METHOD AND DEVICE FOR PRODUCING MATERIAL POWDER

Abstract

A method for producing material powder, comprising providing material and an atomization gas charged with an atomization gas pressure by means of an atomization gas compressor to an atomization device, melting the material and pulverizing the molten material into material powder by means of charging the molten material with the atomization gas using the atomization introducing the material powder from the atomization device into a pressurized container and providing a conveyor gas charged with a conveyer gas pressure by means of a conveyer gas compressor to the pressurized container, wherein the conveyor gas pressure is higher than the atmospheric pressure and lower than the atomization gas pressure, as well as a device for carrying out the method.

Claims

1. A method for producing material powder, comprising the steps of: providing material and an atomization gas charged with an atomization pressure by means of an atomization gas compressor to an atomization device, melting the material pulverizing the molten material (5) into material powder by means of charging the molten material with the atomization gas using the atomization device; introducing the material powder from the atomization device into a pressurized container; characterized by providing a conveyor gas charged with a conveyor gas pressure by means of a conveyer gas compressor to the pressurized container, wherein the conveyor gas pressure is higher than the atmospheric pressure and lower than the atomization gas pressure.

2. A method for producing material powder according to claim 1, characterized by the step of: returning the conveyor gas from the pressurized container the conveyor gas compressor.

3. A method for producing material powder according to claim 1, characterized by the step of: diverting a portion of the conveyor gas having the conveyor gas pressure before the provision thereof to the pressurized container and compressing the diverted portion of the conveyor gas the atomization gas the atomization gas pressure that is higher than the conveyor gas pressure using the atomization gas compressor.

4. A method for producing material powder according to claim 1, characterized by the steps of: conveying the material powder from the pressurized container into a separation device by means of the conveyor gas; separating the material powder into material powder having a first particle size range and material powder having a second particle size range using the separation device; removing the material powder having the first particle size range from the conveyor gas.

5. A method for producing material powder according to claim 4, characterized by the steps of: conveying the material powder having the second particle size range from the separation device into at least one further separation device using the conveyor gas, separating the material powder having the second particle size range into material powder having at least two further particle size ranges using the at least one further separation device; removing the material powder having at least one of the at least two further particle size ranges from the conveyor gas.

6. A method for producing material powder according to claim 1 characterized by the step of: heating the atomization gas using an atomization gas heat exchanger.

7. A method for producing material powder according to claim 1 comprising the step of: cooling the conveyor gas using a second conveyor gas heat exchanger.

8. A device for producing material powder having a conveyor gas compressor, an atomization gas compressor, an atomization device and a pressurized container, wherein the atomization gas compressor is configured to provide an atomization gas charged with an atomization gas pressure to the atomization device, wherein the atomization device is configured to melt a material and to charge the material powder with the atomization gas to atomize into material powder and to introduce the material powder into the pressurized container, characterized in that the device is configured to provide a conveyor gas charged with a conveyor gas pressure that is higher than the atmospheric pressure and lower than the atomization gas pressure by means of the conveyor gas compressor to the pressurized container.

9. A device according to claim 8, characterized in that the device is configured to return the conveyor gas from the pressurized container to the conveyor gas compressor.

10. A device according to claim 8, characterized in that the device is configured to divert a portion of the conveyor gas having the conveyor gas pressure before the provision thereof to the pressurized container and the atomization gas compressor configured to compress the diverted portion of the conveyor gas into the atomization gas having the atomization gas pressure that is higher than the conveyor gas pressure.

11. A device according to claim 8, characterized in that the device has at least one separation device and is configured to convey the material powder with the conveyor gas out of the pressurized container into the separation device, wherein the separation device is configured to separate the material powder into material powder having a first particle size range and material powder having a second particle size range, wherein the device is configured to remove the material powder having the first particle size range from the conveyor gas.

12. A device according to claim 11, characterized in that the device is configured to convey the material powder having the second particle size range from the separation device into at least one further separation device using the conveyor gas and the at least one further separation device configured to separate the material powder having the second particle size range into material powder having at least two further particle size ranges and that the device configured to remove the material powder having at least one of the at least two further particle size ranges from the conveyor gas.

