WO2023006277A1 - Passivierungsvorrichtung, filtersystem, vorrichtung zur additiven herstellung dreidimensionaler objekte, verfahren zum passivieren und verfahren zum filtern - Google Patents
Passivierungsvorrichtung, filtersystem, vorrichtung zur additiven herstellung dreidimensionaler objekte, verfahren zum passivieren und verfahren zum filtern Download PDFInfo
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- WO2023006277A1 WO2023006277A1 PCT/EP2022/064732 EP2022064732W WO2023006277A1 WO 2023006277 A1 WO2023006277 A1 WO 2023006277A1 EP 2022064732 W EP2022064732 W EP 2022064732W WO 2023006277 A1 WO2023006277 A1 WO 2023006277A1
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- Prior art keywords
- filter
- fluid
- passivation
- filter residue
- chamber
- Prior art date
Links
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Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D46/00—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours
- B01D46/0084—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours provided with safety means
- B01D46/0091—Including arrangements for environmental or personal protection
- B01D46/0093—Including arrangements for environmental or personal protection against fire or explosion
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D46/00—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours
- B01D46/42—Auxiliary equipment or operation thereof
- B01D46/48—Removing dust other than cleaning filters, e.g. by using collecting trays
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B22—CASTING; POWDER METALLURGY
- B22F—WORKING METALLIC POWDER; MANUFACTURE OF ARTICLES FROM METALLIC POWDER; MAKING METALLIC POWDER; APPARATUS OR DEVICES SPECIALLY ADAPTED FOR METALLIC POWDER
- B22F10/00—Additive manufacturing of workpieces or articles from metallic powder
- B22F10/70—Recycling
- B22F10/73—Recycling of powder
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B22—CASTING; POWDER METALLURGY
- B22F—WORKING METALLIC POWDER; MANUFACTURE OF ARTICLES FROM METALLIC POWDER; MAKING METALLIC POWDER; APPARATUS OR DEVICES SPECIALLY ADAPTED FOR METALLIC POWDER
- B22F10/00—Additive manufacturing of workpieces or articles from metallic powder
- B22F10/70—Recycling
- B22F10/77—Recycling of gas
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B33—ADDITIVE MANUFACTURING TECHNOLOGY
- B33Y—ADDITIVE MANUFACTURING, i.e. MANUFACTURING OF THREE-DIMENSIONAL [3-D] OBJECTS BY ADDITIVE DEPOSITION, ADDITIVE AGGLOMERATION OR ADDITIVE LAYERING, e.g. BY 3-D PRINTING, STEREOLITHOGRAPHY OR SELECTIVE LASER SINTERING
- B33Y30/00—Apparatus for additive manufacturing; Details thereof or accessories therefor
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B33—ADDITIVE MANUFACTURING TECHNOLOGY
- B33Y—ADDITIVE MANUFACTURING, i.e. MANUFACTURING OF THREE-DIMENSIONAL [3-D] OBJECTS BY ADDITIVE DEPOSITION, ADDITIVE AGGLOMERATION OR ADDITIVE LAYERING, e.g. BY 3-D PRINTING, STEREOLITHOGRAPHY OR SELECTIVE LASER SINTERING
- B33Y40/00—Auxiliary operations or equipment, e.g. for material handling
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B22—CASTING; POWDER METALLURGY
- B22F—WORKING METALLIC POWDER; MANUFACTURE OF ARTICLES FROM METALLIC POWDER; MAKING METALLIC POWDER; APPARATUS OR DEVICES SPECIALLY ADAPTED FOR METALLIC POWDER
- B22F12/00—Apparatus or devices specially adapted for additive manufacturing; Auxiliary means for additive manufacturing; Combinations of additive manufacturing apparatus or devices with other processing apparatus or devices
- B22F12/70—Gas flow means
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B22—CASTING; POWDER METALLURGY
- B22F—WORKING METALLIC POWDER; MANUFACTURE OF ARTICLES FROM METALLIC POWDER; MAKING METALLIC POWDER; APPARATUS OR DEVICES SPECIALLY ADAPTED FOR METALLIC POWDER
- B22F2999/00—Aspects linked to processes or compositions used in powder metallurgy
Definitions
- the present invention relates to a passivation device, a filter system comprising such a passivation device, a device for the additive manufacture of three-dimensional objects comprising such a filter system, a passivation method a filter residue occurring in a filter device and a method for filtering a process gas.
- Devices and methods for the additive manufacturing of three-dimensional objects are used, for example, in methods referred to as “rapid prototyping", “rapid tooling” and “additive manufacturing”.
- rapid prototyping "rapid tooling” and “additive manufacturing”.
- An example of such a process is known under the name “selective laser sintering" or "selective laser melting”.
- a layer of a build-up material is repeatedly applied and the build-up material in each layer is selectively solidified by selectively irradiating the cross-section of the object to be produced in this layer with a laser beam, for example by exposing the build-up material at these locations to the beam provided by the laser beam Energy is partially or completely melted and the melt then solidifies on cooling. Further details are described in EP 2978589 B1, for example.
- a process gas atmosphere is often maintained in the process chamber in which the building material is selectively treated by means of radiation.
- the process gas atmosphere is usually an inert gas atmosphere (also referred to as a "protective gas atmosphere"), since some construction materials, especially if they contain metal, tend to oxidize at the high temperatures that occur, which prevents the formation of objects or at least the formation of objects with the desired material structure would prevent.
- an inert gas atmosphere also referred to as a "protective gas atmosphere”
- some construction materials especially if they contain metal, tend to oxidize at the high temperatures that occur, which prevents the formation of objects or at least the formation of objects with the desired material structure would prevent.
- titanium could start burning uncontrollably in the presence of oxygen.
- a flow of process gas is passed over the construction level, ie the surface of a construction material layer to be solidified.
- part of the building material is often vaporized as a result of the irradiation, which leads to the formation of condensates after the vapors formed have resolidified.
- part of the construction material is often stirred up during the process.
- spatter can form during the process. These are often solidified droplets of the melt of the building material with a diameter of between 20 and 300 ⁇ m, for example. For example, when the laser beam pierces, spatter is thrown out of the resulting melt or the melt pool. Such spatter can also contaminate the process gas. Because of the condensates and/or the build-up material whirled up and/or the spatter and/or other impurities in the form of particles or droplets carried along by the process gas, it is necessary to free the process gas from these undesired ones. This is particularly the case when the process gas is circulated, i.e.
- US 2014/0287080 describes how a closed gas flow circuit is provided for this purpose, with which a gas flow is guided through the process chamber of a selective laser melting device, with two filter devices being arranged in the gas flow circuit, each having a filter element.
- DE 102014207160 A1 describes a cyclical cleaning of a filter element of a circulating air filter device by means of a gas pressure surge.
- metal-containing or metallic structural materials e.g. titanium or titanium alloys
- the particles tend to react with oxidative materials at high temperatures, with the reaction rate increasing at high temperatures.
- Metal condensate can self-ignite spontaneously at room temperature and in contact with atmospheric oxygen, so it is usually pyrophoric.
- the amount of additive particles is selected in such a way that the mixture of these particles with dust that has been introduced does not represent a combustible mixture, at least until an upper filling level of a dust container is reached.
- Calcium carbonate particles and silicon dioxide particles are mentioned as additive particles in connection with aluminum dust.
- additional particles in addition to their provision and their costs, it is also accepted that the upper filling level will be reached more quickly, so that the dust container has to be emptied more often.
- the additive particles can also be referred to as "filter aid”.
- DE 102017207415 A1 describes the treatment of particles separated by a filter element in a separate treatment chamber outside the filter chamber. The formation of superficial oxide layers on the particles by adding oxygen to the treatment chamber in which the particles are located is described.
- the object of the present invention is to provide an alternative or improved passivation device or an alternative or improved filter system or an alternative or improved device for the additive production of three-dimensional objects or an alternative or improved method for passivating a filter residue occurring in a filter device or a to provide an alternative or improved method for filtering a process gas.
- This object is achieved by the passivation device according to claim 1, the filter system according to claim 11, the device for the additive manufacturing of three-dimensional objects according to claim 19, the system for the additive manufacturing of three-dimensional objects according to claim 20, the method according to claim 21 and the method according to claim 26
- Further developments of the invention are specified in the dependent claims. The methods can also be further developed by the features of the devices listed in the following description and in the dependent claims.
- the passivation device according to the invention is a passivation device for passivating a filter residue occurring in a filter device.
- the passivation device according to the invention comprises an outlet region which can be directly or indirectly coupled or is coupled to the filter device and which is designed to receive filter residue from the filter device.
- the passivation device according to the invention also includes a fluid supply for supplying a fluid flow from a fluid, which can include a passivating agent, into the outlet area.
- the passivation device according to the invention also includes a fluid discharge for discharging the fluid flow and the filter residue from the outlet area.
- the passivation device according to the invention also comprises an energy supply device for applying energy to the fluid flow and/or the filter residue.
- the passivation device optionally comprises a passivation agent supply for adding a passivation agent to the fluid flow.
- the passivation device according to the invention is designed and/or controllable to bring about a chemical reaction between the filter residue and the passivation agent at least partially in the entrained flow.
- the filter device can be or is coupled directly and/or indirectly to the outlet area.
- the term "indirect coupling” is used when an intermediate chamber, a connecting line, a pipe or the like is provided between the filter device and the outlet area.
- An intermediate chamber or a connecting line is a chamber or line that is arranged between the filter device and the outlet area, so that filter residue, for example, has to pass through the intermediate chamber or connecting line in order to get from the filter device into the outlet area.
- directly docking occurs when an intermediate chamber and connecting conduit are absent.
- the filter device is preferably detachably coupled or can be coupled to the outlet area. This means that the components coupled to one another can be separated again.
- the area mentioned is therefore referred to as the "exit area” because it is the area of the passivation device into which the filter residue exiting the filter device first reaches before it is conveyed further with the fluid flow through the fluid discharge.
- energy e.g. in the form of thermal energy
- a reaction between the filter residue and the passivation agent is accelerated or brought about, for example.
- chemical reactions often run faster at elevated temperatures or the activation energy barrier can often be overcome by elevated temperatures, so that the chemical reaction only begins when energy is applied.
- mass transport e.g. passivating agent supply
- the reaction rate can increase exponentially with temperature, for example.
- a liquid for example an oil (e.g. silicone oil), can be used, which wets the filter residue and thus protects it from unwanted oxygen ingress.
- a liquid can, for example, be added to the filter residue in the waste container.
- the filter residue is usually indirectly energized when energy is added to the fluid flow and vice versa.
