Patent Application
20240165704
The present invention relates to the production of steel powders and in particular to the production of steel powders by gas atomization for additive manufacturing. The present invention also relates to the installation for producing the steel powders thereof.
There is an increasing demand for steel powders for additive manufacturing and the manufacturing processes have to be adapted consequently.
It is notably known to melt metal material in an electric furnace or a vacuum melting furnace, to refine the composition and to pour the molten steel in a tundish connected to an atomizer. Such batch process is not compatible with the need for producing large amounts of steel powders, preferably in a continuous mode.
An aim of the present invention is therefore to remedy the drawbacks of the facilities and processes of the prior art by providing a versatile process for producing steel powders. In particular, the aim is to provide a process capable of using different raw materials and capable of producing powders at different steel compositions depending on the demand, while possibly running in a continuous mode.
For this purpose, a first subject of the present invention consists of a process for the production of steel powders comprising the steps of:
The process according to the invention may also have the optional features listed below, considered individually or in combination:
A second subject of the invention consists of an installation for the production of steel powders comprising:
The installation according to the invention may also have the optional features listed below, considered individually or in combination:
Other characteristics and advantages of the invention will be described in greater detail in the following description.
The invention will be better understood by reading the following description, which is provided purely for purposes of explanation and is in no way intended to be restrictive.
In a first step of the process, molten iron (or pig iron) is provided from a blast furnace.
The blast furnace is conventionally supplied with solid materials, mainly sinter, pellets, iron ore and carbonaceous material, generally coke, charged into its upper part, called throat of the blast furnace. The iron-containing burden (sinter, pellets and iron ore) is converted to pig iron conventionally by reducing the iron oxides with a reducing gas (containing CO, H2 and N2 in particular), which is formed by combustion of the carbonaceous material in the tuyeres located in the lower part of the blast furnace, where air, preheated to a temperature of between 1000 and 1300° C., called hot blast, is injected.
The pig iron and slag are tapped from the crucible in the bottom of the blast furnace. Pig iron is poured into a transport ladle which is then poured into a converter (or BOF for Basic Oxygen Furnace) in which scraps have conventionally been previously loaded.
Pig iron can be transported directly to the converter or it can be first pretreated before being poured into the converter. According to one variant of the invention, the pig iron from the blast furnace is sent to a hot metal desulfurization station before being poured into the converter. In that case, the pig iron is preferably desulfurized so that it contains less than 50 ppm S in weight. This desulfurization step facilitates the refining of the molten steel downstream and thus the obtainment of the desired steel composition.
In a second step of the process, the molten iron is refined in the converter to form molten steel comprising, in weight, up to 600 ppm C, up to 120 ppm S, up to 125 ppm P, up to 50 ppm N and up to 1200 ppm O.
The refining process of iron into steel includes a step of oxygen blowing to decarburize the iron and a post-blowing step in which a neutral gas such as argon is blown. Lime and/or dolomite are added into the converter so as to remove impurities such as silicon, phosphorus, and manganese and reach the required levels of impurities for the desired steel composition. Those additions together with the impurities extracted from pig iron form converter slags.
As the decarburisation reaction releases energy, scraps are usually added to control the temperature of the produced liquid steel. Mineral additives, such as lime, dolomite, limestone, etc. . . . may further be charged to control the chemical composition and temperature of the produced liquid steel. Those mineral additions may also be used to monitor the chemical composition of the slag, as slag composition has an impact on the equilibrium between liquid steel and slag and thus on promotion of reactions occurring into the liquid steel.
In the present invention, in order to offer a generic composition compatible with all the possible powder compositions to be produced, the composition, at the end of the refining step in the converter, comprises, in weight, up to 600 ppm C, up to 120 ppm S, up to 125 ppm P, up to 50 ppm N and up to 1200 ppm O, the remainder being iron and inevitable impurities resulting from the process.
In certain cases where demanding powder compositions have to be produced, the composition is further limited to up to 250 ppm C and/or up to 90 ppm P and/or up to 25 ppm N.
The molten steel from the converter is then tapped from the converter to a recuperation ladle. Preferably, and in order to minimize the slag carry-over from the converter, only the first heat of the sequence is tapped to the recuperation ladle which is to be transported to the next step of the process according to the invention. The remaining steel and slag are tapped in a standard steel ladle later during the tapping process and transferred to another part of the plant for another process. By minimizing the slag carry-over, additional deoxidizing is prevented and the level of impurities in the molten steel is lowered.
