Hydrometallurgical process for producing spherical maraging steel powders utilizing spherical powder and elemental oxidizable species

Abstract

A process for forming maraging steel alloys comprise forming an aqueous solution containing the metal values of iron, cobalt, nickel and molybdenum in a predetermined ratio, forming the reducible solid material from the solution, reducing the solid material to form metallic powder particles. These particles are entrained in a carrier gas and fed into a high temperature zone to form droplets. The droplets are cooled to form essentially spherical particles which are agglomerated with a predetermined amount of at least one readily oxidizable metal selected from the group consisting of aluminum, titanium and vanadium. The agglomerates are entrained in a carrier gas and fed into a high temperature zone to form droplets which are thereafter cooled to form essentially spherical shaped particles of a maraging steel alloy containing at least one readily oxidizable metal.

Description

CROSS REFERENCE TO RELATED APPLICATIONS

This invention is related to the following applications: Ser. No. 054,557, filed 5/27/87, entitled, "Hydrometallurgical Process For Producing Finely Divided Spherical Metal Alloy Powders"; Ser. No. 026,312, filed 3/16/87, entitled, "Hydrometallurgical Process for Producing Finely Divided Spherial Refractory Metal Alloy Powders"; Ser. No. 028,824, filed 3/23/87, entitled, "Hydrometallurgical Process For Producing Finely Divided Spherical Low Melting Temperature Powders"; Ser. No. 026,222, filed 3/16/87, entitled, "Hydrometallurgical Process for Producing Finely Divided Spherical Precious Metal Alloy Powders"; Ser. No. 054,553, filed 5/27/87, entitled, "Hydrometallurgical Process For Producing Finely Divided Copper and Copper Alloy Powders"; Ser. No. 054,479, filed 5/27/87, entitled "Hydrometallurgical Process For Producing Finely Divided Iron Based Powders", all of which are by the same inventors as this application and assigned to the same assignee.

This invention is related to the following applications: Ser. No. 140,157 entitled "Hydrometallurgical Process For Producing Irregular Morphology Steel Powders"; Ser. No. 140,371 entitled, "Hydrometallurgical Process For Producing Finely Divided Spherical Maraging Steel Powders"; Ser. No. 140,374 entitled "Hydrometallurgical Process for Producing Powders With Readily Oxidizable Alloying Elements"; Ser. No. 140,701 entitled "Hydrometallurgical Process For Producing Spherical Maraging Steel Powders With Readily Oxidizable Alloying Elements"; and Ser. No. 140,514 entitled "Hydrometallurgical Process For Producing Finely Divided Spherical Maraging Steel Powders Pre-Alloyed Containing Readily Oxidizable Alloying Elements", all of which are filed concurrently herewith and all of which are by the same inventors and assigned to the same assignee as the present application.

FIELD OF THE INVENTION

This invention relates to the preparation of maraging steel powders containing an oxidizable metal by a hydrometallurgical process. More particularly, it relates to the production of such powders using substantially spherical pre-alloyed powders to agglomerate with elemental oxidizable species and then feeding such agglomerates to a high temperature zone to produce spherical shaped particles of a maraging steel containing such oxidizbble metal.

BACKGROUND OF THE INVENTION

Maraging steel is a term of the art derived from "martensite age hardening". These alloys are currently the iron- nickel-cobalt-molybdenum alloys as described in the cobalt monograph series entiltled "Cobalt-containing high strenth steels", Centre D'Information Du Cobalt, Brussels, 1974, pp 50-51. Readily oxidizable metals such as Al, V and/or Ti at low levels e.g. 1% by weight or below can be added.

Metal alloy powders heretofore have been produced by gas or water atomization of molten ingots of the alloy. It has not been generally practical to produce the metal alloy powders directly from the individual metal powders because of the difficulty in obtaining uniformity of distribution of the metals. It is difficult to obtain certain powders containing readily oxidizable metals such as aluminum because of the tendency of those metals to form the respective oxides during processing.