- relatively rapid thermal equilibration occurs between the particles of filter cake and the fluid of the fluid stream with which the particles are in contact, particularly in the case of small particles.
- the passivation device is designed and/or controllable to bring about a chemical reaction between the filter residue and the passivation agent at least partially in the entrained flow.
- the term "partly” means that the chemical reaction not only has to take place in the entrained flow, but can also take place in part when the filter residue and the passivating agent are not yet or no longer in the state of an entrained flow.
- the chemical reaction can continue at least to a certain extent after the filter residue has been transported by the fluid flow, i.e. in an entrained flow, to a catchment.
- the chemical reaction does not have to be complete, i.e. the filter residue does not have to be completely chemically converted by the passivating agent.
- the particles of the filter residue form a superficial passivation layer as a result of the chemical reaction.
- a passivation layer can serve, for example, as a protective layer and prevent the particles from being oxidized when they come into contact with oxygen.
- an oxide layer produced in a targeted manner by means of passivation can prevent titanium particles from reacting unintentionally when they come into contact with oxygen or air.
- An entrained flow is understood to mean a two-phase flow of a fluid and a particulate solid, i.e. a flowing aerosol.
- the contact between the fluid and the solid and the movement can, for example, enable an intensive and rapid mass and/or heat exchange.
- the desired chemical reaction can in turn be accelerated or made possible in the first place.
- the use of a fluid stream is therefore provided for three purposes in a combined manner: First, the fluid stream serves to convey the filter residue from the outlet area, where it emerges from the filter device, through the conveying line. This allows the filter residue to be transported to a collection point, e.g. a waste container. Secondly, the fluid flow serves to generate an entrained flow, which accelerates the chemical reaction for passivation, for example. Thus, the filter residue can be removed from the delivery line in a passivated state, for example exit.
- the passivating agent is contained within the fluid stream. This can, for example, simplify the passivation and thus the passivation device compared to a separate addition of passivating agent. Intensive mixing in the entrained flow can also be particularly advantageous, for example, if a solid powder, for example lime powder and/or silicon dioxide powder (quartz powder) and/or glass powder, is used as an inerting agent in addition to the passivating agent in order to increase the combustibility and/or flammability of the filter residue to reduce.
- a solid powder for example lime powder and/or silicon dioxide powder (quartz powder) and/or glass powder
- glass powder proves to be advantageous because it melts at lower temperatures than, for example, quartz powder, so that even at relatively low temperatures the filter residues can be at least partially covered with glass melt or solidified glass melt, which can lead to a reduction in the risk of fire .
- the filter residue can, for example, be mechanically stressed by the entrained flow, for example by the particles of the filter residue colliding with one another and/or against a wall and/or against particles of an inerting agent. As a result, it may be possible, for example, for the filter residue particles to at least partially break up into smaller particles. In particular, in this way, for example, agglomerates of relatively weakly bonded primary particles can be broken up.
- broken agglomerates can, for example, be easier to passivate than unbroken agglomerates.
- inerting agents with sharp-edged particles can be well suited for this.
- a more effective passivation of the filter residue can be achieved by the invention, for example, and the risk of waste igniting itself can be reduced or completely eliminated. This can, for example, enable the waste or the container containing the waste to be removed safely.
- the promotion in the entrained flow can lead to homogenization and compaction of the waste produced, consisting of filter residue and optionally filter aid come, whereby, for example, the service life of a container for the waste can be reduced.
- the fluid discharge of the passivation device according to the invention is preferably designed as a conveying line.
- the conveying line preferably has an inner diameter of at least 2 mm and/or at most 60 mm, at least in one area.
- the conveying line more preferably has an inner diameter of at least 10 mm and/or at most 50 mm, even more preferably at least 20 mm and/or at most 40 mm.
- the conveying line has the mentioned inner diameter at least in a region of its length, but in particular along its entire length.
- the fluid discharge of the passivation device according to the invention is preferably designed as a conveying line.
- the conveying line preferably has a length and an inside diameter averaged over the length for which the ratio of length to average inside diameter is at least 30:1.
- the length of the delivery line is defined as the length of the delivery line between its first end, which is connected to the outlet area and at which the fluid stream enters, and its second end, at which the fluid stream exits and which is connected, for example, to a collector (see below) is connected, understood.
- the inner diameter averaged over the length is understood to mean the average inner diameter, i.e. the inner diameter arithmetically averaged over the entire length of the delivery line. For example, if the inside diameter is constant over the entire length of the delivery line, e.g.
- the delivery line is a cylindrical tube, this constant inside diameter is equal to the average inside diameter.
- the inner diameter is understood in the context of this invention as the diameter of a circular area that has the same surface area as the clear cross-section of the conveying line.
- the fire protection behavior and/or the explosion protection behavior of the passivation device can be improved, for example, since the risk of an unintentional fire or an unintentional explosion from one area of the passivation device propagating through the conveyor line to another area of the passivation device is reduced becomes.
- the delivery line has a diameter that is sufficient for effective delivery.
- the maximum gap width (MESG) for a specific gas mixture is a measure that is determined in a standardized procedure (international standard IEC (International Electrotechnical Commission) 60079-1).
- the maximum width a 25 mm long gap in a container of the gas can have so that ignition is still prevented (EN (European standard) 60079-20-1) is determined. This measure is not directly applicable to the present invention.
- the standard geometry of a 25 mm long gap does not correspond to the typical geometry of the cross-section of the conveying line.
- the fire and ignition properties of the fluid conveyed through the conveying line depend on the composition of the fluid and above all on the nature (chemical composition, surface area, particle size, etc.) and the concentration of the filter residue conveyed by the conveying fluid.
- the principle underlying the dimension of the limit gap width is applicable to the present invention. It states that a relatively small cross-section of a line makes it difficult or impossible to ignite out of the line, into the line and through the line.
- a conveyor line can be provided, for example, which corresponds to an entrained flow long enough for effective passivation and with which the advantageous fire protection behavior and/or explosion protection behavior described above can be implemented is.
- the fluid discharge of the passivation device according to the invention is preferably designed as a conveying line.
- the passivation device is preferably designed and/or controllable in such a way that a dwell time of the filter residue in the delivery line of at least 0.1 s, more preferably at least 0.15 s, even more preferably at least 0.
- the dwell time in the conveying line is the time that a filter residue particle requires on average to be transported from the beginning to the end of the conveying line, in particular along the entire route in the entrained flow. This gives the filter residue, for example, sufficient time for the application of energy and the chemical reaction, preferably without making the delivery line unnecessarily long.
- the passivation device is preferably designed to convey the filter residue exclusively by means of the fluid flow. This means that, for example, an additional mechanical conveyor device such as a screw conveyor can be dispensed with.
- the passivation device is preferably designed to convey the fluid flow at least in the area of the outlet area and the fluid discharge without the influence of a turbomachine and without the influence of a piston machine.
- a turbomachine is a machine for conveying a fluid by means of rotor blades, vanes, vanes or other driven components. Due to the fact that the conveyance in this area, in which the fluid flow is loaded with filter residue, takes place without such a machine, the maintenance effort or the susceptibility to failure of the passivation device can be reduced, for example because devices with driven components are particularly sensitive to contamination with solids.
- the conveyance of the filter residue in the fluid discharge is preferably independent of gravity.
- the fluid discharge can be oriented as desired in space, which is accompanied by improved flexibility in the construction of the passivation device, so that the passivation device can be arranged in a more space-saving manner, for example.
- the energy supply device is preferably a heating device, in particular a heating device which is designed to heat the fluid flow while it flows through the heating device.
- a heating device for example, energy can be provided in a form with which the passivation reaction can be accelerated or initiated in an effective manner, since chemical reactions often take place more quickly at elevated temperatures or the activation energy barrier can often be overcome by elevated temperatures.
- the energy supply device is arranged such that the fluid stream is heated to a predefined minimum target temperature before it enters the exit region.
- the filter residue can already be charged with energy when it comes into contact with the fluid flow, so that the reaction is accelerated or initiated at an early stage and thus the longest possible reaction time and/or the highest possible conversion are achieved.
- the energy supply device is preferably designed and arranged to supply energy to at least one element selected from the group consisting of fluid supply, outlet region and fluid discharge in order to apply energy to the fluid flow.
- the energy supply device can be arranged, for example, at a point on the passivation device at which it effectively introduces energy for accelerating or initiating the desired chemical reaction.
- the fluid supply preferably includes a nozzle, which is designed and/or arranged in such a way that the fluid flow conducted through the nozzle is accelerated in such a way that a suction pressure for conveying the filter residue out of the filter device and a fluid optionally located in the filter device into the outlet area are generated , wherein the filter residue is conveyed with the fluid flow through the fluid discharge from the outlet area, wherein the nozzle is more preferably designed as an ejector nozzle or Venturi nozzle and/or wherein the nozzle is more preferably designed, a speed and/or a diameter of the material passing through the nozzle set fluid flow.
- a suction nozzle can, for example, effectively transport the filter residue from the filter device into the passivation device.
- an ejector nozzle can provide this suction effect.
- an ejector is a jet pump in which the pumping effect is generated by the flow of your flow of pumping fluid (also known as "driving medium"), so that another medium (also known as "suction medium”) is sucked in and pumped.
- the filter residue is included in the suction medium or is sucked out of the first collection area together with the suction medium in the form of a fluid.
- the media are preferably mixed, so that a corresponding mixture is conveyed through the conveying line.
- the present invention is not limited to the use of an ejector, which will become clear from the following description of exemplary embodiments without an ejector.
- the filter residue it is possible, for example, for the filter residue to reach the outlet area under the effect of gravity and to be caught there by a fluid flow and transported further, with the fluid flow being generated by a fan, for example.
- the use of an ejector has proven to be advantageous in many cases, for example because in the ejector or downstream of the ejector an effective breaking up of Filter residue particles can be done without requiring a separate device such as a cross-sectional constriction in the delivery line is required.
- the delivery line preferably includes a check valve.
- the delivery line can be shut off in a fluid-tight manner when a collector connected to one end of the delivery line is uncoupled, so that no material can escape from the passivation device or enter the passivation device.
- the shut-off valve is more preferably arranged in the region of the end of the delivery line which is connected or can be connected to a catchment.
- the delivery line is preferably designed as a rigid line, more preferably as a metal tube, even more preferably a metal tube with a wall thickness of at least 0.5 mm, more preferably at least 1 mm, even more preferably at least 2 mm, particularly preferably at least 5 mm .
- a rigid line in particular a rigid line made of a metallic material such as a metal tube, can provide sufficient stability.