At the end of the second step of the process, the molten steel is preferably refined to obtain a steel composition comprising in weight up to 30 ppm O. In other words, the O content in the steel composition is limited to up to 30 ppm. More preferably the molten steel is refined to obtain a steel composition comprising in weight from 10 to less than 150 ppm S, up to 150 ppm P, up to 100 ppm N and up to 30 ppm O. The main purpose of this step is to de-oxidize the molten steel. Optionally, this step can include a primary alloying of the molten steel.
In that case, the molten steel is transferred from the converter to a ladle metallurgy furnace (LMF). This transfer is preferably done without controlling the atmosphere.
In the ladle metallurgy furnace, the analytical quality of the liquid metal is adjusted, including compositional trimming, not only of metallic alloying elements, but also the control of metalloids (C, H, N, O, P, S), to different degrees depending on the grade. The type and content of oxide inclusions is controlled, by deoxidation (or “killing”) of the steel, generally with aluminium for sheet steels, by calcium treatment to modify their composition, and by controlled floatation. Different additives, such as lime, dolomite, fluorspar and/or various fluxes are added in the ladle furnace to perform such treatments. The produced impurities form a slag floating on the surface of the molten metal. Depending on the composition of the slag, additives are added to remove remaining impurities.
Optionally, a primary alloying of the molten steel can be done by adding ferroalloys or silicide alloys or nitride alloys or pure metals or a mixture thereof. This primary alloying is of particular interest when all the different steel powders to be produced in the plurality of gas atomizers have in common a given alloying element.
Ferroalloys refer to various alloys of iron with a high proportion of one or more other elements such as silicon, niobium, boron, chromium, aluminum, manganese, molybdenum. . . . The main alloys are FeAl (usually comprising 40 to 60 wt % Al), FeB (usually comprising 17.5 to 20 wt % B), FeCa, FeCr (usually comprising 50 to 70 wr % Cr), FeMg, FeMn, FeMo (usually comprising 60 to 75 wt % Mo), FeNb (usually comprising 60 to 70 wt % Nb), FeNi, FeP, FeS, FeSi (usually comprising 15 to 90 wt % Si), FeSiMg, FeTi (usually comprising 45 to 75 wt % Ti), FeV (usually comprising 35 to 85 wt % V), FeW (usually comprising 70 to 80 wt % Mo).
Silicide alloys can notably be MnSi, CrSi, CaSi. Nitride alloys can be MnN.
Pure metals can notably be iron, copper, nickel, cobalt, chromium, calcium, rare earth metals.
The temperature in the ladle metallurgy furnace is preferably maintained between 1520 and 1700° C., more preferably between 1520 and 1620° C.
In one variant of the invention, in order to offer a generic composition compatible with all the possible powder compositions to be produced, the composition, at the end of the refining step in the ladle metallurgy furnace, comprises in weight up to 600 ppm C, from 10 to less than 150 ppm S, up to 150 ppm P, up to 100 ppm N and up to 30 ppm O, the remainder being iron and inevitable impurities resulting from the process.
In certain cases where demanding powder compositions have to be produced, the molten steel can be further treated in a vacuum tank degasser (VTD) or in a Vacuum Oxygen Decarburization (VOD) vessel. This equipment allows for further limiting notably the hydrogen, nitrogen and/or carbon contents. Hydrogen content can be below 2 ppm (in weight). Nitrogen content can be below 20 ppm (in weight). Carbon content can be below 20 ppm (in weight).
In the vacuum tank degasser, a ladle is usually placed in an open-top vacuum tank, which is connected to vacuum pumps or a vacuum cover is placed directly onto the ladle. Under vacuum conditions and argon blowing, carbon and oxygen will react vigorously until they reach equilibrium at very low levels (treatment time permitted). A modification of the vacuum tank degasser is the vacuum oxygen decarburizer (VOD), which has an oxygen lance in the center of the tank lid to enhance carbon removal under vacuum. The VOD is often used to lower the carbon content of high-alloy steels without also overoxidizing such oxidizable alloying elements as chromium.
The treatment in the VTD or in the VOD vessel can take place before the refinement in the ladle metallurgy furnace or after the refinement in the ladle metallurgy furnace.
