USH1086H - Collision centrifugal atomization unit - Google Patents

Collision centrifugal atomization unit Download PDF

Info

Publication number
USH1086H
USH1086H US07/832,266 US83226692A USH1086H US H1086 H USH1086 H US H1086H US 83226692 A US83226692 A US 83226692A US H1086 H USH1086 H US H1086H
Authority
US
United States
Prior art keywords
droplets
substrate
gas
chamber
feeder
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.)
Abandoned
Application number
US07/832,266
Inventor
Monde A. Otooni
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.)
United States Department of the Army
Original Assignee
United States Department of the Army
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 United States Department of the Army filed Critical United States Department of the Army
Priority to US07/832,266 priority Critical patent/USH1086H/en
Application granted granted Critical
Publication of USH1086H publication Critical patent/USH1086H/en
Abandoned legal-status Critical Current

Links

Images

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B22CASTING; POWDER METALLURGY
    • B22FWORKING METALLIC POWDER; MANUFACTURE OF ARTICLES FROM METALLIC POWDER; MAKING METALLIC POWDER; APPARATUS OR DEVICES SPECIALLY ADAPTED FOR METALLIC POWDER
    • B22F9/00Making metallic powder or suspensions thereof
    • B22F9/02Making metallic powder or suspensions thereof using physical processes
    • B22F9/06Making metallic powder or suspensions thereof using physical processes starting from liquid material
    • B22F9/08Making 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
    • B22F9/10Making 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 using centrifugal force
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B22CASTING; POWDER METALLURGY
    • B22FWORKING METALLIC POWDER; MANUFACTURE OF ARTICLES FROM METALLIC POWDER; MAKING METALLIC POWDER; APPARATUS OR DEVICES SPECIALLY ADAPTED FOR METALLIC POWDER
    • B22F1/00Metallic powder; Treatment of metallic powder, e.g. to facilitate working or to improve properties
    • B22F1/05Metallic powder characterised by the size or surface area of the particles
    • B22F1/054Nanosized particles
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B22CASTING; POWDER METALLURGY
    • B22FWORKING METALLIC POWDER; MANUFACTURE OF ARTICLES FROM METALLIC POWDER; MAKING METALLIC POWDER; APPARATUS OR DEVICES SPECIALLY ADAPTED FOR METALLIC POWDER
    • B22F1/00Metallic powder; Treatment of metallic powder, e.g. to facilitate working or to improve properties
    • B22F1/08Metallic powder characterised by particles having an amorphous microstructure
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B22CASTING; POWDER METALLURGY
    • B22FWORKING METALLIC POWDER; MANUFACTURE OF ARTICLES FROM METALLIC POWDER; MAKING METALLIC POWDER; APPARATUS OR DEVICES SPECIALLY ADAPTED FOR METALLIC POWDER
    • B22F9/00Making metallic powder or suspensions thereof
    • B22F9/02Making metallic powder or suspensions thereof using physical processes
    • B22F9/06Making metallic powder or suspensions thereof using physical processes starting from liquid material
    • B22F9/08Making 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
    • B22F9/082Making 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
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B82NANOTECHNOLOGY
    • B82YSPECIFIC USES OR APPLICATIONS OF NANOSTRUCTURES; MEASUREMENT OR ANALYSIS OF NANOSTRUCTURES; MANUFACTURE OR TREATMENT OF NANOSTRUCTURES
    • B82Y30/00Nanotechnology for materials or surface science, e.g. nanocomposites
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B22CASTING; POWDER METALLURGY
    • B22FWORKING METALLIC POWDER; MANUFACTURE OF ARTICLES FROM METALLIC POWDER; MAKING METALLIC POWDER; APPARATUS OR DEVICES SPECIALLY ADAPTED FOR METALLIC POWDER
    • B22F2202/00Treatment under specific physical conditions
    • B22F2202/01Use of vibrations