U.S. Pat. No. 3,663,667 discloses a process for producing multimetal alloy powders. Thus, multimetal alloy powders are produced by a process wherein an aqueous solution of at least two thermally reducible metallic compounds and water is formed, the solution is atomized into droplets having a droplet size below about 150 microns in a chamber that contains a heated gas whereby discrete solid particles are formed and the particles are thereafter heated in a reducing atmosphere and at temperatures from those sufficient to reduce said metallic compounds to temperatures below the melting point of any of the metals in said alloy.

U.S. Pat. No. 3,909,241 relates to free flowing powders which are produced by feeding agglomerates through a high temperature plasma reactor to cause at least partial melting of the particles and collecting the particles in a cooling chamber containing a protective gaseous atmosphere where the particles are solidified In this patent the powders are used for plasma coating and the agglomerated raw materials are produced from slurries of metal powders and binders. Both the U.S. Pat. Nos. 3,663,667 and 3,909,241 are assigned to the same assignee as the present invention.

It is believed therefore that a relatively simple process which enables maraging steel alloy powders containing at least one readily oxidizable metal to be produced from Fe-Ni-Co-Mo elements via a hydrometallurgical process combined with melting and cooling to produce spherical particles which are thereafter agglomerated with readily oxidizable elements followed by a second high temperature melting step in an advancement in the art.

SUMMARY OF THE INVENTION

In accordance with one aspect of this invention there is provided a process comprising forming an aqueous solution containing the metal values of iron, cobalt, nickel and molybdenum, in a predetermined ratio. A reducible solid material is formed from the solution. Thereafter the material is reduced to form metallic powder particles. At least a portion of said powder particles is entrained in a carrier gas, which is fed into a high temperature zone to form droplets therefrom. The droplets are cooled to form essentially spherical shaped metal alloy particles. These spherical shaped particles are agglomerated with a predetermined amount at least one readily oxidizable metal selected from the group consisting of aluminum, titanium and vanadium which are then entrained in a carrier gas and fed into a high temperature zone to form droplets therefrom. These droplets are cooled to form essentially spherical shaped particles of a maraging steel alloy containing at least one readily oxidizable metal.

DETAILS OF THE PREFERRED EMBODIMENTS

For a better understanding of the present invention, together with other and further objects, advantages, and capabilities thereof, reference is made to the following disclosure and appended claims in connection with the foregoing description of some of the aspects of the invention.

While it is preferred to use metal powders as starting materials in the practice of this invention because such materials dissolve more readily than other forms of metals, however, use of the powders is not essential. Metallic salts that are soluble in water or in an aqueous mineral acid can be used. When alloys are desired, the metallic ratio of the various metals in the subsequently formed solids of the salts, oxides or hydroxides can be calculated based upon the raw material input or the solid can be sampled and analyzed for the metal ratio in the case of alloys being produced. The metal values can be dissolved in any water soluble acid. The acids, such as hydrochloric, sulfuric or nitric, can include the mineral acids as well as the organic acids such as acetic, formic and the like. Hydrochloric is especially preferred because of cost and availability.

After the metal sources are dissolved in the aqueous acid solution, the resulting solution can be subjected to sufficient heat to evaporate water. The metal compounds, for example, the oxides, hydroxides, sulfates, nitrates, chlorides, and the like, will precipitate from the solution under certain pH conditions. The solid materials can be separated from the resulting aqueous phase or the evaporation can be continued. Continued evaporation results in forming particles of a residue consisting of the metallic compounds. In some instances, when the evaporation is done in air, the metal compounds may be the hydroxides, oxides or mixtures of the mineral acid salts of the metals and the metal hydroxides or oxides. The residue may be agglomerated and contain oversized particles. The average particle size of the materials can be reduced in size by milling, grinding or by other conventional methods of particle size reduction.

After the particles are reduced to the desired size they are heated in a reducing atmosphere at a temperature above the reducing temperature of the salts but below the melting point of the metals in the particles. The temperature is sufficient to evolve any water of hydration and the anion. If hydrochloric acid is used and there is water of hydration present, the resulting wet hydrochloric acid evolution is very corrosive thus appropriate materials of construction must be used. The temperatures employed are below the melting point of any of the metals therein but sufficiently high to reduce and leave only the cation portion of the original molecule. In most instances a temperature of at least about 500.degree. C. is required to reduce the compounds. Temperatures below about 500.degree. C. can cause insufficient reduction while temperatures above the melting point of the metal result in large fused agglomerates. If more than one metal is present the metals in the resulting multimetal particles can either be combined as intermetallics or as solid solutions of the various metal components. In any event there is a homogenous distribution throughout each partner of each of the metals. The particles are generally irregular in shape. If agglomeration has occurred during the reduction step, particle size reduction by conventional milling, grinding and the like can be done to achieve a desired average particle size for example less than about 20 micrometers with at least 50% being below about 20 micrometers as a preferred size.