In a third step of the process, the molten steel from the converter, or the refined molten steel of the ladle metallurgy furnace, of the VTD or of the VOD if applicable, is poured in a plurality of induction furnaces.
Induction furnaces are electrical furnaces in which the heat is applied by induction heating of metal. An induction furnace consists of a nonconductive crucible holding the charge of metal to be melted, surrounded by a coil of copper wire. A powerful alternating current flows through the wire. The coil creates a rapidly reversing magnetic field that penetrates the metal.
Thanks to the plurality of induction furnaces, the process for producing the steel powders can be easily made continuous.
Each induction furnace can be operated independently of the other induction furnaces. It can notably be shut down for maintenance or repair while the other induction furnaces are still running. It can also be fed with ferroalloys, scrap, Direct Reduced Iron (DRI), silicide alloys, nitride alloys or pure elements in quantities which differ from one induction furnace to the others.
The number of induction furnaces is adapted to the flow of molten steel coming from the converter or refined molten steel coming from the ladle metallurgy furnace and/or to the desired flow of steel powder at the bottom of the atomizers.
According to one variant of the invention, the molten steel from the converter is directly poured in the plurality of induction furnaces or, if applicable, the refined molten steel is directly poured from the ladle metallurgy furnace, from the VTD or from the VOD, to the plurality of induction furnaces. “directly” includes in the present case the use of a ladle to transfer the molten steel to the plurality of induction furnaces.
According to another variant of the invention, the molten steel from the converter, or the refined molten steel from the ladle metallurgy furnace, from the VTD or from the VOD, is first poured in a tundish and then poured from the tundish to the plurality of induction furnaces. Thanks to this configuration, the molten steel can be easily distributed to the induction furnaces on demand. The tundish is mainly used as a storage reservoir. It is batch-fed by the ladle metallurgy furnace and can feed each induction furnace independently. In particular, it is capable of simultaneously pouring the molten steel in all the induction furnaces. One way to achieve this capability is to equip the tundish with as many pouring means as the number of induction furnaces. Pouring means can be pouring holes and corresponding stopper rods.
The temperature in the tundish is preferably maintained between 1520 and 1620° C.
The tundish is preferably purged with Argon to control the oxygen content in the tundish.
In a fourth step of the process, at least one ferroalloy is added in each of the plurality of induction furnaces to adjust the steel composition to the composition of the desired steel powder.
Ferroalloys refer to various alloys of iron with a high proportion of one or more other elements such as silicon, niobium, boron, chromium, aluminum, manganese, molybdenum. . . . The main alloys are FeAl (usually comprising 40 to 60 wt % Al), FeB (usually comprising 17.5 to 20 wt % B), FeCa, FeCr (usually comprising 50 to 70 wr % Cr), FeMg, FeMn, FeMo (usually comprising 60 to 75 wt % Mo), FeNb (usually comprising 60 to 70 wt % Nb), FeNi, FeP, FeS, FeSi (usually comprising 15 to 90 wt % Si), FeSiMg, FeTi (usually comprising 45 to 75 wt % Ti), FeV (usually comprising 35 to 85 wt % V), FeW (usually comprising 70 to 80 wt % Mo).
The mix of ferroalloys and the relative quantity of each of the ferroalloys is adapted case by case to reach the composition of the desired steel powder. The ferroalloys added in the induction furnace are preferably not pre-melted.
Optionally, scraps or Direct Reduced Iron or silicide alloys or nitride alloys or pure elements or a mixture thereof can be also added to ease the composition adjustment.
Direct Reduced Iron is produced from the direct reduction of iron ore (in the form of lumps, pellets, or fines) to iron by a reducing gas or elemental carbon produced from natural gas or coal.
Silicide alloys can notably be MnSi, CrSi, CaSi. Nitride alloys can be MnN.
Pure elements can notably be carbon and pure metals such as iron, copper, nickel, cobalt, chromium, calcium, rare earth metals.
This step can be done independently and asynchronously in each of the induction furnaces. As stated above, different steel compositions can be prepared in different induction furnaces to obtain different steel powders.
The temperature in the plurality of induction furnaces is preferably maintained between 1500 and 1700° C., more preferably between 1620 and 1700° C. to have a proper melting of the ferroalloy and homogenization of the composition. The temperature in at least one of the plurality of induction furnaces is more preferably maintained between 1580 and 1650° C. to extend the induction furnace crucible and refractory lives.