Definitions

  • the present invention relates to apparatus for producing amorphous and ultra fine rapidly solidified alloys, and more particularly to apparatus and a method for producing such alloys as small as submicron or smaller sized particles.
  • Another object of this invention is to provide apparatus for producing a near net shape, rapidly solidified alloys in bulk quantity.
  • Yet another object of the present invention is to provide apparatus for such a product in which subsequent annealing and changing the microstructures of the specimen when desired becomes feasible.
  • the apparatus of this invention includes a feeder unit in which liquid metal from a melt pool is interjected into a chamber in a vertical direction with respect to the length of the chamber from an atomizing circular nozzle with its attendant gas pressure.
  • gas flow accelerators introduce high velocity gas axially along the chamber.
  • the molten liquid alloy is subjected to several strong forces which form it into atomized powder.
  • This ultra fine dispersion is then impacted on a rotating, cooled substrate.
  • the substrate is provided with means to translate the location of the substrate axially in order to maintain an exact and same line of particle flight during deposition of the alloy on the substrate.
  • the alloy is finely dispersed in the chamber as a result of many forces which all act cooperatively to form the ultra small particles. Submicron sizes are readily achievable by this invention.
  • the alloy comes in a molten state from the liquid metal reservoir and is met with a gas stream and and ultrasonically pulsed jets of gas from the circular nozzle. As this atomized powder enters vertically or radially with respect to the axis, it is impacted with gas flowing under controlled acceleration conditions. The droplets are accelerated and undergo many collisions with each other, further reducing the particle size.
  • the particles or droplets impact on the target substrate, under controlled conditions of flight length, they are further subject to shear by the centrifugal force of the substrate as it rotates about the axis of the chamber.
  • FIG. 1 illustrates a side elevational view, partially in section, of the chamber and the preferred embodiment, showing a revolving nozzle on one end and, in partial section, the cooled substrate unit on the other end of the chamber;
  • FIG. 2 illustrates an enlarged, side elevational view, partially cut away, of the substrate unit of the chamber of FIG. 1;
  • FIG. 3 illustrates a greatly enlarged, schematic view of the feed unit of FIG. 1 and shown in the dot and dash circle and labeled FIG. 3.
  • the apparatus of the present invention includes four basic parts.
  • the alloy in introduced into the apparatus by a feeder.
  • the feeder has associated with it various gas nozzles.
  • the alloy is fed into the main chamber, atomized and is interacted with a gas flow accelerator.
  • the droplet alloy then impacts on a rotating substrate with its associated cooling and translation facilities.
  • the unit provides for submicron or even smaller metal droplets which are produced as a result of these several on going processes in the main chamber.
  • a series of of serially positioned vertical or radial nozzles atomize the metal droplets.
  • the chamber is preferably cylindrical and has an axis which defines the vertical or radial direction of the inlet nozzles.
  • the entering droplets moving as a result of controlled gas pressure, will then be subjected to a transporting high pressure gas flow emanating from a series of coaxially positioned gas flow nozzles from the end or base of the cylinder or chamber.
  • Inert gas such as nitrogen, helium or argon causes collision and shearing and transportation of the metal droplets.
  • the device shown generally by reference number 10 includes a chamber 11, shown in the preferred embodiment as a cylinder having a longitudinal axis 13.
  • Chamber 11 has a feeder unit 15 which brings the molten alloy into the chamber as will be described below.
  • Chamber 11 has a gas flow accelerator at one end, comprising a perforated disc 17 which houses gas nozzles to inject the inert gas as described above.
  • Disc 17 provides a source of gas which accelerates the droplets of alloy from feeder unit 15 and causes collisions between particles as well as controlling the velocity of the particles as they move toward substrate 19 at the other end of chamber 11.
  • Substrate 19 forms one part of the end unit, as all of the alloy being atomized is directed on to the surface 19.
  • Outer shell 21 provides support and mounts the substrate 19 in chamber 11, and at the same time incloses liquid nitrogen cooling coils 23.
  • the liquid nitrogen which is the preferred cooling means, is formed as a reservoir at the back of substrate 19, so that it is maintained at a constant temperature.
  • Substrate 19 is mounted at its other end to shaft 25 and shaft 25 rotates in the direction of arrow 27 to impart the centrifugal forces to the impinging droplets as described above.
  • Shaft 25 is also adapted to move axially along axis 13 to adjust or maintain the precise location of the surface of substrate 19 as the bulk production of rapidly solidified materials takes place. This insures that the particle line of flight is kept constant during deposition of alloy.
  • Feeder unit 15 has a main feeder tube 31 where liquid metal is transferred from a reservoir where the metal is maintained at the proper temperature.
  • the metal is subjected to a gas stream 33 of the same type as used in disc 17 and the nozzles associated therewith. Gas in gas stream 33 causes particle formation and moves the droplets into chamber 11.
  • an ultrasonically pulsed jet of gas 35 which serves to introduce the droplets into the chamber.
  • the cooperative effect of gas stream 33 and pulsed gas jet 35 causes the molten alloy to form an atomized powder 37.
  • gas from disc 17 acts to further reduce the size of the particles or droplets.
  • the equipment operates as follows.
  • the feeder units 15, and there may be four or eight or other numbers of units surrounding the chamber 11, will be heated to the required temperature to produce required alloy melt.
  • the circular jet nozzles in disc 17 will be activated prior to allowing the droplets to enter chamber 11.
  • Substrate 19, which has been cooled by liquid nitrogen coils 23 begins to rotate about shaft 25, and is maintained at a predetermined rpm.
  • the feeder valves are opened and the final submicron or smaller products are produced in bulk.
  • Shaft 25 not only rotates but maintains the alignment of substrate 19 in relation to the feeder unit 15 to maintain precision in production.