In preparing the powders of the present disclosed invention, a high velocity stream of at least partially molten metal droplets is formed at two times during the process Such a stream may be formed by any thermal spraying technique such as combustion spraying and plasma spraying. Individual particles can be completely melted (which is the preferred process), however, in some instances surface melting sufficient to enable the subsequent formation of spherical particles from such partially melted particles is satisfactory. In such instances about 50% by weight of the particles or agglomerates are melted. Typically, the velocity of the droplets is greater than about 100 meters per second, more typically greater than 250 meters per second Velocities on the order of 900 meters per second or greater may be achieved under certain conditions which favor these speeds which may include spraying in a vacuum.

In the preferred process of the present invention, a powder is fed through a thermal spray aparatus. Feed powder is entrained in a carrier gas and then fed through a high temperature reactor. The temperature in the reactor is preferably above the melting point of the highest melting component of the metal powder and even more preferably considerably above the melting point of the highest melting component of the material to enable a relatively short residence time in the reaction zone.

The stream of dispersed entrained molten metal droplets may be produced by plasma-jet torch or gun apparatus of conventional nature. In general, a source of metal powder is connected to a source of propellant gas. A means is provided to mix the gas with the powder and propel the gas with entrained powder through a conduit communicating with a nozzle passage of the plasma spray apparatus. In the arc type apparatus, the entrained powder may be fed into a vortex chamber which communicates with and is coaxial with the nozzle passage which is bored centrally through the nozzle. In an arc type plasma apparatus, an electric arc is maintained between an interior wall of the nozzle passage and an electrode present in the passage. The electrode has a diameter smaller than the nozzle passage with which it is coaxial to so that the gas is discharged from the nozzle in the form of a plasma jet. The current source is normally a DC source adapted to deliver very large currents at relatively low voltages. By adjusting the magnitude of the arc powder and the rate of gas flow, torch temperatures can range from 5500 degrees centigrade up to about 15,000 degrees centigrade. The apparatus generally must be adjusted in accordance with the melting point of the powders being sprayed and the gas employed. In general, the electrode may be retracted within the nozzle when lower melting powders are utilized with an inert gas such as nitrogen while the electrode may be more fully extended within the nozzle when higher melting powders are utilized with an inert gas such as argon.

In the induction type plasma spray apparatus, metal powder entrained in an inert gas is passed at a high velocity through a strong magnetic field so as to cause a voltage to be generated in the gas stream. The current source is adapted to deliver very high currents, on the order of 10,000 amperes, although the voltage may be relatively low such as 110 volts. Such currents are eequired to generate a very strong direct magnetic field and create a plasma Such plasma devices may include additional means for aiding in the initation of a plasma generation, a cooling means for the torch in the form of annular chamber around the nozzle.

In the plasma process, a gas which is ionized in the torch regains its heat of ionization on exiting the nozzle to create a highly intense flame. In general, the flow of gas through the plasma spray apparatus is effected at speeds at least approaching the speed of sound. The typical torch comprises a conduit means having a convergent portion which converges in a downstream direction to a throat. The convergent portion communicates with an adjacent outlet opening so that the discharge of plasma is effected out the outlet opening.

Other types of torches may be used such as an oxy-acetylene type having high pressure fuel gas flowing through the nozzle. The powder may be introduced into the gas by an aspirating effect. The fuel is ignited at the nozzle outlet to provide a high temperature flame.

Preferably the powders utilized for the torch should be uniform in size and composition. A relatively narrow size distribution is desirable because, under set flame conditions, the largest particles may not melt completely, and the smallest particles may be heated to the vaporization point. Incomplete melting is a detriment to the product uniformity, whereas vaporization and decomposition decreases process efficiency. Typically, the size ranges for plasma feed powders of this invention are such that 80 percent of the particles fall within about a 15 micrometer diameter range.