The atmosphere in each of the induction furnaces is preferably not controlled. That said, in one variant of the invention, at least one of the induction furnaces is capable of having its atmosphere controlled. In particular, it is a vacuum induction furnace. It can act as an alternative to the vacuum tank degasser or to the Vacuum Oxygen Decarburization vessel described above to further treat the molten steel.
The minimal duration in each induction furnace is controlled by the atomizing rate and the rate at which the liquid steel can be drained from the reservoir.
In a fifth step of the process, for each induction furnace, the molten steel at the desired composition is poured in a dedicated reservoir connected to at least one gas atomizer. By “dedicated” it is meant that the reservoir is paired with a given induction furnace. That said, a plurality of reservoirs can be dedicated to one given induction furnace. For the sake of clarity, each induction furnace has its own production stream with at least one reservoir connected to at least one gas atomizer. With such parallel and independent production streams, the process for producing the steel powders is versatile and can be easily made continuous.
The reservoir is mainly a storage tank capable of being atmospherically controlled, capable of heating the molten steel and capable of being pressurized.
The atmosphere in each of the dedicated reservoirs is preferably Argon, Nitrogen or a mixture thereof to avoid the oxidation of the molten steel.
The steel composition poured in each reservoir is heated above its liquidus temperature and maintain at this temperature Thanks to this overheating, the clogging of the atomizer nozzle is prevented. Also, the decrease in viscosity of the melted composition helps obtaining a powder with a high sphericity without satellites, with a proper particle size distribution.
The composition is preferably heated at a temperature at least 150° C. above its liquidus temperature to have the viscosity decrease enough. That said, as the surface tension increases with temperature, it is preferred not to heat the composition at a temperature more than 450° C. above its liquidus temperature.
Preferably, the composition is heated at a temperature 200 to 300° C. above its liquidus temperature.
In one variant of the invention, the composition is heated between 1300 and 1750° C., preferably between 1550 and 1750° C., which represents a good compromise between viscosity decrease and surface tension increase.
The reservoir is either continuously under pressure or it can be pressurized once it has been fed with the molten steel. Means for pressurizing the reservoir are designed accordingly. The continuous pressurization of each reservoir is favored to have a continuous flow from the reservoir to at least one atomizer connected to the reservoir. The pressure in each of the dedicated reservoirs is adjusted to keep the metal flow constant. The pressure setting depends on a plurality of parameters. It can be adjusted case by case by the person skilled in the art.
The reservoir can comprise one single chamber or a plurality of chambers capable of being pressurized independently from each other. Thanks to a plurality of chambers, the process for producing the steel powders can be made continuous even more easily.
In a sixth step of the process, when a dedicated reservoir is pressurized, the molten steel can flow from the reservoir to at least one of the gas atomizers connected to the reservoir.
The molten composition is atomized into fine metal droplets by forcing a molten metal stream through an orifice at the bottom of the reservoir, the nozzle, at moderate pressures and by impinging it with jets of gas. The gas is introduced into the metal stream as it leaves the nozzle, serving to create turbulence as the entrained gas expands (due to heating) and exits into a large collection volume, the atomizing tower. The latter is filled with inert gas to prevent the powder from oxidizing. The metal droplets cool down during their fall in the atomizing tower. Gas atomization is preferred because it favors the production of powder particles having a high degree of roundness and a low amount of satellites. The particles are also less oxidized than with water atomization.
The atomization gas is preferably argon or nitrogen. They both increase the melt viscosity slower than other gases, e.g. helium, which promotes the formation of smaller particle sizes. They also control the purity of the chemistry, avoiding undesired impurities, and play a role in the good morphology of the powder. Finer particles can be obtained with argon than with nitrogen since the molar weight of nitrogen is 14.01 g/mole compared with 39.95 g/mole for argon. On the other hand, the specific heat capacity of nitrogen is 1.04 J/(g K) compared to 0.52 for argon. So, nitrogen increases the cooling rate of the particles. Argon might be preferred over nitrogen to avoid the contamination of the composition by nitrogen.