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Nanotechnology (AREA)
  • Crystallography & Structural Chemistry (AREA)
  • Inorganic Chemistry (AREA)
  • Physics & Mathematics (AREA)
  • Composite Materials (AREA)
  • Condensed Matter Physics & Semiconductors (AREA)
  • General Physics & Mathematics (AREA)
  • Materials Engineering (AREA)
  • Manufacture Of Metal Powder And Suspensions Thereof (AREA)

Abstract

Apparatus and a method for producing submicron and smaller metal alloy pacles using a main chamber having a longitudinal axis and a feeder for introducing a quantity of molten alloy under pulsed gas pressure in a direction generally radial to the axis. The feeder has a gas stream for forming metal droplets from said alloy. A gas accelerator directs axially flowing gas against the droplets from the feeder in the chamber. The accelerator directs the droplets in an axial direction to a substrate located along the axis and in the direction of flow from the accelerator to receive the droplets at a predetermined distance from the feeder, whereby the particles are produced.

Description

GOVERNMENTAL INTEREST
The invention described herein may be manufactured, used, and licensed by or for the Government for Government purposes without payment to me of any royalties thereon.
FIELD OF THE INVENTION
The present invention relates to apparatus for producing amorphous and ultra fine rapidly solidified alloys, and more particularly to apparatus and a method for producing such alloys as small as submicron or smaller sized particles.
BACKGROUND OF THE INVENTION
Ever since the beginning of rapid solidification technology became into being and began to be used, there have been several major problems which have prevented full industrial acceptance of the process. Apparatus has not been available which produces the products as they have been envisioned in the laboratory and in theory.
Primarily, the prior art methods and apparatus produce a microstructure which is not at all uniform. Grain size and dimensions are far too large at at the present time. At its simplest, the problem is stated as the lack of know how to produce near net shape product.
In prior art methods and apparatus, the atomization process produces droplets of varying size on any given substrate. In present systems, as deposition takes place, the length of the droplet trajectory becomes varied. Consequently, the thermal history of the deposit will not be the same throughout the specimen.
One important feature of the process of atomizing alloys is that it is necessary to control the flow parameters such as velocity and configuration of flow lines in order to cause collisions of higher intensity and thereby produce finer particles. To date, that has not been effective.
Accordingly, it is an object of this invention to produce new apparatus for producing ultra fine to amorphous alloys with uniform microstructures.
Another object of this invention is to provide apparatus for producing a near net shape, rapidly solidified alloys in bulk quantity.
Yet another object of the present invention is to provide apparatus for such a product in which subsequent annealing and changing the microstructures of the specimen when desired becomes feasible.
Other objects will appear hereinafter.
SUMMARY OF THE INVENTION
It has now been discovered that the above and other objects of the present invention may be accomplished in the following manner. Specifically, a new apparatus for manufacturing submicron metal alloy products of the type described has been discovered, and a method of making these products using the apparatus.
The apparatus of this invention includes a feeder unit in which liquid metal from a melt pool is interjected into a chamber in a vertical direction with respect to the length of the chamber from an atomizing circular nozzle with its attendant gas pressure.
At the same time, gas flow accelerators introduce high velocity gas axially along the chamber. The molten liquid alloy is subjected to several strong forces which form it into atomized powder. This ultra fine dispersion is then impacted on a rotating, cooled substrate. In the preferred embodiment, the substrate is provided with means to translate the location of the substrate axially in order to maintain an exact and same line of particle flight during deposition of the alloy on the substrate.
The alloy is finely dispersed in the chamber as a result of many forces which all act cooperatively to form the ultra small particles. Submicron sizes are readily achievable by this invention. The alloy comes in a molten state from the liquid metal reservoir and is met with a gas stream and and ultrasonically pulsed jets of gas from the circular nozzle. As this atomized powder enters vertically or radially with respect to the axis, it is impacted with gas flowing under controlled acceleration conditions. The droplets are accelerated and undergo many collisions with each other, further reducing the particle size.
Finally, as the particles or droplets impact on the target substrate, under controlled conditions of flight length, they are further subject to shear by the centrifugal force of the substrate as it rotates about the axis of the chamber.
BRIEF DESCRIPTION OF THE DRAWINGS
For a more complete understanding of the invention, reference is hereby made to the drawings, in which:
FIG. 1 illustrates a side elevational view, partially in section, of the chamber and the preferred embodiment, showing a revolving nozzle on one end and, in partial section, the cooled substrate unit on the other end of the chamber;
FIG. 2 illustrates an enlarged, side elevational view, partially cut away, of the substrate unit of the chamber of FIG. 1; and
