EP1658150A1 - Dispositif pour atomiser un jet de matiere fondue et procede pour atomiser des metaux ou des ceramiques refractaires - Google Patents
Dispositif pour atomiser un jet de matiere fondue et procede pour atomiser des metaux ou des ceramiques refractairesInfo
- Publication number
- EP1658150A1 EP1658150A1 EP04764728A EP04764728A EP1658150A1 EP 1658150 A1 EP1658150 A1 EP 1658150A1 EP 04764728 A EP04764728 A EP 04764728A EP 04764728 A EP04764728 A EP 04764728A EP 1658150 A1 EP1658150 A1 EP 1658150A1
- Authority
- EP
- European Patent Office
- Prior art keywords
- melt
- nozzle
- gas flow
- lavalduse
- melt nozzle
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Withdrawn
Links
- 239000000155 melt Substances 0.000 title claims abstract description 110
- 238000000034 method Methods 0.000 title claims abstract description 18
- 229910052751 metal Inorganic materials 0.000 title claims abstract description 15
- 239000002184 metal Substances 0.000 title claims abstract description 15
- 239000000919 ceramic Substances 0.000 title claims abstract description 9
- 150000002739 metals Chemical class 0.000 title abstract description 8
- 239000000843 powder Substances 0.000 claims abstract description 12
- 210000002445 nipple Anatomy 0.000 claims description 31
- 238000000889 atomisation Methods 0.000 claims description 14
- 238000005507 spraying Methods 0.000 claims description 13
- 238000009413 insulation Methods 0.000 claims description 9
- 238000010438 heat treatment Methods 0.000 claims description 8
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 4
- 229910002804 graphite Inorganic materials 0.000 claims description 4
- 239000010439 graphite Substances 0.000 claims description 4
- 230000008569 process Effects 0.000 claims description 4
- 230000006835 compression Effects 0.000 claims description 2
- 238000007906 compression Methods 0.000 claims description 2
- 230000000171 quenching effect Effects 0.000 claims description 2
- 239000011214 refractory ceramic Substances 0.000 claims description 2
- 239000003870 refractory metal Substances 0.000 claims description 2
- 238000010292 electrical insulation Methods 0.000 claims 1
- 238000010791 quenching Methods 0.000 claims 1
- 239000012774 insulation material Substances 0.000 abstract description 2
- 239000007789 gas Substances 0.000 description 46
- 239000002245 particle Substances 0.000 description 11
- 238000009826 distribution Methods 0.000 description 5
- 230000000694 effects Effects 0.000 description 5
- 239000000463 material Substances 0.000 description 5
- 230000005855 radiation Effects 0.000 description 5
- 230000009172 bursting Effects 0.000 description 4
- 230000017525 heat dissipation Effects 0.000 description 4
- 239000002775 capsule Substances 0.000 description 3
- 239000007788 liquid Substances 0.000 description 3
- 238000004519 manufacturing process Methods 0.000 description 3
- 238000002844 melting Methods 0.000 description 3
- XKRFYHLGVUSROY-UHFFFAOYSA-N Argon Chemical compound [Ar] XKRFYHLGVUSROY-UHFFFAOYSA-N 0.000 description 2
- 229910000881 Cu alloy Inorganic materials 0.000 description 2
- 230000008901 benefit Effects 0.000 description 2
- 239000000498 cooling water Substances 0.000 description 2
- 239000000835 fiber Substances 0.000 description 2
- 230000008014 freezing Effects 0.000 description 2
- 238000007710 freezing Methods 0.000 description 2
- 239000011810 insulating material Substances 0.000 description 2
- 230000001788 irregular Effects 0.000 description 2
- 230000008018 melting Effects 0.000 description 2
- BASFCYQUMIYNBI-UHFFFAOYSA-N platinum Chemical compound [Pt] BASFCYQUMIYNBI-UHFFFAOYSA-N 0.000 description 2
- 229910000679 solder Inorganic materials 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- 229910000838 Al alloy Inorganic materials 0.000 description 1
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 1
- 229910001369 Brass Inorganic materials 0.000 description 1
- 229910016347 CuSn Inorganic materials 0.000 description 1
- 229910000640 Fe alloy Inorganic materials 0.000 description 1
- 238000003723 Smelting Methods 0.000 description 1
- 229910000831 Steel Inorganic materials 0.000 description 1
- NEIHULKJZQTQKJ-UHFFFAOYSA-N [Cu].[Ag] Chemical compound [Cu].[Ag] NEIHULKJZQTQKJ-UHFFFAOYSA-N 0.000 description 1
- 230000001133 acceleration Effects 0.000 description 1
- 229910045601 alloy Inorganic materials 0.000 description 1
- 239000000956 alloy Substances 0.000 description 1