The gas flow impacts the particle size distribution and the microstructure of the metal powder. In particular, the higher the flow, the higher the cooling rate. Consequently, the gas to metal ratio, defined as the ratio between the gas flow rate (in m3/h) and the metal flow rate (in Kg/h), is preferably kept between 1 and 5, more preferably between 1.5 and 3.
The nozzle diameter has an impact on the molten metal flow rate and, thus, on the particle size distribution and on the cooling rate. The maximum nozzle diameter is preferably limited to 6 mm to limit the increase in mean particle size and the decrease in cooling rate. The nozzle diameter is more preferably between 2 and 3 mm to more accurately control the particle size distribution and favor the formation of the desired microstructure.
The metal powders obtained by atomization can be sieved to keep the particles whose size better fits the technique, notably the additive manufacturing technique, to be used afterwards. For example, in case of additive manufacturing by Powder Bed Fusion, the range 15-50 μm is preferred. In the case of additive manufacturing by Laser Metal Deposition or Direct Metal Deposition, the range 45-150 μm is preferred.
The parts made of the metal powders produced by the present process can be obtained by additive manufacturing techniques such as Powder Bed Fusion (LPBF), Direct metal laser sintering (DMLS), Electron beam melting (EBM), Selective heat sintering (SHS), Selective laser sintering (SLS), Laser Metal Deposition (LMD), Direct Metal Deposition (DMD), Direct Metal Laser Melting (DMLM), Direct Metal Printing (DMP), Laser Cladding (LC), Binder Jetting (BJ). Coatings made of the metal powder according to the invention can also be obtained by manufacturing techniques such as Cold Spray, Thermal Spray, High Velocity Oxygen Fuel. They can also be obtained by conventional powder metallurgy, such as press and sinter.
The process according to the invention can be implemented thanks to an installation shown in
The installation can further comprise a ladle metallurgy furnace 103 capable of refining the molten steel to obtain a steel composition comprising up to 30 ppm O.
The installation can further comprise a tundish 109 capable of simultaneously pouring the molten steel or refined molten steel in all the induction furnaces. Such a tundish facilitates the storage of the molten steel and the feeding of the induction furnaces on demand. The tundish is preferably positioned above the plurality of induction furnaces to make the feeding even easier.
The induction furnaces are preferably movable in and out of their position and tiltable to de-slag and to pour the liquid steel in the reservoir. They are preferably positioned on one floor of the steel shop, more preferably one floor below the tundish. They are preferably positioned above the corresponding reservoirs and atomizers to make the feeding even easier.
At least one of the plurality of induction furnaces can be a vacuum induction furnace to meet the steel composition of certain powders. Alternatively, the installation can further comprise a vacuum tank degasser and/or Vacuum Oxygen Decarburization vessel to adjust the composition of certain powders. This vacuum tank degasser and this Vacuum Oxygen Decarburization vessel 108 are preferably positioned between the ladle metallurgy furnace 103 and the plurality of induction furnaces 104, 106, or the tundish 109 if applicable.
The ferroalloy feeding unit 111 preferably comprises storage silos containing one ferroalloy each and conveying means capable of conveying each ferroalloy to each induction furnace and optionally to the ladle metallurgy furnace. The ferroalloy feeding unit can also comprises storage means for silicide alloys and/or nitride alloys and/or pure elements and conveying means capable of conveying these materials to each induction furnace and optionally to the ladle metallurgy furnace. The conveying means can be feeding pipes. They can go directly to each induction furnace or can go to a mixing unit where mixes of ferroalloys, silicide alloys, nitride alloys, pure elements are prepared before being conveyed to each induction furnace. The ferroalloy feeding unit can also comprise feeding means for scraps and Direct Reduced Iron.
Each dedicated reservoir is preferably connected to at least two gas atomizers so that one gas atomizer can be shut down, for example for collecting the powder at its bottom, for maintenance or for repair, while maintaining the continuous production of the steel powders.
Each reservoir is preferably connected to the at least one gas atomizer by a feeding pipe. More preferably, the feeding pipe is heated, for example inductively heated, to keep the proper overheating of the molten steel and thus prevent the clogging of the atomizer nozzle. The feeding pipe can be closed thanks to closing means, such as a stopper rod operated from inside the reservoir or a stopper positioned in the feeding pipe.
| Filing Document | Filing Date | Country | Kind |
|---|---|---|---|
| PCT/IB2021/052836 | 4/6/2021 | WO |