13. A device according to claim 8, characterized in that the device comprises an atomization gas heat exchanger, which is configured to heat the atomization gas.

14. A device according to claim 8, characterized in that the device comprises a second conveyor gas heat exchanger which is configured to cool the conveyor gas.

Description

[0028] Advantageous embodiments of the method according to the invention and the device according to the invention are explained in greater detail in the following by way of the figures.

[0029] FIG. 1 shows a process scheme of the method according to the invention and a schematic depiction of the set-up of the device according to the invention, respectively.

[0030] FIG. 2a shows an atomization device of the device according to the invention in a first embodiment variant.

[0031] FIG. 2b shows the atomization device of the device according to the invention in a second embodiment variant.

[0032] FIG. 3 shows the influence of a conveyor gas pressure on the particle size of the material powder produced using the method according to the invention.

[0033] FIG. 4 shows a distribution of particle diameters of material powders produced using the method according to the invention.

[0034] FIG. 1 shows a process scheme of the method according to the invention and a schematic depiction of the device 20 according to the invention having a conveyor gas compressor 1, an atomization gas compressor 2, an atomization device 3 and a pressurized container 4, respectively, wherein the pressurized container 4 and the atomization device 3 in the process scheme are depicted as a common unit 3 and 4. In the method according to the invention for producing material powder a material 5 and an atomization gas 6 charged with an atomization gas pressure by means of the atomization gas compressor 2 are provided to the atomization device 3. Various atomization devices 3, which have been known from prior art, may be used within the frame of the method according to the invention. There are to be mentioned as examples open (free) jet-, confined (or closed couple)-, close coupled atomization-, plasma atomization and in general internally mixing and externally mixing atomization devices 3. In the atomization device 3 the material 5 is molten and atomized into material powder by the molten material 5 being charged with the atomization gas 6 using the atomization device 3. The material powder is not depicted in the schematic view of FIG. 1. Subsequently, the material powder is introduced by the atomization device 3 into the pressurized container 4, which is depicted in FIG. 1 in an entity 3 and 4 with the atomization device 3. According to the invention, a conveyor gas 7 charged with a conveyor gas pressure using the conveyor gas compressor is provided to the pressurized container 4. In this way, in addition the conveyor gas 7 is introduced into the pressurized container 4 in a gas stream of its own, as depicted in detail in FIG. 2a and FIG. 2b. This conveyor gas pressure in this regard is higher than the atmospheric pressure and lower than the atomization gas pressure. In the pressurized container 4 there is then developed an equilibrium pressure. In this way, there is given the possibility to adjust the gas density in particular at the atomization point and to obtain a higher pulse transfer between the molten material 5 and the gas surrounding the molten material 5 and flowing through it, as is possible in a method known from prior art. In this way, there is obtained a better atomization result in comparison to prior art, and the particle fineness of the material powder produced by means of the method according to the invention is improved. Due to the conveyor gas pressure that is increased compared to the atmospheric pressure there is in addition obtained the advantage that no undesired ambient air may contaminate the material powder in the method according to the invention. In this way, the purity of the material powder produced is increased, as undesired reactions with oxygen, nitrogen or hydrogen are avoided. Furthermore, there is provided an improved cooling effect by the conveyor gas pressure. Flow rate and particle sizes may also be controlled by means of the conveyor gas pressure. By charging the conveyor gas 7 with pressure and, hence, also one of the outlet openings 8 depicted in the FIGS. 2a and 2b of the atomization device 3 in opposition to the flow direction of the exiting stream of molten material 5 the purity of the material powder as well as the production rate may be separately adjusted. The higher the gas pressure at the outlet opening of the atomization device 3 in comparison to the pressure of the molten material 5, the lower the production rate. The higher the gas flow rate in comparison to the flow rate of the molten material 5, the finer the material powder produced. This results in the possibility of an independent adjustment of powder fineness and production rate. Via the conveyor gas pressure, the fineness of the produced particles of the material powder may be adjusted. A flow rate of the molten material may be adjusted by a pressure, which acts on the molten material 5. By atomization of the molten material 5 in the pressurized container 4 charged with the conveyor gas, there is provided an option for adjusting the fineness of the material powder.

