NZ619930B2 - Processes, systems, and apparatus for forming products from atomized metals and alloys - Google Patents
Processes, systems, and apparatus for forming products from atomized metals and alloys Download PDFInfo
- Publication number
- NZ619930B2 NZ619930B2 NZ619930A NZ61993012A NZ619930B2 NZ 619930 B2 NZ619930 B2 NZ 619930B2 NZ 619930 A NZ619930 A NZ 619930A NZ 61993012 A NZ61993012 A NZ 61993012A NZ 619930 B2 NZ619930 B2 NZ 619930B2
- Authority
- NZ
- New Zealand
- Prior art keywords
- alloy
- molten alloy
- particles
- molten
- melting
- Prior art date
Links
- 239000000956 alloy Substances 0.000 title claims abstract description 488
- 229910045601 alloy Inorganic materials 0.000 title claims abstract description 464
- 238000000034 method Methods 0.000 title claims abstract description 105
- 229910052751 metal Inorganic materials 0.000 title abstract description 27
- 239000002184 metal Substances 0.000 title abstract description 27
- 150000002739 metals Chemical class 0.000 title abstract description 19
- REDXJYDRNCIFBQ-UHFFFAOYSA-N aluminium(3+) Chemical class [Al+3] REDXJYDRNCIFBQ-UHFFFAOYSA-N 0.000 claims abstract description 438
- 239000002245 particle Substances 0.000 claims abstract description 262
- 239000007787 solid Substances 0.000 claims abstract description 101
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- 210000002381 Plasma Anatomy 0.000 claims description 121
- 238000001816 cooling Methods 0.000 claims description 21
- 238000002844 melting Methods 0.000 description 188
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- 238000009718 spray deposition Methods 0.000 description 35
- 238000010313 vacuum arc remelting Methods 0.000 description 26
- 239000007789 gas Substances 0.000 description 23
- 239000000155 melt Substances 0.000 description 19
- 238000000889 atomisation Methods 0.000 description 17
- 239000012530 fluid Substances 0.000 description 16
- 239000001307 helium Substances 0.000 description 16
- 229910052734 helium Inorganic materials 0.000 description 16
- 238000010586 diagram Methods 0.000 description 14
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- 229910000601 superalloy Inorganic materials 0.000 description 13
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- 239000007788 liquid Substances 0.000 description 8
- PXHVJJICTQNCMI-UHFFFAOYSA-N nickel Chemical compound [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 description 8
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- 239000000843 powder Substances 0.000 description 8
- 238000007711 solidification Methods 0.000 description 8
- 238000007600 charging Methods 0.000 description 7
- RYGMFSIKBFXOCR-UHFFFAOYSA-N copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 7
- 229910052802 copper Inorganic materials 0.000 description 7
- 239000010949 copper Substances 0.000 description 7
- SWQJXJOGLNCZEY-UHFFFAOYSA-N helium(0) Chemical compound [He] SWQJXJOGLNCZEY-UHFFFAOYSA-N 0.000 description 7
- 238000004663 powder metallurgy Methods 0.000 description 7
- 230000001105 regulatory Effects 0.000 description 7
- WFKWXMTUELFFGS-UHFFFAOYSA-N tungsten Chemical compound [W] WFKWXMTUELFFGS-UHFFFAOYSA-N 0.000 description 7
- 229910052721 tungsten Inorganic materials 0.000 description 7
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- 230000000694 effects Effects 0.000 description 6
- 230000005484 gravity Effects 0.000 description 6
- 239000000203 mixture Substances 0.000 description 6
- RTAQQCXQSZGOHL-UHFFFAOYSA-N titanium Chemical compound [Ti] RTAQQCXQSZGOHL-UHFFFAOYSA-N 0.000 description 6
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- 210000000614 Ribs Anatomy 0.000 description 5
- 241000519995 Stachys sylvatica Species 0.000 description 5
- 238000004891 communication Methods 0.000 description 5
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- 239000002893 slag Substances 0.000 description 5
- 206010014970 Ephelide Diseases 0.000 description 4
- 229910052782 aluminium Inorganic materials 0.000 description 4
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminum Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 4
- GUTLYIVDDKVIGB-UHFFFAOYSA-N cobalt Chemical compound [Co] GUTLYIVDDKVIGB-UHFFFAOYSA-N 0.000 description 4
- 229910052803 cobalt Inorganic materials 0.000 description 4
- 239000010941 cobalt Substances 0.000 description 4
- 239000004020 conductor Substances 0.000 description 4
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- 229910052742 iron Inorganic materials 0.000 description 4