- a metal pipe can be sufficiently pressure-resistant.
- the delivery line is preferably thermally insulated.
- the filter residue and the fluid in the delivery line can be kept at an elevated temperature, which can be desirable, for example, if the filter residue is to react chemically with the fluid because an elevated temperature accelerates the chemical reaction (e.g. oxidation with the fluid contained oxygen).
- the passivation device preferably comprises a catch for collecting passivated filter residue, the catch being in fluid connection with the outlet area via the delivery line without check valve or the delivery line when the check valve is open. For example, passivated filter residue can be collected in a catchment area for subsequent treatment or disposal.
- a catch is a container.
- the passivation device preferably comprises a passivation agent supply for supplying the passivation agent.
- the fluid that initially forms the fluid flow can be taken from a fluid reservoir that does not contain the passivating agent.
- a commercially available compressed gas bottle filled with inert gas e.g. argon or nitrogen
- Such a fluid can be mixed with the passivating agent by the later addition via the passivating agent feed. It is further preferred if the amount of passivating agent added per unit of time is adjustable and/or controllable.
- the passivating agent feed is in particular designed and arranged to feed passivating agent to at least one element selected from the group consisting of fluid feed, outlet region and fluid discharge.
- the passivating agent can be supplied at the point in the passivating device at which the passivating agent is required for the desired chemical reaction.
- the passivating agent is preferably an oxidizing agent which is suitable for at least partially oxidizing the filter residue. In this way, for example, filter residues that contain a metal can be passivated and an unwanted later reaction with oxygen (e.g. air) can be avoided.
- the oxidizing agent more preferably comprises oxygen, even more preferably the oxidizing agent is oxygen, with the passivating agent being supplied in particular in the form of a mixture of oxygen and an inert gas, in particular argon.
- oxygen for example, an oxidizing agent can be used with which filter residues that tend to react spontaneously with air can be passivated.
- Oxygen means in particular O 2 understood.
- ozone is also possible.
- oxidizing agents which contain oxygen in a different form for example peroxides such as hydrogen peroxide.
- the use of oxidizing agents that are not based on oxygen is possible within the scope of the present invention. Chlorine or a chlorine-based oxidizing agent is conceivable.
- an inert substance e.g. inert fluid, inert gas, etc.
- inert fluid inert gas, etc.
- nitrogen and/or argon can serve as the inert fluid (an inert gas in the specific case).
- the passivation device preferably also comprises a fluid reservoir containing a fluid, in particular a pressurized gas reservoir containing a pressurized gas, the fluid supply providing a fluid connection between the fluid reservoir and the outlet area, and the fluid contained in the fluid reservoir at least partially including the passivating agent and/or wherein the passivating agent is at least partially fed into the fluid supply and/or the fluid discharge and/or the outlet area by a passivating agent feed from a passivating agent reservoir and/or in the form of air from the atmosphere.
- a fluid reservoir containing a fluid in particular a pressurized gas reservoir containing a pressurized gas
- the fluid supply providing a fluid connection between the fluid reservoir and the outlet area
- the fluid contained in the fluid reservoir at least partially including the passivating agent and/or wherein the passivating agent is at least partially fed into the fluid supply and/or the fluid discharge and/or the outlet area by a passivating agent feed from a passivating agent reservoir and/or in the form of air from the atmosphere.
- the fluid supply and the fluid reservoir and optionally the passivating agent reservoir are designed or adjusted or controllable, so that in the outlet area or an area of the fluid discharge the fluid flow is a gas flow made of a mixture of inert gas, in particular argon, and O 2 is present with an adjustable O 2 salary and/or with an O 2 content in a range of at least 0.01% by volume, more preferably at least 0.1% by volume, even more preferably at least 1% by volume and/or at most up to 20.8% by volume, more preferably at most 10% by volume, more preferably at most 5% by volume and/or with an O 2 - Content below the limiting oxygen concentration, more preferably at least 1%, even more preferably at least 2%, most preferably at least 3% below the limiting oxygen concentration.
- the oxygen content can be adjusted so that effective oxidation can take place while still ensuring the safety of the passivation device.
- concentration ranges given can provide a suitably reactive atmosphere in many cases.
- the limiting oxygen concentration is the maximum oxygen concentration of an oxygen-containing gas mixture, an oxygen-containing aerosol, etc., at which an explosion does not occur.
- the risk of explosion can be reduced or completely eliminated by falling below the limit oxygen concentration.
- An explosion inside the filter device is undesirable for safety reasons.
- controlled oxidation with oxygen can be carried out under safe conditions.
- the risk of explosion can be reduced even in the event of a fault.
- the fluid supply is preferably connected to the filter chamber in such a way that at least part of the filtered process gas is conveyed into the outlet area, with the fluid supply more preferably comprising a turbomachine, in particular a blower.
- filtered process gas i.e. clean gas
- filtered process gas can, for example, be used as the fluid for generating the fluid flow, so that the provision of an additional fluid can be dispensed with or the need for additional fluid is reduced.
- the conveying line preferably comprises at least one locally limited cross-sectional constriction, with an inner cross-sectional area of the conveying line in the region of the cross-sectional constriction being reduced by at least 25%, even more preferably at least 50%, particularly preferably at least 75% compared to an inner cross-sectional area upstream of the cross-sectional constriction.
- Such a narrowing of the cross section can, for example, lead to a local acceleration of the fluid flow and thereby to additional mechanical stress on the filter residue. As a result, can e.g. breaking up filter residue particles into smaller particles.
- the filter system according to the invention is a filter system which comprises: a) at least one filter device, each comprising aa) at least one filter chamber, bb) at least one filter element arranged in the filter chamber and cc) optionally a collection chamber coupled to the filter chamber, which preferably can be separated from the filter chamber in a fluid-tight manner by a shut-off device, and b) at least one passivation device according to the invention which is directly or indirectly coupled to the at least one filter device or is connected to the at least one filter device by a transport device for transporting the filter residue.
- Such a system can be used, for example, to filter a process gas, in particular the process gas of a device for additively manufacturing three-dimensional objects, and to passivate the filter residues that occur in the process.
- filtering a process gas means that the process gas, which is cleaned of impurities that are not gaseous, is cleaned by at least partially separating off these impurities.
- Process gas is also commonly referred to as "raw gas” before filtering, while process gas is also commonly referred to as "clean gas” after filtering.
- a passivation device of the system is preferably assigned to a plurality of filter devices. As a result, for example, the capacity of the passivation device can be optimally utilized.
- a passivation device can, for example, be better utilized if it takes care of the passivation of the filter residue from several filter devices.
- a filter device can comprise a plurality of filter chambers, in each of which at least one filter element is arranged. Several filter chambers of a filter device can be connected in parallel.
- a passivation device can be associated with a filter device having one or more filter chambers.
- a passivation device can also be associated with a plurality of filter devices, each with one or more filter chambers.
- a filter device can be used for filtering the process gas of a number of devices for the additive production of three-dimensional objects.
- the filter device can have a plurality of filter chambers, with one filter chamber being able to be assigned to each device for the additive production of three-dimensional objects at a time.
- the number of filter chambers is more preferably greater than the number of devices for the additive manufacturing of three-dimensional objects, so that for example at a certain point in time only some of the filter chambers are filtering process gas, while for the other part a cleaning of the at least one filter element and/or or the passivation of the filter residue can be carried out.
- An example of such an overall system for the additive production of three-dimensional objects could consist, for example, of three devices for the additive production of three-dimensional objects, a filter device with four filter chambers and a passivation device. Furthermore, several filter devices, each with at least one filter chamber, can be used for filtering the process gas of several devices for the additive manufacturing of three-dimensional objects, wherein a filter device can be assigned to each device for the additive manufacturing of three-dimensional objects at a time.
- the number of filter devices is more preferably greater than the number of devices for the additive manufacturing of three-dimensional objects, so that, for example, at a certain point in time only some of the filter devices are currently filtering process gas, while for the other part a cleaning of the at least one filter element and/or or the passivation of the filter residue can be carried out.
- a An example of such an overall system for the additive production of three-dimensional objects could consist, for example, of three devices for the additive production of three-dimensional objects, four filter devices and a passivation device.
- the filter chamber preferably has a collection area, with the collection area being arranged below the at least one filter element in the operating position.
- the collection area has a wall that tapers downwards and opens into a filter chamber outlet that is connected to the passivation device or the collection chamber.
- a conveying device for conveying filter residue is preferably provided at least in a partial area of the collection area, in particular in a partial area with a lower inclination to the vertical relative to other partial areas, with the conveying device more preferably being a solid fluidization device, in particular a Fluidizing plate, and / or one or more gas nozzles for introducing gas pulses.
- a solids fluidization device can ensure, for example, that filter residue that remains on the wall of the filter chamber slides down or is conveyed down.
- the filter chamber in particular the collection area, is preferably designed in such a way that the passivation device and a collection chamber optionally included in the filter device can be arranged at least partially below the filter chamber in the operating position, with a collector optionally included in the passivation device being able to be arranged at least partially below the filter chamber is.
- a space-saving arrangement can thereby be possible, for example.
- the filter system preferably comprises an application device for applying a filter aid, in particular a powdered filter aid, to the at least one filter element.
- Filter residues can be rendered inert by using a filter aid.
- the use of a filter aid can also be used in addition to the use of a passivating agent such as an oxidizing agent (e.g. O 2 ) be provided.
- the use of a filter aid can be particularly effective, for example, in combination with the entrained flow according to the invention, for example because good mixing of filter residue and filter aid can be possible as a result of the recirculation.
- the function of the filter aid is, according to one non-limiting theory, to provide thermal ballast and/or to spatially separate the filter residue particles to slow or moderate a chemical reaction of the filter residue.
- the filter aid preferably includes a filling level sensor for measuring a quantity of filter residue detached from the at least one filter element in the filter chamber, in particular in the collection area and/or in the optional collection chamber.
- the filter system comprises precisely one filter device, with the passivation device being coupled directly or indirectly to the filter chamber or to the optional collection chamber.
- the entire filter residue to be passivated which is in a Filter device accumulates, are treated in a passivation device available only for this purpose.
- Such a filter system can form an overall system together with a device for the additive production of three-dimensional objects or together with several such devices.
- the filter device can be used to filter the process gas of one or more devices for the additive manufacturing of three-dimensional objects.
- the filter system comprises at least two filter devices and a transport device for transporting the filter residue from the at least two filter devices to the passivation device, with the transport device more preferably being a suction device.
- the transport device more preferably being a suction device.
- the number of passivation devices required can be reduced, for example when operating a plurality of filter devices.