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 1
- 229910052786 argon Inorganic materials 0.000 description 1
- 239000011324 bead Substances 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 210000000988 bone and bone Anatomy 0.000 description 1
- 239000010951 brass Substances 0.000 description 1
- 238000010924 continuous production Methods 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- KUNSUQLRTQLHQQ-UHFFFAOYSA-N copper tin Chemical class [Cu].[Sn] KUNSUQLRTQLHQQ-UHFFFAOYSA-N 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 230000018109 developmental process Effects 0.000 description 1
- 239000010419 fine particle Substances 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 230000001939 inductive effect Effects 0.000 description 1
- 230000007246 mechanism Effects 0.000 description 1
- 239000002923 metal particle Substances 0.000 description 1
- TWNQGVIAIRXVLR-UHFFFAOYSA-N oxo(oxoalumanyloxy)alumane Chemical compound O=[Al]O[Al]=O TWNQGVIAIRXVLR-UHFFFAOYSA-N 0.000 description 1
- 239000011049 pearl Substances 0.000 description 1
- JTJMJGYZQZDUJJ-UHFFFAOYSA-N phencyclidine Chemical class C1CCCCN1C1(C=2C=CC=CC=2)CCCCC1 JTJMJGYZQZDUJJ-UHFFFAOYSA-N 0.000 description 1
- 229910052697 platinum Inorganic materials 0.000 description 1
- 230000002028 premature Effects 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 230000001681 protective effect Effects 0.000 description 1
- 230000001105 regulatory effect Effects 0.000 description 1
- 230000003716 rejuvenation Effects 0.000 description 1
- 230000000630 rising effect Effects 0.000 description 1
- 238000007711 solidification Methods 0.000 description 1
- 230000008023 solidification Effects 0.000 description 1
- 238000001228 spectrum Methods 0.000 description 1
- 239000012798 spherical particle Substances 0.000 description 1
- 239000010935 stainless steel Substances 0.000 description 1
- 229910001220 stainless steel Inorganic materials 0.000 description 1
- 239000010959 steel Substances 0.000 description 1
- 230000008719 thickening Effects 0.000 description 1
Classifications
-
- 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
- B22F9/00—Making metallic powder or suspensions thereof
- B22F9/02—Making metallic powder or suspensions thereof using physical processes
- B22F9/06—Making metallic powder or suspensions thereof using physical processes starting from liquid material
- B22F9/08—Making metallic powder or suspensions thereof using physical processes starting from liquid material by casting, e.g. through sieves or in water, by atomising or spraying
- B22F9/082—Making metallic powder or suspensions thereof using physical processes starting from liquid material by casting, e.g. through sieves or in water, by atomising or spraying atomising using a fluid
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2/00—Processes or devices for granulating materials, e.g. fertilisers in general; Rendering particulate materials free flowing in general, e.g. making them hydrophobic
- B01J2/02—Processes or devices for granulating materials, e.g. fertilisers in general; Rendering particulate materials free flowing in general, e.g. making them hydrophobic by dividing the liquid material into drops, e.g. by spraying, and solidifying the drops
- B01J2/04—Processes or devices for granulating materials, e.g. fertilisers in general; Rendering particulate materials free flowing in general, e.g. making them hydrophobic by dividing the liquid material into drops, e.g. by spraying, and solidifying the drops in a gaseous medium
-
- 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
- B22F9/00—Making metallic powder or suspensions thereof
- B22F9/02—Making metallic powder or suspensions thereof using physical processes
- B22F9/06—Making metallic powder or suspensions thereof using physical processes starting from liquid material
- B22F9/08—Making metallic powder or suspensions thereof using physical processes starting from liquid material by casting, e.g. through sieves or in water, by atomising or spraying
- B22F9/082—Making metallic powder or suspensions thereof using physical processes starting from liquid material by casting, e.g. through sieves or in water, by atomising or spraying atomising using a fluid
- B22F2009/088—Fluid nozzles, e.g. angle, distance
Definitions
- the invention relates to a device for spraying a melt jet according to the preamble of the main claim and a method for spraying refractory metals and ceramics.