The stream of entrained molten metal droplets which issues from the nozzle tends to expand outwardly so that the density of the droplets in the stream decreases as the distance from the nozzle increases. Prior to impacting a surface, the stream typically passes through a gaseous atmosphere which solidifies and decreases the velocity of the droplets. As the atmosphere approaches a vacuum, the cooling and velocity loss is diminished. It is desirable that the nozzle be positioned sufficiently distant from any surface so that the droplets remain in a droplet form during cooling and solidification. If the nozzle is too close, the droplets may solidify after impact.

The stream of molten particles may be directed into a cooling fluid. The cooling fluid is typically disposed in a chamber which has an inlet to replenish the cooling fluid which is volatilized and heated by the molten particles and plasma gases. The fluid may be provided in liquid form and volatilized to the gaseous state during the rapid solidification process. The outlet is preferably in the form of a pressure relief valve. The vented gas may be pumped to a collection tank and reliquified for reuse.

The choice of the particle cooling fluid depends on the desired results. If large cooling capacity is needed, it may be desirable to provide a cooling fluid having a high thermal capacity. An inert cooling fluid which is non-flammable and nonreactive may be desirable if contamination of the product is a problem. In other cases, a reactive atmosphere may be desirable to modify the powder. Argon and nitrogen are preferable nonreactive cooling fluids. Hydrogen may be preferable in certain cases to reduce oxides and protect from unwanted reactions.

Since the melting plasmas are formed from many of the same gases, the melting system and cooling fluid may be selected to be compatible.

The cooling rate depends on the thermal conductivity of the cooling fluid and the molten particles to be cooled, the size of the stream to be cooled, the size of individual droplets, particle velocity and the temperature difference between the droplet and the cooling fluid. The cooling rate of the droplets is controlled by adjusting the above mentioned variables. The rate of cooling can be altered by adjusting the distance of the plasma from the liquid bath surface. The closer the nozzle to the surface of the bath, the more rapidly cooled the droplets.

Powder collection is conveniently accomplished by removing the collected powder from the bottom of the collection chamber. The cooling fluid may be evaporated or retained if desired to provide protection against oxidation or unwanted reactions.

The particle size of the spherical powders will be largely dependent upon the size of the feed into the high temperature reactor. Some densification occurs and the surface area is reduced thus the apparent particle size is reduced. The preferred form of particle size measurement is by micromergraph, sedigraph or microtrac. Materials having a particle size below about 250 micrometers over any particle size are useful in many applications. It is preferred however that a majority of the particles be below about 20 micrometers with an average particle size of about 20 micrometers.

After cooling and resolidification, the resulting high temperature treated material can be classified to remove the major spheroidized particle portion from the essentially non-spheroidized minor portion of particles and to obaain the desired particle size. The classification can be done by standard techniques such as screening or air classification. The unmelted minor portion can then be reprocessed according to the invention to convert it to fine spherical particles.

The powdered materials of this invention are essentially spherical particles which are essentially free of elliptical shaped material and essentially free of elongated particles having rounded ends, is shown in European Patent Application No. WO8402864.

Prealloyed spherical component particles will have the advantage of decreased consolidation time and temperature to achieve homogeneity in the final product.

U.S. Pat. Nos. 3,974,245 and 3,617,358 incorporated by reference herein disclose suitable agglomeration techniques, which can be utilized to form the agglomerates of the spherical particles and the readily oxidizable source of metals. Spray drying in a non-oxidizing atmosphere is the preferred method of agglomeration.

To further illustrate this invention, the following non-limiting example is presented. All parts, proportions and percentages are by weight unless otherwise indicated.

EXAMPLE

About 670 parts of iron powder and about 180 parts of nickel powder and about 100 parts of cobalt are dissolved in about 4000 parts of 10N HCl using a glass lined agitated reactor. About 50 parts of molybdenum as a solution of ammonium molybdate are added to the above solution.