- Such a filter system can form an overall system together with a device for the additive production of three-dimensional objects or together with several such devices.
- the at least two filter devices can each be used to filter the process gas of one or more devices for additively manufacturing three-dimensional objects. It is also possible for a number of filter devices to be used at the same time to filter the process gas of a device for additively manufacturing three-dimensional objects.
- the filter system comprises at least two filter devices, with the passivation device being coupled directly or indirectly to one of the filter devices, and a transport device for transporting the filter residue from at least one other of the filter devices to the passivation device, with the transport device preferably being a suction device.
- the number of passivation devices required can be reduced, for example when operating a plurality of filter devices.
- Such a filter system can form an overall system together with a device for the additive production of three-dimensional objects or together with several such devices.
- the at least two filter devices can be assigned to a specific Time each serving the filtering of the process gas one or more devices for the additive manufacturing of three-dimensional objects.
- the filter system comprises at least two filter devices and a transport device for transporting the filter residue from at least one of the filter devices into the collection chamber of at least one further filter device, with the transport device preferably being a suction device.
- the number of passivation devices required can be reduced, for example when operating a plurality of filter devices.
- Such a filter system can form an overall system together with a device for the additive production of three-dimensional objects or together with several such devices.
- the at least two filter devices can each be used to filter the process gas of one or more devices for additively manufacturing three-dimensional objects. It is also possible for a number of filter devices to be used at the same time to filter the process gas of a device for additively manufacturing three-dimensional objects.
- the at least two filter devices are preferably assigned or can be assigned to different devices for the additive production of three-dimensional objects (e.g. different systems for selective laser sintering). As a result, the number of passivation devices required can be reduced, for example when operating a plurality of additive manufacturing devices.
- a filter system according to the invention can also include more than one passivation device.
- the device according to the invention for the additive manufacturing of three-dimensional objects comprises: - a process chamber in which the additive manufacturing takes place, - a process gas conveying device for conveying a process gas flowing through the process chamber from a process chamber inlet to a process chamber outlet, the process gas conveying device being designed to convey between the process chamber inlet and the process chamber outlet, preferably at least partially in circulation, - a filter system according to the invention.
- the at least one filter chamber is arranged in such a way that the process gas emerging from the process chamber is filtered by the at least one filter element.
- the device according to the invention for additive manufacturing makes it possible to provide a device, for example, during operation of which the above-described advantageous properties of the filter system according to the invention or the passivation device according to the invention can be implemented.
- the passivation device according to the invention and the filter system according to the invention can be constructed in such a way that a conventional device for additive manufacturing can be retrofitted with a process chamber and a process gas conveying device. If the conventional device for additive manufacturing has a filter device, this can be exchanged for retrofitting, for example with the filter system according to the invention.
- the passivation device according to the invention can be supplemented. Alternatively, for example, the missing components can also be retrofitted.
- the system according to the invention for the additive manufacturing of three-dimensional objects comprises at least two devices for the additive manufacturing of three-dimensional objects, the devices each having a process chamber, in which the additive manufacturing takes place, and a process gas conveying device for conveying a process gas flowing through the process chamber from a process chamber inlet to a process chamber outlet, wherein the process gas conveying device is designed in each case to bring about the conveying between the process chamber inlet and the process chamber outlet preferably at least partially in a circuit.
- the system according to the invention for the additive production of three-dimensional objects also includes a filter system according to the invention with at least two filter devices.
- a system for additive manufacturing of three-dimensional objects in which the number of passivation devices required is relatively small, in particular fewer than the number of devices for the system for additive manufacturing of three-dimensional objects.
- one of the at least two filter devices can preferably be assigned or assigned to each device for additive manufacturing. More preferably, the number of filter devices in the system is greater, in particular by 1, than the number of additive manufacturing devices.
- An example of a system according to the invention for the additive production of three-dimensional objects could, for example, comprise three devices for the additive production of three-dimensional objects, four filter devices, each with a filter chamber, and a passivation device.
- a system according to the invention for the additive production of three-dimensional objects can, for example, also comprise more than one passivation device.
- the method according to the invention for passivating a filter residue occurring in at least one filter device comprises the steps: - feeding filter residue emerging from the at least one filter device into an outlet area, in particular by suction, - feeding a fluid stream into the outlet area, - removing the fluid stream loaded with the filter residue from the exit area, - Applying energy to the fluid flow, in particular heating the fluid flow, wherein the application of energy to the fluid flow before the supply and/or during the supply of the fluid flow into the outlet area and/or in the outlet area and/or during the discharge and/or after the discharge of the fluid flow from the outlet area takes place.
- a fluid flow consisting of a fluid that includes a passivating agent is used as the fluid flow.
- a passivating agent is added to the fluid flow.
- the filter residue is at least partially passivated in the entrained flow by a chemical reaction with the passivating agent.
- the fluid stream loaded with the filter residue preferably falls below either the lower explosion limit, preferably at most 0.9 times, more preferably at most 0.8 times the lower explosion limit being reached.
- the fluid stream loaded with the filter residue preferably exceeds the upper explosion limit, preferably at least 1.1 times, more preferably at least 1.2 times the upper explosion limit being reached. Explosion limits are the limits of the so-called explosion range.
- the lower explosion limit or the upper explosion limit is the lower or upper limit of the concentration (e.g. mole fraction) of a combustible substance in a mixture of gases, vapours, mists and/or dusts in which a flame that is independent of the ignition source develops after ignition can no longer reproduce independently. If the mixture either falls below the lower explosion limit or exceeds the upper explosion limit, there is no explosive mixture. As a result, for example, by reducing the risk of explosion, safety can be improved when carrying out the method according to the invention for passivation or the operation of a device used for this purpose.
- the passivation preferably results in at least 75%, more preferably at least 85%, even more preferably at least 95% complete chemical conversion of the filter residue particles.
- a passivation layer e.g. B. an oxide layer formed on the filter residue particles, the passivation layer having a layer thickness of at least 0.5 nm, preferably at least 0.75 nm, more preferably at least 1 nm and/or at most 10 nm, preferably at most 5 nm, more preferably at most 2 nm.
- the fluid stream is preferably fed into the outlet area in such a way that a suction pressure is generated in the outlet area, preferably through a nozzle, with the filter residue and any fluid optionally located in the at least one filter device being sucked into the outlet area from the at least one filter device by the suction pressure, and wherein the filter residue is conveyed with the fluid flow through the fluid discharge from the outlet area, with more preferably a speed and/or a diameter of the fluid flow passing through the nozzle being adjusted.
- Such suction can, for example, effectively transport the filter residue out of the filter device into the passivation device.
- an ejector nozzle can provide this suction effect.
- the amount of filter residue that is sucked in per unit of time can be adjusted, for example.
- the fluid flow is preferably adjusted and/or controlled in such a way that particle agglomerates occurring in the filter residue are broken up, in particular in such a way that the filter residue is in the form of particles with a secondary particle diameter after breaking up which is a maximum of 100 times, more preferably a maximum of 50 times , even more preferably at most 10 times, particularly preferably at most 5 times the primary particle diameter and/or a secondary particle diameter of at most 200 ⁇ m, preferably at most 100 ⁇ m.
- the breaking up preferably takes place directly or indirectly through the action of the fluid flow, i.e.
- particle agglomerates are broken up into the primary particles or into agglomerates of a few primary particles. Such a break-up can, for example, promote passivation by a chemical reaction and/or mixing with an inerting agent (e.g. lime powder).
- an inerting agent e.g. lime powder
- metal condensates in particular have a very high specific surface area (e.g.
- the transport of oxygen into the interior of agglomerates is severely impeded, for example Knudsen diffusion could occur.
- the obstruction of the oxygen transport slows down the reaction. Breaking up the agglomerates, according to the non-limiting theory, exposes the surface better or makes the surface more accessible and thus increases the reaction rate.
- the particle size or the particle diameter is preferably understood as meaning the d50 value.
- the d50 value can be used for particles of the construction material and for condensate particles or those contained in them primary particles contained can be determined, for example, by means of laser diffraction according to the established and standardized methods (e.g. according to ISO 13320 or ASTM B822). Alternatively, a determination is possible, for example, using dynamic image analysis (e.g. according to the ISO 13322-2 standard).
- the size of agglomerates can also be given in the form of a d50 value.
- a certain d50 value means that 50% of the particles have a smaller diameter than the stated value.
- Suitable methods for determining the d50 value of agglomerates are, for example, transmission electron microscopy (TEM) and scanning electron microscopy (SEM), the images obtained thereby being subjected to a suitable image evaluation to determine the d50 value. If the conveyor has a nozzle such as an ejector nozzle or a venturi nozzle, it may be possible for the breakup to occur in the nozzle or downstream of the nozzle.
- Such a nozzle can therefore, in addition to its function in conveying the filter residue, have the function, among other things, of ensuring that the filter residue particles are comminuted. If no such nozzle is used, or if additional fracturing is desired, a reduction in the cross-section of the delivery line can be provided.
- the fluid is preferably discharged through the fluid discharge from the outlet area into a catchment. In this way, for example, the filter residue can be transported to a collection point and stored there until further processing or disposal.
- the chemical reaction preferably takes place in the outlet area and/or during the discharge, i.e. while the filter residue is being transported through the conveying line.
- a fluid flow used for the purpose of transporting the filter residue into or out of the outlet area can be used to generate the entrained flow provided for the chemical passivation reaction, without a new generation of a corresponding fluid flow being necessary.
- the method according to the invention for filtering a process gas, in particular a process gas of a device for the additive manufacturing of three-dimensional objects comprises the following steps: - optionally coating at least one filter element with a filter aid, in particular with a powdered filter aid, - passing the process gas through the at least one filter element for filtering out of particles from the process gas, - cleaning the filter element or cleaning at least part of two or more than two filter elements from the filter residue formed from particles filtered out and the optional filter aid, - optionally collecting the filter residue and - passivating the filter residue according to the passivation method according to the invention .
- a process gas When carrying out the method for filtering a process gas, a process gas can be cleaned and the resulting filter residue can be passivated, for example, with the advantages of the method for passivation described above being able to be realized.
- At least two filter elements are preferably used to carry out the method for filtering a process gas, with the cleaning of the filter elements taking place at different times, with a waiting time being observed between two successive cleanings and with the passivation step being carried out at least partially during the waiting time. As a result, for example, the portions of the filter residue produced by a cleaning process can be reduced, while the continuous filtering of the process gas can still be maintained over a longer period of time.
- the at least two filter elements are preferably arranged in different filter chambers.