[0035] The method according to the invention is suited for producing material powder from various materials 5. To be mentioned as examples are metals like iron, copper and titanium, metal alloys, molten mineral masses and slags, waxes, polymers, plastics and plastic blends. In the case of the production of material powders from waxes it is advantageous to use nitrogen or argon as atomization gas 6 and/or conveyor gas 7 in the method according to the invention. In the case of the production of materials powders from polymers it is advantageous to use CO.sub.2 as atomization gas 6 and/or conveyor gas 7 in the method according to the invention. Further suitable combinations of various material powders with various gases or gas mixtures, respectively, are known to those skilled in the art.

[0036] As depicted in FIG. 1, in this method the gas is guided according to the invention in part or also completely in a cycle. According to the preferred embodiment of the method according to the invention the conveyor gas 7 is returned from the pressurized container 4 to the conveyor gas compressor 1. In this way, there is obtained the advantage that the conveyor gas 7 is not lost but is rather reused in the method according to the invention. This is in particular advantageous when using expensive conveyor gases 7 such as, for example, noble gases.

[0037] According to the preferred embodiment of the method according to the invention a portion of the conveyor gas 7 is deviated using the conveyor gas pressure, as depicted in FIG. 2, before the provision thereof to the pressurized container 4. This deviated conveyor gas 7 is compressed into the atomization gas 6 by means of the atomization gas compressor 2 to the atomization gas pressure. The atomization gas pressure is higher than the conveyor gas pressure. The atomization gas 6 is then provided to the atomization device 3. In this way, there is obtained the advantage that the same gas is used as atomization gas 6 and as conveyor gas 7. In this way, the method according to the invention is simplified and may be realized more cost-effectively.

[0038] Subsequently to the atomization of the molten material 5 using the atomization device 3 into the material powder and to the introduction of the material powder into the pressurized container 4, the material powder is conveyed preferably out of the pressurized container 4 by means of the conveyor gas 7 into a separation device 9. The separation device 9 separates the material powder into material powder having a first particle size range and material powder having a second particle size range. Subsequently, the material powder having the first particle size range is removed from the conveyor gas 7. The separation device 9 may, for example, be configured as a cyclone separator. Alternatively, the separation device 9 may also be configured as filter, magnetic or electrostatic separation device 9. Further embodiments of separation devices 9 have in general been known to those skilled in the art.

[0039] In the preferred embodiment depicted in FIG. 1 of the method according to the invention the material powder having the second particle size range is conveyed out of the separation device 9 into two further separation devices 9. According to the invention the material powder having the second particle size range is conveyed out of the separation device 9 into at least one further separation device 9. In the at least one further separation device 9 the material powder having the second particle size range is separated into material powder having at least two further particle size ranges. Subsequently, the material powder having at least one of the at least two further particle size ranges is removed from the conveyor gas 7. In this way, there is obtained the advantage that the material powder may be split into various particle size ranges. The further separation devices 9 may be configured like the separation device 9, or they may apply an alternative separation method.

[0040] The separation device 9 is, for example, configured as a cyclone separator, wherein there is provided a further successive separation device 9, which is configured as a filter. Alternatively, there may also be used two cyclone separators in series with a successive filter. Another exemplary embodiment variant of the device according to the invention comprises a coarse separator, a cyclone separator and one or also two successive filters. Instead of filters, there may also be used wet separators.

[0041] As depicted in FIG. 1, the method according to the invention comprises in the preferred embodiment heating the atomization gas 6 using an atomization gas heat exchanger 10. In this way there is obtained the advantage that the temperature of the atomization gas 6 is increased, whereby there may be obtained a better atomization result.

[0042] The method according to the invention preferably comprises furthermore cooling the conveyor gas 7 using a first conveyor gas heat exchanger 11. The first conveyor gas heat exchanger 11 cools the conveyor gas 7 preferably before the compression thereof using the conveyor gas compressor 1. In this way, there is prevented overheating of the conveyor gas in the conveyor gas compressor 1.

[0043] In the preferred embodiment of the method according to the invention there is further provided a second conveyor gas heat exchanger 12, which cools the conveyor gas 7. In this way there is obtained the advantage that overheating of the conveyor gas 7 or of individual components of the method, respectively, of a device 20 according to the invention, respectively, which performs the method according to the invention, is prevented.