FIG. 3 illustrates a greatly enlarged, schematic view of the feed unit of FIG. 1 and shown in the dot and dash circle and labeled FIG. 3.
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENT
The apparatus of the present invention includes four basic parts. The alloy in introduced into the apparatus by a feeder. The feeder has associated with it various gas nozzles. The alloy is fed into the main chamber, atomized and is interacted with a gas flow accelerator. The droplet alloy then impacts on a rotating substrate with its associated cooling and translation facilities.
The unit provides for submicron or even smaller metal droplets which are produced as a result of these several on going processes in the main chamber. As will be shown, a series of of serially positioned vertical or radial nozzles atomize the metal droplets. The chamber is preferably cylindrical and has an axis which defines the vertical or radial direction of the inlet nozzles.
The entering droplets, moving as a result of controlled gas pressure, will then be subjected to a transporting high pressure gas flow emanating from a series of coaxially positioned gas flow nozzles from the end or base of the cylinder or chamber. Inert gas, such as nitrogen, helium or argon causes collision and shearing and transportation of the metal droplets.
The droplets are controlled accurately by the gas flow parameters and will experience production, collision and motions in several directions. The controlled droplets are then deposited on a rotating, cooled axially moving substrate. The purpose of the axial translation is to keep the distance of the source to the deposition place or substrate always constant. This results in production of either a near net-shaped specimens and/or the desired particle size. The rotation of the substrate will cause centrifugally generated forces to shear the depositing droplets to shear further during impact with the substrate.
Turning now to FIG. 1, the device shown generally by reference number 10 includes a chamber 11, shown in the preferred embodiment as a cylinder having a longitudinal axis 13. Chamber 11 has a feeder unit 15 which brings the molten alloy into the chamber as will be described below. Chamber 11 has a gas flow accelerator at one end, comprising a perforated disc 17 which houses gas nozzles to inject the inert gas as described above. Disc 17 provides a source of gas which accelerates the droplets of alloy from feeder unit 15 and causes collisions between particles as well as controlling the velocity of the particles as they move toward substrate 19 at the other end of chamber 11.
Substrate 19 forms one part of the end unit, as all of the alloy being atomized is directed on to the surface 19. Outer shell 21 provides support and mounts the substrate 19 in chamber 11, and at the same time incloses liquid nitrogen cooling coils 23. The liquid nitrogen, which is the preferred cooling means, is formed as a reservoir at the back of substrate 19, so that it is maintained at a constant temperature.
Substrate 19 is mounted at its other end to shaft 25 and shaft 25 rotates in the direction of arrow 27 to impart the centrifugal forces to the impinging droplets as described above. Shaft 25 is also adapted to move axially along axis 13 to adjust or maintain the precise location of the surface of substrate 19 as the bulk production of rapidly solidified materials takes place. This insures that the particle line of flight is kept constant during deposition of alloy.
The other end 17 of chamber 11 is also rotating in the direction of arrow 27, and this rotation is independently controlled to control the collision and acceleration of droplets in chamber 11. As the alloy enters from feeder unit 15, it is subjected to these forces, substantially improving the operation of the process and apparatus.
Turning now to FIG. 3, the action of the feeder unit is seen in greater detail. Feeder unit 15 has a main feeder tube 31 where liquid metal is transferred from a reservoir where the metal is maintained at the proper temperature. The metal is subjected to a gas stream 33 of the same type as used in disc 17 and the nozzles associated therewith. Gas in gas stream 33 causes particle formation and moves the droplets into chamber 11.
Also impinging on the droplets in this unit is an ultrasonically pulsed jet of gas 35 which serves to introduce the droplets into the chamber. The cooperative effect of gas stream 33 and pulsed gas jet 35 causes the molten alloy to form an atomized powder 37. As powder 37 enters fully into chamber 11, gas from disc 17 acts to further reduce the size of the particles or droplets. First there is a collision of primary droplets, caused by gas from disc 17. Then there is the formation of secondary, smaller droplets as the primary droplets hit substrate 19. In this manner, the microstructures produced as superior to any produced by known methods.
The equipment operates as follows. The feeder units 15, and there may be four or eight or other numbers of units surrounding the chamber 11, will be heated to the required temperature to produce required alloy melt. The circular jet nozzles in disc 17 will be activated prior to allowing the droplets to enter chamber 11. Substrate 19, which has been cooled by liquid nitrogen coils 23 begins to rotate about shaft 25, and is maintained at a predetermined rpm. The feeder valves are opened and the final submicron or smaller products are produced in bulk. Shaft 25 not only rotates but maintains the alignment of substrate 19 in relation to the feeder unit 15 to maintain precision in production.
While particular embodiments of the present invention have been illustrated and described, it is not intended to limit the invention, except as defined by the following claims.