- Figure 1 is a schematic, partially sectioned view of a passivation device according to a first embodiment of the invention coupled to a filter device.
- Figure 2 is a schematic sectional view of a detail of the passivation device according to the first embodiment.
- Figure 3 is a schematic, partially sectioned view of a passivation device according to a second embodiment of the invention coupled to a filter device.
- Fig. 4 is a schematic view, partly in section, of a filter system according to another embodiment of the invention.
- Fig. 5 is a schematic view, partly in section, of a filter system according to another embodiment of the invention.
- Fig. 6 is a schematic view, partly in section, of a filter system according to another embodiment of the invention.
- Fig. 7 is a schematic view, partly in section, of a filter system according to another embodiment of the invention.
- Fig. 8 is a schematic view, partly in section, of a filter system according to another embodiment of the invention.
- Fig. 9 is a schematic view, partly in section, of an apparatus for the additive manufacturing of three-dimensional objects according to further embodiments of the invention.
- Fig. 10 is a schematic representation of the method for passivating a filter residue according to a further embodiment of the invention.
- Figure 11 is a graph showing the heating of various particles in a gaseous atmosphere as a function of time.
- FIG. 12 is a schematic representation of the method for filtering a process gas according to a further embodiment of the invention.
- the passivation device 1 according to the first embodiment is shown in FIG. 1 in a possible operating position. In this case, the passivation device 1 is coupled to a filter device 10 .
- the passivation device 1 corresponds to the area of FIG. 1 framed with dashed lines. 1 thus shows a filter system 100 according to the invention overall.
- the filter system 100 and the filter device 10 will be discussed in detail further below.
- the filter device 10 is also shown in a possible operating position in FIG.
- the process gas can be, for example, the process gas of a device for the additive production of three-dimensional objects, such as a system for selective laser sintering.
- the solids that are entrained by the process gas can therefore be solids that can be released into the process gas in such a device, in particular condensate particles and/or whirled-up build-up material formed from vaporized build-up material. These solids are using the Filter device at least partially separated from the process gas (raw gas) and then form the filter residue.
- the passivation device 1 comprises an outlet region 3 which can be coupled or is coupled to the filter device 10 . A situation is shown in FIG. 1 in which the outlet area 3 is coupled to the filter device 10 . The outlet area 3 is designed to receive filter residue from the filter device 10 .
- the passivation device 1 also includes a fluid supply 4 for supplying a fluid stream into the outlet area 3.
- the fluid stream consists of a fluid which includes a passivating agent.
- the fluid consists of a mixture of an inert fluid and the passivating agent, which is also fluid.
- it can be a mixture of an inert gas gas with which the filter residue reacts chemically for passivation.
- the chemical reaction is preferably an oxidation reaction, more preferably an oxidation reaction with oxygen.
- a mixture of oxygen and an inert gas such as argon or nitrogen
- the fluid can, for example, be taken from a fluid reservoir 90 that is provided, e.g.
- a fluid connection 91 is provided between the fluid supply 4 and the fluid reservoir 90 for this purpose.
- a compressed gas cylinder with an optional reducing valve is usually suitable for providing the fluid in the quantity and pressure required for a longer period of operation.
- a pressurized gas cylinder another container suitable for storing the fluid can be used as the fluid reservoir 90, with a device for increasing or decreasing the fluid pressure and/or a device for adjusting and/or regulating the fluid pressure being provided in addition to the container if necessary can.
- the fluid can be taken from a plurality of fluid reservoirs 90 .
- the inert fluid can be taken from a fluid reservoir and the passivating agent can be taken from another fluid reservoir, with the inert fluid and the passivating agent being mixed.
- oxygen is provided as the passivating agent, it can also be used in the form of air from the ambient atmosphere, optionally after compression and/or filtering.
- the ambient atmosphere is understood as a fluid reservoir for the passivating agent.
- a fluid reservoir it is also possible for a fluid reservoir to contain a mixture of an inert fluid and the passivating agent and for further passivating agents to be added from another fluid reservoir, at least if required.
- the amount of fluid that enters the outlet area 3 per unit of time can preferably be adjusted and/or regulated by a regulating device (not shown in FIG. 1).
- the direction of flow of the fluid flow through the fluid supply 4 is symbolized by the arrow 43 in FIG.
- the passivation device 1 optionally includes a passivating agent feed (not shown in FIG.
- the conveying line 5 is optionally thermally insulated, i.e. at least one section of the conveying line is optionally provided with an insulating device, for example an insulating jacket.
- the fluid discharge 5 includes a check valve, with which the fluid discharge 5 can be blocked for fluid passage.
- the fluid supply 4 includes a nozzle 41 through which the fluid flow enters the outlet area 3 . When the fluid stream flows through the nozzle 41 into the outlet area 3, the fluid is accelerated through the nozzle 41. As a result, a suction pressure is generated in the outlet area 3 , through which the filter residue and any fluid present in the filter device 10 are sucked in and thus sucked into the outlet area 3 .
- the filter residue sucked out of the filter device 10 and any residue from the filter device 10 are ejected from the outlet area 3 through the ejection area 51 .
- This embodiment of the outlet area 3 with such a nozzle 41, which generates an intake pressure, is often referred to as an "ejector".
- Alternative terms are, for example, “jet pump”, “propellant pump” and “jet pump”.
- Such a nozzle 41 of an ejector is often referred to as “ejector nozzle” or “driving nozzle”.
- 2 is a detailed view showing a specific example of the outlet area 3, the fluid supply 4 designed as a nozzle 41 and the ejection area 51 according to the first exemplary embodiment, which are components of the ejector, in a schematic sectional view.
- the passivation device 1 comprises an energy supply device 70 for applying energy to the fluid flow and/or the passivation agent and/or the filter residue.
- the energy supply device 70 is preferably a heating device. According to the first exemplary embodiment, the energy supply device 70 is designed and arranged to introduce energy into the region of the fluid supply. The positioning of the energy supply device 70 shown in FIG.
- the energy supply device 70 is preferably a heating device, in particular a continuous-flow heater, i.e. a heating device which heats the fluid stream as it flows through the heating device or the section of the line in which the heating device is fitted.
- the passivation device 1 includes a collector 80 which is in fluid communication with the outlet region 3 via the fluid discharge 5 if the fluid discharge does not have a check valve or an existing check valve is open.
- a collector 80 preferably has a filter 81 through which the fluid entering the collector 80 as a fluid flow can escape.
- the flow of the escaping fluid is symbolized by the arrow 82 in FIG.
- a filling level sensor 83 is preferably arranged in the area of such a collector 80, with which the filling level of the collector 80 can be monitored, in particular in order to determine the point in time at which the collector 80 must be emptied or replaced by an empty collector.
- the passivation device 1 is designed and/or controllable to bring about a chemical reaction between the filter residue and the passivation agent at least partially in the entrained flow. Firstly, this means that filter residue is sucked in by the ejector effect and conveyed together with the fluid flow in the entrained flow state. Secondly, this means that the passivation device provides a fluid stream which contains a suitable passivating agent and whose composition enables a chemical reaction. Furthermore, energy is applied by means of an energy supply device, as a result of which the reaction is started and/or accelerated, for example.
- the passivation device 1 comprises at least one sensor (not shown in FIG. 1) that detects a pressure and/or a temperature and/or a chemical composition.
- the at least one sensor can be arranged, for example, in such a way that it determines the properties of the fluid in the delivery line 5 .
- the at least one sensor can also be arranged in the outlet area 3 and/or in the fluid feed 4 and/or in the optional collector 80 .
- the temperature is preferably measured at least in the outlet area 3 or at the adjoining end of the conveyor line 5 and in the area of the end of the conveyor line 5 opposite the outlet area 3, for example around the entrained flow and the temperature conditions advantageous for passivation in the entire entrained flow area, i.e. in the delivery line 5.
- a sensor can be used, for example, to monitor whether the properties of the fluid flow that are suitable for the operation of the ejector and for the formation of an entrained flow are present.
- a sensor can also be used, for example, to monitor whether suitable conditions (e.g. in terms of passivating agent concentration, temperature and/or pressure). Controlled by signals emitted by such a sensor, for example, the temperature, the pressure and the amount of a passivating agent can be regulated in the region of the filter device in which a chemical reaction is desired.
- the delivery line 5 includes at least one cross-sectional constriction. This will be discussed in more detail in connection with the second exemplary embodiment. Second embodiment The passivation device 1 according to the second embodiment is shown in FIG. The components and properties of the passivation device 1 according to the second embodiment, which correspond to those of the passivation device 1 according to the first embodiment, will not be described separately below.
- the passivation device 1 of the first and second exemplary embodiment are also denoted by the same reference symbols. All those components and properties of the filter device 1 that are described as optional features for the first embodiment also represent optional features for the second embodiment.
- the passivation device 1 according to the second embodiment differs from the passivation device 1 according to the first embodiment in particular in Configuration of the outlet area and the fluid supply. According to the second exemplary embodiment, no ejector for sucking in the filter residue from the filter device 10 is provided.
- the gravity acting on the filter residue located in the filter device 10 means that this in the exit region 3' and is conveyed through the conveying line 5 by means of the fluid flow entering through the fluid supply 4' into the exit region 3'.
- the outlet area 3′ is designed, for example, as a chamber to which the fluid supply 4′ and the delivery line 5 are connected, so that the fluid flow can be guided through the chamber.
- the chamber can be connected or is connected directly or indirectly via a pipe, a line, etc. to an outlet opening through which the filter residue can escape from the filter device 10 .
- the delivery line 5 includes a cross-sectional constriction 511.
- the cross-sectional constriction 511 can be seen in the enlargement shown in the lower area of FIG.
- the cross-sectional constriction 511 is arranged at a distance from the outlet region 3' in FIG.
- the cross-sectional constriction 511 can also be arranged at a different point in the conveying line 5, for example closer to the outlet area 3', in particular at a position adjacent to the outlet area 3'.
- the delivery line 5 can also have several cross-sectional constrictions. The fluid flowing through the delivery line 5 is accelerated by the cross-sectional constriction 511 . As a result, particle agglomerates contained in the filter residue can break up, for example. This is symbolized in the enlargement shown in FIG.
- third exemplary embodiment The passivation device 1 according to the third exemplary embodiment is not shown in the drawing figures. Apart from the exit area, fluid supply and fluid discharge, the third exemplary embodiment corresponds to the first exemplary embodiment. The components and Properties of the passivation device 1 according to the third exemplary embodiment which correspond to those of the passivation device 1 according to the first exemplary embodiment are not described separately below. With regard to the similarities, reference is made to the above description of the first exemplary embodiment. The following description is limited to the differences.