[0044] The device 20 according to the invention, which is depicted in FIG. 1, for producing material powder comprises the conveyor gas compressor 1, the atomization gas compressor 2, the atomization device 3 and the pressurized container 4. The device 20 according to the invention preferably comprises the at least one separation device 9 for separating the material powder into various particle size ranges. In the preferred embodiment of the device 20 according to the invention the device 20 further comprises the cooling device, the atomization gas heat exchanger 10, the first conveyor gas heat exchanger 11 and the second conveyor gas heat exchanger 12.

[0045] FIG. 2a shows a first embodiment variant of the atomization device 3 of the device 20 according to the invention. The atomization device 3 is configured in the first embodiment variant as a plasma atomization device, preferably for metal. The material 5 is introduced in the form of metal wires into the atomization device 3, wherein melting the material 5 is carried out by applying an electrical voltage onto the metal wires by means of a light arc 13. This results in a change of the distance of the ends of the metal wires by a continuous melting thereof, which is compensated by a constant advance of the wire. The light arc 13 is charged with the atomization gas 6 having the atomization gas pressure, whereby the molten material 5 is atomized into material powder. The material powder is introduced by the atomization gas 6 into the pressurized container 4, whereby the pressurized container 4 is charged with the conveyor gas 7 being lower than the conveyor gas pressure. The conveyor gas 7 is preferably, as depicted in FIG. 2, introduced in several gas streams or in parallel to the ejection of the material powder out of the atomization device 3, respectively, into the pressurized container 4. It may, however, also be introduced in a tangential inlet, or also in the radial direction to the ejection of the material powder. In this way, turbulences are prevented, whereby satellite formation of material powder is being avoided. Satellite formation in general is to be understood as the attachment of smaller particles at larger particles within the material powder. In addition, in this way there is also achieved cooling of the pressurized container 4, whereby the energy requirement of the method according to the invention or of the device 20 according to the invention, respectively, is reduced. By adjusting the atomization gas pressure and the conveyor gas pressure, a length of the light arc 13 may be influenced, whereby there is also achieved a variation of the particle size distribution and the average particle size of the material powder produced.

[0046] FIG. 2b shows a second embodiment variant of the atomization device 3 of the device 20 according to the invention, wherein in this embodiment variant the material 5 is thermally molten. The material 5 may, for example, be molten by means of induction. Further melting methods are commonly known to those skilled in the art. The molten material 5 is charged in the atomization device 3 with the atomization gas 6 and atomized to material powder. The conveyor gas 7 is preferably introduced, like in the first embodiment variant of the atomization device 3, in several gas streams or in parallel, respectively, or also in the tangential or radial direction, respectively, to the ejection of the material powder out of the atomization device 3 into the pressurized container 4. In this way, again satellite formation is being avoided. Furthermore, this will result in a cooling of the pressurized container 4, whereby the energy requirement of the method according to the invention or of the device 20 according to the invention, is reduced. This atomization device 3 is suitable, apart from metals and alloys thereof, also, for example, for electrically non-conductive materials 5 such as waxes and plastics such as polymers, or also for molten mineral masses and slags. It is furthermore also possible to melt meltable, dielectric material 5 by means of a microwave generator. Further atomization methods are commonly known to those skilled in the art.

[0047] The conveyor gas pressure is preferably at least 0.5 bar above the atmospheric pressure, and may be up to 100 bar above the atmospheric pressure. The higher the conveyor gas pressure, the finer the material powder produced and the better the cooling effect. The conveyor gas pressure is preferably between 1 and 10 bar.

[0048] The atomization gas pressure is usually above the critical pressure to reach at least sonic speed in the narrowest nozzle diameter of the atomization device 3. Due to higher relative velocities between gas and molten material 5 there are produced finer material particles. Also at lower pressure ratios atomization and, hence, production of material powder is possible, in particular if it is necessary to produce coarser material powder having a narrower particle size distribution.