Ammonium hydroxide is added to a pH of about 6.5-7.5. The iron, nickel, cobalt and molybdenum are precipitated as an intimate mixture of hydroxides. This mixture is then evaporated to dryness. The mixture is then heated to about 350.degree. C. in air for about 3 hours to remove the excess ammonium chloride. This mixture is then hammermilled to produce a powder having a greater than 50% of the particles smaller than about 50 micrometers with no particles larger than about 100 micrometers. These milled particles are heated in a reducing atmosphere of H.sub.2 at a temperature of about 750.degree. C. for about 3 hours. Finely divided particles containing 67% iron, 18% nickel, 10% cobalt and 5% molybdenum are formed.

The Fe, Ni, Co, Mo powder particles are entrained in an argon carrier gas. The particles are fed to a Metco 9MB plasma gun at a rate of about 10 pounds per hour. The gas is fed at the rate of about 6 cubic feet per hour. The plasma gas (Ar+H.sub.2) is fed at the rate of about 70 cubic feet per hour. The torch power is about 20 KW at about 50 volts and 400 amperes. The molten droplets exit into a chamber containing inert gas. The resulting powder contains two fractions, the major fraction consists of the spherical shaped resolidified particles. The minor fraction consists of particles having surfaces which have been partially melted and resolidified. Resulting spherical Fe, Ni, Co and Mo alloy is agglomerated with aluminum, titanium and/or vanadium to achieve a composition haivng a predetermined ratio of elements. The agglomerates are fed to a similar gun under similar condition to achieve spherical shaped particles of a maraging steel alloy containing up to about 1% by weight of the readily oxidizable metal.

While there has been shown and described what are considered the preferred embodiments of the invention, it will be obvious to those skilled in the art that various changes and modifications may be made therein without departing from the scope of the invention as defined by the appended claims.

Claims

1. A process comprising:

(a) forming an aqueous solution containing the metal values of iron, cobalt, nickel and molybdenum, said metals being present in a predetermined ratio,

(b) forming from said solution a reducible solid material selected from the group consisting of salts of said metals, oxides of said metals, hydroxides of said metals and mixtures thereof,

(c) reducing said material to form metallic powder particles,

(d) entraining at least a portion of said powder particles in a carrier gas,

(e) feeding said entrained particles and said carrier gas into a high temperature zone and maintaining said particles in said zone for a sufficient time to melt at least about 50% by weight of said particles, and to form droplets therefrom,

(f) cooling said droplets to form essentially spherical shaped metal alloy particles,

(g) agglomerating said spherical shaped particles with a predetermined amount of particles of at least one readily oxidizable metal selected from the group consisting of aluminum, titanium and vanadium,

(h) entraining at least a portion of said agglomerates in a carrier gas,

(i) feeding said entrained agglomerates and said carrier gas into a high temperature zone and maintaining said agglomerates in said zone for a sufficient time to melt at least about 50% by weight of said agglomerates and to form droplets therefrom, and

(j) cooling said droplets to form essentially spherical shaped particles of a maraging steel alloy containing at least one readily oxidizable metal.

2. A process according to claim 1 wherein said solution is a mineral acid selected from the group consisting of hydrochloric, sulfuric and nitric acids.

3. A process according to claim 2 wherein said mineral acid is hydrochloric acid.

4. A process according to claim 1 wherein said aqueous solution contains a water soluble acid.

5. A process according to claim 2 wherein said reducible solid material is formed by evaporation of the water from the solution.

6. A process according to claim 2 wherein said reducible solid material is formed by adjusting the pH of the solution to form a solid which is separated from the resulting aqueous phase.

7. A process according to claim 1 wherein said carrier gas is an inert gas.

8. A process according to claim 1 wherein said high temperature zone is created by a plasma torch.

9. A process according to claim 1 wherein said agglomerating is achieved by spray drying.

10. A process according to claim 1 wherein said material produced by step (b) is subjected to a particle size reduction step prior to the reduction step (c).

11. A process according to claim 1 wherein the powder particles from step (c) are subjected to a particle size reduction step prior to the entraining step (d).

12. A process according to claim 1 wherein at least 50% of said spherical shaped particles of step (j) have a size less than about 50 micrometers.

13. A process according to claim 1 wherein essentially all of the particles in step (e) are melted.

14. A process according to claim 1 whrein essentially all of the agglomerates in step (i) are melted.