- the outlet area, the fluid supply and the fluid discharge are in the form of a Venturi nozzle or as components a Venturi nozzle formed.
- the suction of filter residue from the filter device 10 thus takes place, unlike in the first exemplary embodiment, not by means of an ejector but by means of a Venturi nozzle.
- other devices are used instead of or in addition to an ejector or a venturi nozzle in order to cause filter residue to be sucked into the fluid flow.
- the passivation device 1 according to the various exemplary embodiments can thus have one energy supply device or multiple energy supply devices. Further exemplary embodiments of the passivation device 1 according to the invention result, for example, from the fact that instead of a passivating agent feed for feeding the passivating agent into the fluid feed 4, 4' or in addition to such a passivating agent feed, a passivating agent feed for feeding the passivating agent into the outlet area 3, 3' is provided.
- Further exemplary embodiments of the passivation device 1 according to the invention result, for example, from the fact that instead of a passivating agent feed for feeding the passivating agent into the fluid feed 4, 4′ and/or the outlet region 3, 3′ or in addition to such a passivating agent feed, a passivating agent feed for feeding the passivating agent into the fluid discharge 5 is provided. Further exemplary embodiments of the passivation device 1 according to the invention result, for example, from the fact that the at least one cross-sectional constriction 511 of the conveying line described specifically in connection with the second exemplary embodiment as an optional feature is implemented in the passivating device 1 of another exemplary embodiment.
- Embodiments of the filter system according to the invention include a passivation device 1 according to one of the embodiments described above and a filter device 10, wherein the Passivation device 1 coupled to the filter device or can be coupled.
- the filter system 100 according to a first group of exemplary embodiments is shown in FIGS. With regard to the passivation device 1 (area surrounded by a dashed line), reference is made to the above description of the individual exemplary embodiments.
- the passivation device 1, the filter device 10 and the filter system 100 as a whole are shown in FIGS. 1 and 3 as well as in FIGS. 4 to 9 in a possible operating position.
- the passivation device 1 is coupled to a filter device 10 and arranged in such a way that the passivation of filter residue is possible.
- the filter device 10 is arranged such that, on the one hand, a process gas (raw gas) can be filtered by means of the filter device 10 and thereby cleaned of solids carried along in the process gas, and on the other hand, filter residue can exit the filter device 10 and enter the passivation device 1.
- the filter system 100 includes a filter device 1.
- the filter device 1 includes a filter chamber 11 formed by a filter chamber wall 12, in which at least one filter element 20 is arranged. In FIGS. 1 and 3, six filter elements 20 arranged in the filter chamber 11 are shown as an example.
- the filter chamber 11 has a process gas inlet (not shown in Figures 1 and 3) and a process gas outlet (not shown in Figures 1 and 3), the process gas inlet, the process gas outlet and the at least one filter element 20 being arranged in such a way that a process gas , which enters the filter chamber 10 via the process gas inlet and leaves the filter chamber again via the process gas outlet, is filtered by means of the at least one filter element 20 .
- the process gas inlet and the process gas outlet can be openings in the filter chamber wall 12 to which corresponding process gas lines are connected. By filtering the process gas, the solids carried along by the process gas are at least partially separated by being held back by the at least one filter element 20 .
- the held back Solids remain at least initially on the at least one filter element 20 .
- the retained solids are also commonly referred to as "filter residue".
- An area inside the filter chamber 10, which is arranged below the at least one filter element 20, is designed to receive filter residue which is detached from or detaches from the at least one filter element. This means that this filter residue falls within this range in the simplest case.
- the area is preferably a collection area 13 in which a certain amount of filter residue can be collected before it enters the passivation device 1 .
- the detachment can take place, for example, through the action of gravity.
- an optional detachment device (not shown in FIGS. 1 and 3) can be provided.
- the detachment device can be designed, for example, to detach the filter residue adhering to the at least one filter element 20 by means of the action of gas. It is preferred to interrupt the filtering of the process gas from time to time and to direct a gas through the at least one filter element in the direction opposite to the direction of flow of the process gas during its filtering. In order to remove filter residue, the gas is preferably passed through the at least one filter element 20 in an intermittent manner.
- detachment is not limited to the procedure described above, but can also take place in other ways, for example by blowing off, sweeping, scraping off, shaking off, etc. A combination of several detachment techniques is also possible.
- the fluid supply 4, 4' of the passivation device 1 is connected to an external fluid source, so that fluid can be fed from outside the filter system 100 into the fluid supply 4, 4'.
- the fluid passing through the Fluid supply 4, 4′ is supplied to the outlet area 3, 3 can, for example, be taken from a provided fluid reservoir 90 (e.g. compressed gas reservoir in the form of a compressed gas bottle or the like), as already mentioned in connection with the above description of the passivation device.
- a fluid connection 91 is provided between the fluid supply 4 and the fluid reservoir 90 for this purpose.
- the lower area of the filter chamber or the collection area 13 preferably has a wall that tapers downwards and an outlet through which the filter residue can exit from the filter chamber 10 .
- a collection area 13 is shown in FIGS.
- a conveyor device 14 is provided in the collection area, which causes or supports the movement of the filter residue in the direction of the outlet, especially when the slope of the collection chamber wall is relatively flat, so that the filter residue may not reliably move by gravity in the direction of the outlet.
- the conveying device can, for example, comprise a fluidizing plate provided in the wall.
- the filter device 10 has a collection chamber 15 which is arranged between the filter chamber 11 and the passivation device 1 and in which the filter residue can be collected.
- the individual components of the system 100 are preferably designed and arranged in such a way that the passivation device and an optional collection chamber 15 are arranged at least partially below the filter chamber in a space-saving manner, as is shown in FIGS. Furthermore, the individual components of the system 100 are preferably designed and arranged in such a way that an optional collection device 80 and an optional collection chamber 15 are arranged at least partially below the filter chamber in a space-saving manner, as is shown in FIGS.
- the filter device 1 comprises at least one sensor that detects a pressure and/or a temperature and/or a chemical composition.
- FIGS. 1 and 3 are an example of an oxygen sensor 151, a Temperature sensor 152 and a pressure sensor 153 are shown, with which the oxygen concentration, the temperature and the pressure in the collection chamber 15 can be detected.
- These sensors 151, 152, 153 can be used, for example, to record measured values with which conclusions can be drawn about the risk of ignition of the filter residue in the collection area 15 and the possible need for countermeasures such as a supply of inert gas.
- such sensors can be arranged, for example, in such a way that they record measured values for the interior of the filter chamber 11 .
- the filter device 1 optionally includes at least one fill level sensor (not shown in FIGS.
- FIGS. 1 and FIGS. 2 Further exemplary embodiments of the filter system 100 according to the invention result, for example, from modifications to the exemplary embodiments described above.
- at least part of the fluid that is supplied to the outlet region 3, 3 through the fluid supply 4, 4' is removed from a point on the clean gas side of the process gas circuit.
- the fluid can be taken from a buffer store, which provides fluid for cleaning the at least one filter element 20 by means of a compressed gas blast.
- the fluid stored in the buffer store can, for example, already have the pressure required to operate the filter system, so that an additional compression device can be dispensed with.
- the filter system 100 according to the further exemplary embodiments is shown as an example in FIGS.
- the exemplary embodiments illustrated therein are modifications of the exemplary embodiments illustrated in FIGS.
- the filter system 100 includes a line 92 through which clean gas is removed from the filter chamber 11 and fed into the fluid supply 4, 4'.
- a fluid delivery device 93 is provided, which delivers the clean gas from the filter chamber 11 into the fluid supply 4, 4'.
- the fluid delivery device 93 can be a blower or a compressor, for example.
- a passivating agent feed 6 is shown in FIGS. 4 and 5, through which passivating agent (for example oxygen) is fed into the line 92 .
- the passivating agent feed 6 is connected, for example, to a passivating agent reservoir (not shown in FIGS. 4 and 5).
- the passivating agent can also be fed in at another point, for example in the area of the fluid feed 4, 4' of the outlet area 3, 3', the fluid discharge 5.
- Several passivating agent feeds can also be provided in order to feed passivating agent at different points.
- a passivating agent feed can also be dispensed with if the process gas already contains a passivating agent.
- the process gas contains oxygen, which leads to an effective oxidation of particles contained in the filter residue due to the supply of energy in the passivation device.
- the process gas could have an oxygen content of less than 1.3% by volume, for example. Oxygen levels in the low percentage range, tenths or less may be partially acceptable for the additive manufacturing process.
- the filter system 100 corresponds to the exemplary embodiments described above with the difference that it comprises at least two filter devices 10 .
- it includes a transport device 200, which transports the filter residue from the individual filter devices 10 into the passivation device 1, for example via lines 201.
- the transport device 200 is, for example, a suction device.
- Such a filter system 100 is shown in FIG. 6 as an example with two filter devices 10-1 and 10-2.
- the filter system 100 can also include more than two filter devices.
- the at least two filter devices are preferably assigned to different devices for the additive production of three-dimensional objects (e.g.
- the filter system 100 corresponds to the exemplary embodiments described above, it likewise comprising at least two filter devices 10 .
- the passivation device 1 is coupled directly or indirectly to at least one of the filter devices, as has already been described above.
- the filter system 100 includes a transport device 200, which transports the filter residue from the individual filter devices 10, which are not directly or indirectly coupled to the passivation device 1, into the passivation device 1, for example via lines 201.
- the transport device 200 is, for example, a suction device.
- Such a filter system 100 is shown in FIG. 7 as an example with two filter devices 10-1 and 10-2.
- the filter system 100 can also include more than two filter devices.
- the at least two filter devices are preferably assigned to different devices for the additive production of three-dimensional objects (e.g. different systems for selective laser melting or laser powderbed fusion).
- the filter system 100 corresponds to the exemplary embodiments described above, it likewise comprising at least two filter devices 10 .
- the passivation device 1 is coupled directly or indirectly to at least one of the filter devices, as has already been described above.
- the filter system includes 100 a transport device 200, which transports the filter residue from the individual filter devices 10, which are not directly or indirectly coupled to the passivation device 1, into the collection chamber or the filter chamber of at least one filter chamber 10, which is directly or indirectly coupled to the passivation device 1, for example via lines 201.
- the transport device 200 is, for example, a suction device.
- Such a filter system 100 is shown in FIG. 8 as an example with two filter devices 10-1 and 10-2.
- the filter system 100 can also include more than two filter devices.
- the at least two filter devices are preferably assigned to different devices for the additive manufacturing of three-dimensional objects (e.g. different systems for selective laser melting).