- the melt monofilament is clearly over 10 mm, depending on the discharge cross-section, also over 25 mm in length before it bursts open.
- the risk of freezing the monofilament over this length is not great there because of the relatively small temperature difference between the melt jet and the gas flow, in particular the heat loss due to radiation is proportional to T 4 and measures of the present invention were not considered.
- the atomization of a film results in a broader distribution of the particle sizes and these are coarser for a material under otherwise identical conditions than is possible with omnidirectional (monofilament) atomization according to the present method.
- the throughput in film atomization can, however, be much larger because the slot cross section can be larger and the gas forces laterally attack a thin melt stream.
- Fig. 1 shows a section through the atomizing device according to the invention
- FIGS. 2a and 2b mutually perpendicular section through the lower region of a device for jetting with a slot-shaped melt nozzle.
- a gas flow flows according to the arrows 7 from the side to the narrowest cross section 8, where it accelerates to the speed of sound when the critical pressure ratio is reached or exceeded.
- the gas flow can be "cold", ie it can be ambient temperature or the temperature from it Compression and need not be heated up.
- a separating flange 18 which separates the atomization chamber 19 below, in which the powder is collected and transported further in the narrowest area 8 of the Lavalduse 6 after the melt monofilament has burst open, and is transported further from the pressure chamber 20 located above. Because of the high temperatures, both the Lavalduse 6 and the housing of the container forming the atomizing chamber 19 are cooled, e.g. by being double-walled for the flow of cooling water.
- the gas is supplied from the outside, and the melt is heated by an inductive heating in coil form around the crucible 1, expediently insulated against the crucible 1, cooling water flowing through the coil.
- Resistance heaters are also used, but less so.
- the design of rooms 20 and 19 in Fig. 1 is similar to that in DE 33 11 343, only in the room 20 above the separating flange 18 is a pressure vessel for pressures of 20, 30 bar overpressure and more, in the atomization chamber 19 below a vessel for pressures slightly above atmospheric pressure in order to be able to overcome the following separating devices such as cyclones, classifiers and filters.
- the room 19 can also as
- Pressure vessel are executed. This has advantages with the production of very fine powders, in which the average density in the atomization area of the narrowest cross section 8 is greater than if the pressure is relaxed to about atmospheric pressure.
- the insulating piece 21 comprises, in the area of the lower wedge-shaped melt nipple 24, a screen 29 made of the best possible heat-insulating material, but which withstands the temperature, to reduce the heat dissipation on both sides of the lower wedge-shaped melt nipple 24. For further heat insulation there is between the screen 29 and the melt nipple 24 An air gap 30 is provided in the lower region.
- the melt nipple 24 has a flow channel 31 which merges into a slot-shaped space 32 (see FIG. 2 b) which is arcuate in cross section and has a slot length and corresponding slot-shaped outlet opening 26.
- the melt flow channel 31 can already be oval in preparation for the later expansion to the slot, as shown in FIG. 2b at 33.
- the heat-insulating screen 29 is brought close to the slot-shaped outlet opening 26 and only a small part of the melt nipple 24 is released around it.
- the lower wedge-shaped end 25 of the melt nipple 24 with the slit-shaped outlet opening 26 is above the likewise slit-shaped Lavalduse 27, which opens into an atomization chamber (not shown) with the pressure p 3 .
- the upper part of the melt nipple 24, not shown here in more detail, is insulated against heat dissipation by, for example, rotationally symmetrical parts and, as shown in FIG. 1, can additionally be actively supported by heating.
- the melt is fed to the flow channel 31 for spraying and the melt film emerging from the slot-shaped outlet opening is accelerated by the gas flow, which flows laterally into the capsule 34 along the arrows and accelerates on the way to the narrowest cross section 28 of the Lavalduse 27. Just below the Lavalduse, the film breaks up as described above.
- Stainless steel of the type X2CrNiMo 17-12-2 corresponding to 316L was atomized from a crucible 1 and the nipple 2 with a discharge diameter of 1.5 mm, both made of aluminum oxide, at a melt temperature of 1680 ° C.