Claims (6)

What is claimed is:
1. The method of producing submicron and smaller metal alloy particles, comprising the steps of:
providing a main chamber means having a longitudinal axis;
introducing a quantity of molten alloy under pulsed gas pressure in a direction generally radial to said axis, and forming metal droplets from said alloy by said gas;
directing axially flowing gas against said droplets in said chamber in an axial direction; and
impacting said droplets on a substrate located along said axis and in the direction of flow of gas at a predetermined distance from said feeder means, whereby said particles are produced.
2. The method of claim 1, wherein said substrate is cooled to a low temperature.
3. The method of claim 2, wherein said cooling is from liquid nitrogen coils.
4. The method of claim 1, wherein said substrate is rotated to impart centrifugal force to droplets impinging on said substrate.
5. The method of claim 1, which further includes adjusting the distance between said substrate and said feeder means to maintain said predetermined distance.
6. The method of claim 1, which further includes ultrasonically pulsing gas to form said droplets as said droplets are introduced into said chamber.
US07/832,266 1992-02-07 1992-02-07 Collision centrifugal atomization unit Abandoned USH1086H (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
US07/832,266 USH1086H (en) 1992-02-07 1992-02-07 Collision centrifugal atomization unit

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US07/832,266 USH1086H (en) 1992-02-07 1992-02-07 Collision centrifugal atomization unit

Publications (1)

Publication Number Publication Date
USH1086H true USH1086H (en) 1992-08-04

Family

ID=25261163

Family Applications (1)

Application Number Title Priority Date Filing Date
US07/832,266 Abandoned USH1086H (en) 1992-02-07 1992-02-07 Collision centrifugal atomization unit

Country Status (1)

Country Link
US (1) USH1086H (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN114653450A (en) * 2020-12-22 2022-06-24 中国石油化工股份有限公司 Micro-droplet generating device and generating method

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN114653450A (en) * 2020-12-22 2022-06-24 中国石油化工股份有限公司 Micro-droplet generating device and generating method

Similar Documents

Publication Publication Date Title
CN103747898B (en) For the method and apparatus being formed product by atomization metal and alloy
JP5837731B2 (en) Apparatus and method for producing clean and rapidly solidified alloys
US5935461A (en) Pulsed high energy synthesis of fine metal powders
US5649992A (en) Methods for flow control in electroslag refining process
US4689074A (en) Method and apparatus for forming ultrafine metal powders
RU2145644C1 (en) Method and device for producing coat from powder materials
KR20060071315A (en) Laser Enhancement of Cold Spray Deposits
US4224356A (en) Deposition of metals on a base
KR101512772B1 (en) Method and atomizer apparatus for manufacturing metal powder
US6858262B2 (en) Method for producing a surface-alloyed cylindrical, partially cylindrical or hollow cylindrical component and a device for carrying out said method
DE4221512C2 (en) Process for producing rapidly solidified, flaky metal powder and device for producing the same
GB2367073A (en) Free-form tooling; rapid prototyping
EP3655185A1 (en) Method for cost-effective production of ultrafine spherical powders at large scale using thruster-assisted plasma atomization
EP4034320B1 (en) Device for atomizing a melt stream by means of a gas
US11919089B2 (en) Method and device for breaking up an electrically conductive liquid
US6773246B2 (en) Atomizing apparatus and process
US5235895A (en) Ballistic armor and method of producing same
JPH02116656A (en) Method and device for manufacture of amorphous ceramic or metallic powder
USH1086H (en) Collision centrifugal atomization unit
US5855642A (en) System and method for producing fine metallic and ceramic powders
US5149063A (en) Collision centrifugal atomization unit
US4977950A (en) Ejection nozzle for imposing high angular momentum on molten metal stream for producing particle spray
EP3463812B1 (en) Apparatus for additive manufacturing of 3d objects using cold spraying
US6461403B1 (en) Apparatus and method for the formation of uniform spherical particles
GB1605035A (en) Simultaneous spray deposition and peening of metal

Legal Events

Date Code Title Description
STCF Information on status: patent grant

Free format text: PATENTED CASE