- a suction device that serves as a transport device 200 in the aforementioned sense can be implemented, for example, by arranging a blower at the outlet of a filter device or a line connected to the outlet of a filter device or the outlets of a plurality of filter devices.
- pneumatic conveying is possible, for example by means of an ejector instead of a blower.
- a filter residue conveyor is provided in the area of the outlet of the filter device 10, through which the filter residue reaches the outlet area 3, 3', in order to transport the filter residue into the outlet area 3, 3' to effect or to force.
- a filter residue conveyor can be particularly advantageous in the exemplary embodiments in which no suction pressure or no high suction pressure is generated by the conveyor device.
- a laser sintering system with a process chamber and a process gas conveying device can be equipped with the filter system 100 according to the invention according to one of the above exemplary embodiments, so that the filter device 10 and the passivation device 1 represent part of the device for additive manufacturing of three-dimensional objects.
- the device shown as an example in FIG. 9 is a laser sintering or laser melting device 101.
- To build up an object 102 it contains a process chamber 103 with a chamber wall 104 .
- a working plane 107 is defined by the upper opening of the container 105 , with the area of the working plane 107 lying within the opening, which can be used to construct the object 102 , being referred to as the construction field 108 .
- a carrier 110 Arranged in the container 105 is a carrier 110 that can be moved in a vertical direction V and to which a base plate 111 is attached, which closes off the container 105 at the bottom and thus forms its bottom.
- the base plate 111 may be a plate formed separately from the bracket 110 and fixed to the bracket 110 or may be formed integrally with the bracket 110 .
- a construction platform 112 can also be attached to the base plate 111 as a construction base, on which the object 102 is built. However, the object 102 can also be built on the base plate 111 itself, which then serves as a building base.
- the laser sintering device 101 also contains a storage container 114 for an electromagnetic Radiation-solidifiable powdered construction material 115 and a coater 116 movable in a horizontal direction H for applying the construction material 115 within the construction field 108.
- the coater 116 preferably extends transversely to its direction of movement over the entire area to be coated.
- a radiant heater 117 is optionally arranged in the process chamber 103 and is used to heat the build-up material 115 applied.
- An infrared radiator for example, can be provided as the radiant heater 117 .
- the laser sintering device 101 also contains an exposure device 120 with a laser 121, which generates a laser beam 122, which is deflected via a deflection device 123 and through a focusing device 124 via a coupling window 125, which is attached to the upper side of the process chamber 103 in the chamber wall 104 the working plane 107 is focused. Furthermore, the laser sintering device 101 contains a control unit 129, via which the individual components of the device 101 are controlled in a coordinated manner for carrying out the construction process. Alternatively, the control unit can also be fitted partially or entirely outside the device. The control unit may include a CPU whose operation is controlled by a computer program (software).
- the computer program can be stored separately from the device on a storage medium from which it can be loaded into the device, in particular into the control unit.
- the carrier 110 is first lowered by a height which corresponds to the desired layer thickness.
- the coater 116 first travels to the storage container 114 and takes from it a quantity of the building material 115 sufficient for applying a layer. Then it drives over the construction field 108, applies powdered construction material 115 there to the construction base or a previously existing powder layer and pulls it out to form a powder layer.
- the application takes place at least over the entire cross section of the object 102 to be produced, preferably over the entire construction field 108, ie the area delimited by the container wall 106.
- the powdered construction material 115 is heated to a working temperature by means of a radiant heater 117 .
- the cross section of the object to be produced 102 is scanned by the laser beam 122, so that the powdered construction material 115 at the Places is solidified that correspond to the cross section of the object 102 to be manufactured.
- the powder grains are partially or completely melted at these points by means of the energy introduced by the radiation, so that after cooling they are connected to one another as solid bodies.
- the process gas conveying device 136 which is a blower, for example, serves to convey a process gas flowing through the process chamber 103 from a process chamber inlet 132 to a process chamber outlet 134 .
- the flow of the process gas through the process chamber 103 is shown schematically in FIG.
- the process gas is preferably at least partially circulated, which means that at least part of the process gas flowing through the process chamber outlet 134 is returned to the process chamber 103 through the process chamber inlet 132 after it has been filtered by the filter device 10 of the filter system 100.
- Such a process gas circuit is shown in FIG. 9, the direction of flow being symbolized by arrows.
- the process chamber 103 is connected to the filter system 100 in such a way that process gas exiting the process chamber 103 through the process chamber outlet 134 is routed into a process gas inlet 100 - 1 of the filter device 10 .
- a line 135 is provided for this purpose, for example. If the process gas is circulated, a process gas outlet 100 - 2 of the filter device 10 is also connected to the process chamber inlet 132 .
- a line 135 is provided for this purpose, for example.
- a process gas conveying device 136 can be provided, for example, between the process gas outlet 100-2 and the process chamber inlet 132 and/or between the process chamber outlet 134 and the process gas inlet 100-1.
- the process gas delivery device 136 is preferably located between the process gas outlet 100 - 2 of the filter device 10 and the process chamber inlet 132 arranged because the process gas delivery device 136 promotes clean gas in this case, which reduces the risk of contamination of the process gas delivery device 136.
- This arrangement of the process gas delivery device 136 is shown in FIG. 9 .
- the process chamber 103 and filter chamber 11 can be connected to one another in such a way that the process chamber outlet 134 is directly connected to the process gas inlet 100-1 of the filter device 10 and/or that the process chamber inlet 132 is directly connected to the process gas outlet 100-2 of the filter device 10 is connected.
- Process gas is also commonly referred to as “raw gas” before filtering, while process gas is also commonly referred to as “clean gas” after filtering. This means that raw gas flows during operation from the process chamber outlet 134 into the process gas inlet 100-1 of the filter device.
- process gas is also commonly referred to as “clean gas” after filtering.
- the exemplary embodiments of the device for additive manufacturing have been described using a selective laser sintering or laser melting device, they are not restricted to selective laser sintering or laser melting. It can be applied to any method for generatively producing a three-dimensional object by applying and selectively solidifying a building material in layers.
- the imagesetter can, for example, include one or more gas or solid-state lasers or any other type of laser such as laser diodes, in particular VCSEL (Vertical Cavity Surface Emitting Laser) or VECSEL (Vertical External Cavity Surface Emitting Laser), or a line of these lasers.
- laser diodes in particular VCSEL (Vertical Cavity Surface Emitting Laser) or VECSEL (Vertical External Cavity Surface Emitting Laser), or a line of these lasers.
- any device with which energy can be selectively applied to a layer of the building material as wave or particle radiation can be used as an exposure device.
- a laser another light source, an electron beam or any other energy or radiation source that is suitable for solidifying the building material can be used, for example.
- deflecting a beam exposure with a movable line exposer can also be used.
- the invention can be used.
- Various types of powder can be used as the building material, in particular metal powder, plastic powder, ceramic powder, sand, filled or mixed powders.
- the method for passivation according to the invention (hereinafter also referred to as “passivation method”) is carried out, for example.
- Filter residue exiting a filter device 10 is fed to an exit area 3, 3' (step A). This is preferably done by sucking it out of the filter device, for example by means of an ejector.
- a fluid stream is fed into the outlet area 3, 3' (step B). As a result, the fluid flow is loaded with the filter residue.
- the fluid flow picks up the filter residue and transports it in the direction of flow.
- the fluid flow entrains the filter residue with it.
- the fluid stream loaded with the filter residue is discharged from the outlet area 3, 3' (step C).
- the feeding of the filter residue into the outlet area 3, 3 'and the loading of the fluid flow with the filter residue is preferably carried out in that the Filter residue sucked off as a result of the fluid flow and is thereby included in the fluid flow.
- the feeding of the filter residue into the outlet area 3, 3', the loading of the fluid flow with the filter residue and the discharge from the outlet area 3, 3' are preferably carried out by using an ejector.
- the fluid flow is first fed into the ejector as a driving medium.
- Step D The fluid stream loaded with the filter residue is subsequently ejected from the ejector.
- the fluid stream is energized as part of the passivation process (Step D). Energizing can take place: (a) upstream of the exit area, i.e. before the fluid flow is fed into the exit area 3,3', for example in the fluid feed 4, 4', (b) at the point where the fluid flow enters the exit area 3,3', i.e.
- step D can occur anywhere before, after, and during the sequence of steps A through C.
- step A a fluid stream composed of a fluid that includes a passivating agent is used as the fluid stream.
- the passivating agent is added to the fluid in a further step (step E), i.e. the fluid flow is mixed with the passivating agent.
- the fluid contains passivating agent from the outset, but further passivating agent is added to it in the course of the passivation process.
- Step E can - if it is carried out - take place: (i) upstream of the outlet area, i.e.
- the passivating agent before the fluid flow is fed into the outlet area 3,3', for example by feeding the passivating agent into the fluid feed 4, 4', (ii) at Place where the fluid flow enters the exit area 3,3', i.e. during the feeding of the fluid flow into the exit area 3,3', (iii) in the exit area 3,3', e.g. by feeding the passivating agent into the exit area 3,3 ', (iv) at the point where the fluid flow exits the exit area 3,3', i.e. during the discharge of the fluid flow from the exit area 3,3', (v) downstream of the exit area, i.e. after the fluid flow has been discharged from the Outlet area 3,3', for example by feeding the passivating agent into the conveying line 5.
- the fluid can also be mixed with the passivating agent simultaneously or at different times or at several points n, i.e. any combination of the above options (i) to (v) is possible.
- the filter residue is at least partially passivated in the entrained flow by a chemical reaction with the passivating agent (step F). "Partial passivation" is used when only part of the particles in the filter residue react chemically with the passivating agent and/or when only part of the material of the particles which is passivated and which is basically reactive to the passivating agent is chemically converted.
- An oxidizing agent that is suitable for at least partially oxidizing the filter residue is preferably used as a passivating agent, more preferably included the passivating agent is oxygen, more preferably the passivating agent is oxygen.
- the fluid forming the fluid stream is an inert gas, for example nitrogen and/or argon, containing O 2 contains or with O 2 is transferred.
- the mixing can be done, for example, by adding pure oxygen gas or a mixture containing oxygen gas (e.g. air).
- the amount of O is preferred 2 , with which the fluid stream is added, adjustable and/or at least 0.01% by volume, and/or at most 20.8% by volume.
- An exemplary embodiment of the method is shown graphically in FIG.
- the fluid flow is displaced (step E) before the fluid flow is fed into the outlet region 3, 3' (step B).
- energy is applied after the fluid stream mixed with the filter residue has left the outlet region 3, 3'.
- the chemical reaction for passivation is initiated by the application of energy.