- the diameter of the Lavalduse 6 was 4 mm.
- a brass melt with a temperature of 950 ° C. was atomized from a device according to FIG. 1 with nitrogen (N 2 ) of 2 barg, and water was blown in laterally through 2 bores of 1.5 mm in diameter directly below the narrowest cross section 8.
- the melt throughput was 1.3 kg / min, the amount of water sprayed in to cool the metal particles as quickly as possible, without round particles being produced by the surface tension, was about 1.5 kg / min.
- the particles had a strongly irregular shape from ellipsoids to bone and root-shaped, but finer round particles also resulted.
- the size distribution showed approximately
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Manufacture Of Metal Powder And Suspensions Thereof (AREA)
Abstract
L'invention concerne un dispositif et un procédé pour atomiser un jet de matière fondue, notamment des métaux ou des céramiques réfractaires, et les transformer en poudre. Le jet de matière fondue, qui se présente sous forme de monofil ou de film, sort d'une buse alimentée en matière fondue et dotée d'un orifice de sortie dans la zone d'une tuyère de Laval. Ce jet de matière fondue est accompagné d'un flux gazeux de préférence «froid» que la tuyère de Laval accélère jusque dans le domaine de vitesse supersonique, un éclatement se produisant derrière la tuyère de Laval. La buse alimentée en matière fondue est entourée d'une isolation thermique qui s'étend jusque dans la zone de la tuyère de Laval et ne laisse libre pratiquement que l'orifice de sortie de ladite buse, de sorte que le jet de matière fondue est protégé du flux gazeux à sa sortie.
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| DE2003140606 DE10340606B4 (de) | 2003-08-29 | 2003-08-29 | Vorrichtung zum Verdüsen eines Schmelzestrahls und Verfahren zum Verdüsen von hochschmelzenden Metallen und Keramikschmelzen |
| PCT/EP2004/009769 WO2005023465A1 (fr) | 2003-08-29 | 2004-08-27 | Dispositif pour atomiser un jet de matiere fondue et procede pour atomiser des metaux ou des ceramiques refractaires |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| EP1658150A1 true EP1658150A1 (fr) | 2006-05-24 |
Family
ID=34223306
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| EP04764728A Withdrawn EP1658150A1 (fr) | 2003-08-29 | 2004-08-27 | Dispositif pour atomiser un jet de matiere fondue et procede pour atomiser des metaux ou des ceramiques refractaires |
Country Status (3)
| Country | Link |
|---|---|
| EP (1) | EP1658150A1 (fr) |
| DE (1) | DE10340606B4 (fr) |
| WO (1) | WO2005023465A1 (fr) |
Families Citing this family (15)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP1923188A1 (fr) * | 2006-11-14 | 2008-05-21 | Linde Aktiengesellschaft | Dispositif de production de particule |
| DE102006056119A1 (de) * | 2006-11-14 | 2008-05-15 | Linde Ag | Vorrichtung zur Partikelerzeugung |
| US7827822B2 (en) * | 2007-07-25 | 2010-11-09 | Schott Corporation | Method and apparatus for spray-forming melts of glass and glass-ceramic compositions |
| DE102008004607A1 (de) | 2008-01-16 | 2009-05-28 | Daimler Ag | Lichtbogendrahtbrenner |
| CN102837001B (zh) * | 2012-09-29 | 2013-07-03 | 湖南恒基粉末科技有限责任公司 | 一种金属液流易流出的微细金属粉末雾化喷嘴 |
| DE102013022096B4 (de) | 2013-12-20 | 2020-10-29 | Nanoval Gmbh & Co. Kg | Vorrichtung und Verfahren zum tiegelfreien Schmelzen eines Materials und zum Zerstäuben des geschmolzenen Materials zum Herstellen von Pulver |