[0049] As atomization gas 6 and as conveyor gas 7 for the material 5 to be atomized are suitable gases known to those skilled in the art as being suitable. There may, however, also be used gas mixtures. For example, a low portion of oxygen in the otherwise inert gas (nitrogen, argon, helium or the like) may provide for the surface of the material powder being covered by an oxide layer, resulting in passivation. There are also suitable reducing gas mixtures, such as, for example, a gas proportionally containing a low amount of hydrogen. This offers the possibility to chemically reduce impurities such as oxides or the like from the particulate material. Especially advantageous is the use of reactive gas mixtures in the device 20 according to the invention or the method according to the invention, respectively. The thermodynamic equilibrium composition thereof may be adjusted via the reaction components introduced such as gases having proportional contents of CO, CO.sub.2, H.sub.2O, H.sub.2, NH.sub.3 etc. as a function of pressure and temperature in the stream of the conveyor gas to an oxygen residual potential that is controllable within a wide range. Such reactive gas atmospheres having an optionally exothermic or endothermic character have been known to those skilled in the art, for example, from the field of reactive oven atmospheres for metallurgical processes. In this way, with the method according to the invention oxidation, carbonization and nitration processes or alternatively oxide-free powder production methods for very oxidation-sensitive produces, such as, for example, chromium containing stainless steels, the contamination-free production thereof in common inert gas atmospheres would not be possible on the sole basis of nitrogen or argon, are made accessible. Finally, deviating from the embodiment of the method according to the invention as a cycle process, the method according to the invention may also be realized as an open method, in which various gases or gas mixtures may be used as atomization gas 6 and conveyor gas 7. In this way, for example, passivation of the material powder may only be achieved by the conveyor gas 7.

[0050] FIG. 3 shows the influence of the conveyor gas pressure onto the particle size of the material powder by way of the exemplary production of aluminium powder by means of a crucible nozzling by the method according to the invention. FIG. 3 shows the ratio of the mean particle diameter for a given mass d50 (mass-median-diameter MMD) vs. the mass ratio of atomization gas 7 to molten material mass (M′gas/M′liq). Curve A of the diagram in FIG. 3 represents the relationship mentioned for a conveyor gas pressure of one bar, curve B for four bar and curve C for ten bar. It is obvious that an increase of the conveyor gas pressure will surprisingly lead to a reduction of the mean particle diameter of the material powder produced.

[0051] The applicant has furthermore performed, using the atomization device 3 depicted in FIG. 2b according to the plasma atomization method, with the method according to the invention, experiments for determining the mean particle diameter d50 and the distribution range of the particle diameter as a function of the conveyor gas pressure. The results of these experiments are summarized as examples in table 1 and FIG. 4. The results shown in table 1 were obtained using copper as material 5:

TABLE-US-00001 TABLE 1 Conveyor gas pressure Mean particle Distribution range p [bar] diameter d50 [μm] (d90 − d10)/d50 7 19.84 1.33 4 28.61 1.43 2 43.82 1.58

[0052] Comparable results were obtained with the method according to the invention using various steels, molybdenum and various metal alloys.

[0053] In the following there are indicated two further exemplary embodiments of the method according to the invention.

Exemplary Embodiment 1

[0054] In this exemplary embodiment of the method according to the invention 50 kg/h aluminium are molten at 750° C. Argon is selected as an atomization gas 6, which is then introduced at a rate of 150 kg/h at a temperature of 500° C. The respective pressure ratios are:

[0055] conveyor gas pressure: 3 bar

[0056] atomization gas pressure: 10 bar

[0057] Due to the supply of the atomization gas 6 and the conveyor gas 7 this results in a system pressure in the pressurized container 4 of 4 bar.

[0058] In this way, aluminium particles having a mean diameter d50.3 of smaller than 10 μm are producing, having a distribution range of d84/d50<1.6.

Exemplary Embodiment 2

[0059] Molten stainless steel is produced at a rate of 20 kg/h in a light arc 13 generated by a welding power source. The stream of atomization gas 6 is introduced into the atomization device 3 at a mass flow rate of 150 kg/h and atomizes the molten stainless steel. The light arc 13 may be reduced by the conveyor gas pressure in the pressurized container 4 or by the counter-pressure acting thereon, respectively. This leads to very homogenous atomization conditions. The atomized stainless steel particles have a mean diameter d50.3 of 22 μm and a distribution range of d84/d50=1.38.