- Steps A, B, C are shown as steps carried out one after the other, because they can have this sequence for a specific quantity of filter residue and the part of the fluid flow that transports this filter residue.
- the passivation process is preferably carried out continuously, so that at least over a certain period of time fluid is continuously fed into the outlet area 3,3' and removed from it, and during which filter residue is fed into the fluid flow.
- the energy is supplied exclusively or predominantly to either the fluid or the filter residue by means of the energy supply device, it will happen after the supply or after the encounter of fluid and filter residue to an equilibration of the energy, which takes place very quickly, for example in the range of less than a second or in the range of at most a few milliseconds, particularly in the case of small filter residue particles.
- This can be the case, for example, when the fluid stream is first charged with energy before it reaches the outlet area and thus before it comes into contact with the filter residue.
- the speed of the equilibration depends, among other things, on the flow speed of the fluid stream, its temperature and the particle diameter.
- an ejector as described above for the first embodiment, is supplied with argon via the fluid supply in the form of a delivery line with a circular cross-section and an internal diameter of 4 mm at a pressure of 2 bar in front of the ejector (ejector -admission pressure), a temperature of 250 °C and a flow rate of 3.8 L/s. Particles with different particle diameters get into the fluid flow in the ejector.
- Equation 1 The first term of the sum on the right side of Equation 1 describes the particle temperature change based on convection and conduction.
- the second term describes the particle temperature change based on thermal radiation.
- Fig. 11 A diagram is shown in Fig. 11, which shows the course of T p as a function of time t for different particle diameters dp. The time for which the particles are in contact with the fluid before they leave the conveying line 5 again can be relatively short in some cases.
- the fluid flow can be set and/or controlled in such a way that particle agglomerates occurring in the filter residue are at least partially broken up.
- This effect can be achieved, for example, as an additional effect of using an ejector or a Venturi nozzle to suck in the filter residue from the filter device 10, since there is a strong flow in an ejector or a Venturi nozzle and often also downstream of it, which often breaking up of agglomerates.
- the fluid flow loaded with the filter residue can alternatively or additionally be guided through a cross-sectional constriction 511 of the fluid line 5 .
- the optional breaking up takes place in particular in such a way that the particles of the filter residue are either in the form of primary particles or in the form of smaller agglomerates after the breaking up.
- comminution to a secondary particle diameter of 100 ⁇ m or less are considered advantageous for the most effective heating possible.
- the value can also be higher, for example 200 ⁇ m.
- Equations (1) to (4) above can be used, for example, to estimate whether particles of different diameters are heated up quickly enough.
- the required length of the conveying line can be estimated. According to this estimate, for example, to heat up particles with a diameter of 100 ⁇ m from room temperature to at least approximately 250° C., a time of around 250 ms is required. If the particles are then given 100 ms for the chemical reaction at the temperature reached, the desired residence time in the conveying line is 350 ms. If the average flow velocity is 10 m/s, a length of the conveying line of 3.5 m can be estimated.
- the method according to the invention for filtering a process gas (hereinafter also referred to as “filter method”) is carried out, for example.
- At least one filter element can optionally be coated with a filter aid (optional step I).
- a process gas is passed through at least one filter element 20 arranged in a filter chamber 11 of the filter device 10, the process gas being filtered, i.e. being at least partially cleaned of entrained solids (step II).
- the process gas is admitted into the filter chamber 11 via a process gas inlet and the filter chamber is discharged again via a process gas outlet, taking its way via the at least one filter element 20 or, in the case of several filter elements, via at least one of them.
- the process gas can in particular be the process gas of a device for the additive production of three-dimensional objects such as a system for selective laser sintering/melting.
- the solids that have been filtered out remain at least initially on the at least one filter element 20 .
- the retained solids are also commonly referred to as "filter residue".
- the filter element is cleaned, or in the case of several filter elements, at least part of it is cleaned (step III).
- the filter residue either detaches itself from the at least one filter element 20 and the at least one filter element is cleaned as a result. Or the filter residue is removed by a suitable measure and the at least one filter element is cleaned in this way.
- a blast of compressed gas can be passed through the at least one filter element 20 from time to time, the direction of flow of which is opposite to the direction in which the process gas flows through the at least one filter element for filtering.
- the detachment can also be carried out by blowing off, sweeping away, scraping off, shaking off etc.
- a combination of several techniques for detachment is also possible.
- the filtering of the process gas is optionally interrupted while the filter residue is being removed.
- filtering of the process gas can be continued if the stripping technique used allows.
- Another possibility is that several filter elements 20 are provided and the filtering of the process gas is continued with some of the filter elements 20 while another part is cleaned.
- step IV The filter residue which has become detached from at least one filter element or which has been detached from this is optionally collected. This can be done, for example, by means of a collection chamber into which the filter residue is introduced and in which it remains until it is subjected to the passivation process.
- the filter residue is subjected to the passivation process according to the invention (step V).
- An exemplary embodiment of the filtering method is shown graphically in FIG. 12, with step D corresponding to the implementation of the passivation method as shown in FIG.
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- Chemical Kinetics & Catalysis (AREA)
- Life Sciences & Earth Sciences (AREA)
- Sustainable Development (AREA)
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Abstract
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Priority Applications (2)
Application Number | Priority Date | Filing Date | Title |
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CN202280058392.XA CN117916005A (zh) | 2021-07-27 | 2022-05-31 | 钝化装置、过滤系统、用于三维物体的增材制造的装置、用于钝化的方法和用于过滤的方法 |
EP22732075.1A EP4376980A1 (de) | 2021-07-27 | 2022-05-31 | Passivierungsvorrichtung, filtersystem, vorrichtung zur additiven herstellung dreidimensionaler objekte, verfahren zum passivieren und verfahren zum filtern |
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DE102021208113.4 | 2021-07-27 | ||
DE102021208113.4A DE102021208113A1 (de) | 2021-07-27 | 2021-07-27 | Passivierungsvorrichtung, Filtersystem, Vorrichtung zur additiven Herstellung dreidimensionaler Objekte, Verfahren zum Passivieren und Verfahren zum Filtern |
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CN (1) | CN117916005A (de) |
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DE102022211877A1 (de) | 2022-11-09 | 2024-05-16 | Eos Gmbh Electro Optical Systems | Verfahren und Vorrichtung zur Passivierung von in einer Filtervorrichtung auftretenden Filterrückständen |
Citations (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP1527807A1 (de) | 2003-10-28 | 2005-05-04 | Handte Umwelttechnik GmbH | Vorrichtung und Verfahren zum Abscheiden von Staubbestandteilen aus einem explosionsfähigen Staub-Luft-Gemisch |
US20050147548A1 (en) * | 2004-01-05 | 2005-07-07 | Shiban Samir S. | Combined chemical agent and dynamic oxidation treatment of hazardous gas |
US20140287080A1 (en) | 2008-09-05 | 2014-09-25 | Mtt Technologies Limited | Filter assembly |
DE102014207160A1 (de) | 2014-04-15 | 2015-10-15 | Eos Gmbh Electro Optical Systems | Umluftfiltervorrichtung für eine Vorrichtung zum schichtweisen Herstellen eines dreidimensionalen Objekts |
DE102017207415A1 (de) | 2017-05-03 | 2018-11-08 | Ult Ag | Vorrichtung zur Separation und Behandlung metallischer Partikel |
EP2978589B1 (de) | 2013-03-28 | 2019-06-19 | EOS GmbH Electro Optical Systems | Verfahren und vorrichtung zum herstellen eines dreidimensionalen objekts |
WO2020120623A1 (de) * | 2018-12-12 | 2020-06-18 | Eos Gmbh Electro Optical Systems | Verfahren und vorrichtung zur nachbehandlung von in einem prozessgas mitgeführten partikeln sowie filter hierfür |
DE102020102034A1 (de) * | 2019-11-13 | 2021-05-20 | Herding Gmbh Filtertechnik | Verfahren zur Trockenfiltration eines Fremdkörper mitführenden Gasstroms, Verwendung eines anorganischen Materials auf Basis von Siliziumdioxid als Filtrationshilfsstoff, und Filtervorrichtung zur Reinigung von Fremdkörper mitführendem Rohgas |
-
2021
- 2021-07-27 DE DE102021208113.4A patent/DE102021208113A1/de active Pending
-
2022
- 2022-05-31 EP EP22732075.1A patent/EP4376980A1/de active Pending
- 2022-05-31 CN CN202280058392.XA patent/CN117916005A/zh active Pending
- 2022-05-31 WO PCT/EP2022/064732 patent/WO2023006277A1/de active Application Filing
Patent Citations (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP1527807A1 (de) | 2003-10-28 | 2005-05-04 | Handte Umwelttechnik GmbH | Vorrichtung und Verfahren zum Abscheiden von Staubbestandteilen aus einem explosionsfähigen Staub-Luft-Gemisch |
US20050147548A1 (en) * | 2004-01-05 | 2005-07-07 | Shiban Samir S. | Combined chemical agent and dynamic oxidation treatment of hazardous gas |
US20140287080A1 (en) | 2008-09-05 | 2014-09-25 | Mtt Technologies Limited | Filter assembly |
EP2978589B1 (de) | 2013-03-28 | 2019-06-19 | EOS GmbH Electro Optical Systems | Verfahren und vorrichtung zum herstellen eines dreidimensionalen objekts |
DE102014207160A1 (de) | 2014-04-15 | 2015-10-15 | Eos Gmbh Electro Optical Systems | Umluftfiltervorrichtung für eine Vorrichtung zum schichtweisen Herstellen eines dreidimensionalen Objekts |
DE102017207415A1 (de) | 2017-05-03 | 2018-11-08 | Ult Ag | Vorrichtung zur Separation und Behandlung metallischer Partikel |
WO2020120623A1 (de) * | 2018-12-12 | 2020-06-18 | Eos Gmbh Electro Optical Systems | Verfahren und vorrichtung zur nachbehandlung von in einem prozessgas mitgeführten partikeln sowie filter hierfür |
DE102020102034A1 (de) * | 2019-11-13 | 2021-05-20 | Herding Gmbh Filtertechnik | Verfahren zur Trockenfiltration eines Fremdkörper mitführenden Gasstroms, Verwendung eines anorganischen Materials auf Basis von Siliziumdioxid als Filtrationshilfsstoff, und Filtervorrichtung zur Reinigung von Fremdkörper mitführendem Rohgas |
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DE102021208113A1 (de) | 2023-02-02 |
EP4376980A1 (de) | 2024-06-05 |
CN117916005A (zh) | 2024-04-19 |
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