| DE102014016723A1 (de) | 2014-11-13 | 2016-05-19 | C. Hafner Gmbh + Co. Kg | Amorph erstarrende Legierung auf Edelmetallbasis |
| DE202014008963U1 (de) | 2014-11-13 | 2016-02-16 | C. Hafner Gmbh + Co. Kg | Amorph erstarrende Legierung auf Edelmetallbasis |
| CN104985187B (zh) * | 2015-07-08 | 2017-03-01 | 深圳市金鼎丰贵金属设备科技有限公司 | 一种粉末制备的贵金属雾化装置 |
| CN109550623B (zh) * | 2018-12-29 | 2021-01-22 | 中材江苏太阳能新材料有限公司 | 一种提高多晶硅铸锭用坩埚内表面粗糙度的方法 |
| DE102019201472A1 (de) * | 2019-02-05 | 2020-08-06 | Deutsches Institut Für Lebensmitteltechnik E.V. | Vorrichtung und Verfahren zur Herstellung feiner Fettpartikel |
| CN109986086A (zh) * | 2019-03-08 | 2019-07-09 | 北京矿冶科技集团有限公司 | 一种用于增材制造的高球形度多组元合金粉末的制备方法 |
| CN112296344B (zh) * | 2020-12-18 | 2025-06-03 | 浙江亚通新材料股份有限公司 | 一种用于改善粉末球形度的双层气雾化喷嘴 |
| DE102021212367A1 (de) | 2021-11-03 | 2023-05-04 | Sms Group Gmbh | Verdüsungs-Einheit zum Verdüsen von metallenen Schmelzen, insbesondere für pulvermetallurgische Zwecke |
| WO2025051364A1 (fr) | 2023-09-07 | 2025-03-13 | Wacker Chemie Ag | Fusion continue de silicium pour procédés en aval |
Family Cites Families (11)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE3311343C2 (de) * | 1983-03-29 | 1987-04-23 | Alfred Prof. Dipl.-Ing.Dr.-Ing. 7830 Emmendingen Walz | Verfahren zur Herstellung von feinen Metallpulvern sowie Vorrichtung zur Durchführung des Verfahrens |
| US4631013A (en) * | 1984-02-29 | 1986-12-23 | General Electric Company | Apparatus for atomization of unstable melt streams |
| US4622001A (en) * | 1985-03-12 | 1986-11-11 | Electra Form, Inc. | Cavity cooling system |
| DE3533964C1 (de) * | 1985-09-24 | 1987-01-15 | Alfred Prof Dipl-Ing Dr-I Walz | Verfahren und Vorrichtung zum Herstellen von Feinstpulver in Kugelform |
| US4784302A (en) * | 1986-12-29 | 1988-11-15 | Gte Laboratories Incorporated | Gas atomization melt tube assembly |
| US5280884A (en) * | 1992-06-15 | 1994-01-25 | General Electric Company | Heat reflectivity control for atomization process |
| US5468133A (en) * | 1992-07-27 | 1995-11-21 | General Electric Company | Gas shield for atomization with reduced heat flux |
| DE19607114A1 (de) * | 1995-01-28 | 1996-12-05 | Lueder Dr Ing Gerking | Fäden aus Schmelzen mittels kalter Gasstrahlen |
| DE19758111C2 (de) * | 1997-12-17 | 2001-01-25 | Gunther Schulz | Verfahren und Vorrichtung zur Herstellung feiner Pulver durch Zerstäubung von Schmelzen mit Gasen |
| DE19929709C2 (de) * | 1999-06-24 | 2001-07-12 | Lueder Gerking | Verfahren zur Herstellung von im Wesentlichen endlosen feinen Fäden und Verwendung der Vorrichtung zur Durchführung des Verfahrens |
| DE10001968B4 (de) * | 1999-10-15 | 2004-02-12 | Applikations- Und Technikzentrum Für Energieverfahrens-, Umwelt- Und Strömungstechnik (Atz-Evus) | Verfahren zur Herstellung eines Pulvers |
-
2003
- 2003-08-29 DE DE2003140606 patent/DE10340606B4/de not_active Expired - Lifetime
-
2004
- 2004-08-27 WO PCT/EP2004/009769 patent/WO2005023465A1/fr not_active Ceased
- 2004-08-27 EP EP04764728A patent/EP1658150A1/fr not_active Withdrawn
Non-Patent Citations (1)
| Title |
|---|
| See references of WO2005023465A1 * |
Also Published As
| Publication number | Publication date |
|---|---|
| DE10340606B4 (de) | 2005-10-06 |
| DE10340606A1 (de) | 2005-03-31 |
| WO2005023465A1 (fr) | 2005-03-17 |
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