019-12-19 | 2023-02-28 | 6K Inc. | Process for producing spheroidized powder from feedstock materials |
US12176529B2 (en) | 2020-06-25 | 2024-12-24 | 6K Inc. | Microcomposite alloy structure |
US11855278B2 (en) | 2020-06-25 | 2023-12-26 | 6K, Inc. | Microcomposite alloy structure |
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US11919071B2 (en) | 2020-10-30 | 2024-03-05 | 6K Inc. | Systems and methods for synthesis of spheroidized metal powders |
US12042861B2 (en) | 2021-03-31 | 2024-07-23 | 6K Inc. | Systems and methods for additive manufacturing of metal nitride ceramics |
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