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- IJGRMHOSHXDMSA-UHFFFAOYSA-N nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 4
- 230000015572 biosynthetic process Effects 0.000 description 3
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- GUCVJGMIXFAOAE-UHFFFAOYSA-N niobium Chemical compound [Nb] GUCVJGMIXFAOAE-UHFFFAOYSA-N 0.000 description 3
- 229910052758 niobium Inorganic materials 0.000 description 3
- 239000010955 niobium Substances 0.000 description 3
- 230000002829 reduced Effects 0.000 description 3
- 239000011163 secondary particle Substances 0.000 description 3
- 238000011144 upstream manufacturing Methods 0.000 description 3
- 229910000967 As alloy Inorganic materials 0.000 description 2
- NLZUEZXRPGMBCV-UHFFFAOYSA-N Butylhydroxytoluene Chemical compound CC1=CC(C(C)(C)C)=C(O)C(C(C)(C)C)=C1 NLZUEZXRPGMBCV-UHFFFAOYSA-N 0.000 description 2
- 229940035295 Ting Drugs 0.000 description 2
- 238000009825 accumulation Methods 0.000 description 2
- XKRFYHLGVUSROY-UHFFFAOYSA-N argon Chemical compound [Ar] XKRFYHLGVUSROY-UHFFFAOYSA-N 0.000 description 2
- 238000006243 chemical reaction Methods 0.000 description 2
- 238000010276 construction Methods 0.000 description 2
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- 230000001808 coupling Effects 0.000 description 2
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- 238000004090 dissolution Methods 0.000 description 2
- 238000009826 distribution Methods 0.000 description 2
- 239000003574 free electron Substances 0.000 description 2
- 239000001257 hydrogen Substances 0.000 description 2
- 229910052739 hydrogen Inorganic materials 0.000 description 2
- 238000005272 metallurgy Methods 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 238000006011 modification reaction Methods 0.000 description 2
- ZOKXTWBITQBERF-UHFFFAOYSA-N molybdenum Chemical compound [Mo] ZOKXTWBITQBERF-UHFFFAOYSA-N 0.000 description 2
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- QCWXUUIWCKQGHC-UHFFFAOYSA-N zirconium Chemical compound [Zr] QCWXUUIWCKQGHC-UHFFFAOYSA-N 0.000 description 2
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- 229910052582 BN Inorganic materials 0.000 description 1
- 229910052684 Cerium Inorganic materials 0.000 description 1
- IBDHMAYMLSYGAK-UHFFFAOYSA-N Lanthanum boride Chemical compound [La].B12B3[B-]41B1B4[B-]312 IBDHMAYMLSYGAK-UHFFFAOYSA-N 0.000 description 1
- PZNSFCLAULLKQX-UHFFFAOYSA-N N#B Chemical compound N#B PZNSFCLAULLKQX-UHFFFAOYSA-N 0.000 description 1
- 241001313099 Pieris napi Species 0.000 description 1
- 229910001069 Ti alloy Inorganic materials 0.000 description 1
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- 239000012080 ambient air Substances 0.000 description 1
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- UIMGJWSPQNXYNK-UHFFFAOYSA-N azane;titanium Chemical compound N.[Ti] UIMGJWSPQNXYNK-UHFFFAOYSA-N 0.000 description 1
- 239000010953 base metal Substances 0.000 description 1
- 238000009835 boiling Methods 0.000 description 1
- OKTJSMMVPCPJKN-UHFFFAOYSA-N carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 230000015556 catabolic process Effects 0.000 description 1
- 229910010293 ceramic material Inorganic materials 0.000 description 1
- GWXLDORMOJMVQZ-UHFFFAOYSA-N cerium Chemical compound [Ce] GWXLDORMOJMVQZ-UHFFFAOYSA-N 0.000 description 1
- 239000002801 charged material Substances 0.000 description 1
- VEXZGXHMUGYJMC-UHFFFAOYSA-M chloride anion Chemical compound [Cl-] VEXZGXHMUGYJMC-UHFFFAOYSA-M 0.000 description 1
- 230000003749 cleanliness Effects 0.000 description 1
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- 230000005495 cold plasma Effects 0.000 description 1
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- 238000007872 degassing Methods 0.000 description 1
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- 230000001627 detrimental Effects 0.000 description 1
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- 235000013601 eggs Nutrition 0.000 description 1
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- 238000001704 evaporation Methods 0.000 description 1
- 239000010419 fine particle Substances 0.000 description 1
- 238000007667 floating Methods 0.000 description 1
- 239000002803 fossil fuel Substances 0.000 description 1
- 238000000227 grinding Methods 0.000 description 1
- 230000036541 health Effects 0.000 description 1
- UFHFLCQGNIYNRP-UHFFFAOYSA-N hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 1
- 150000002431 hydrogen Chemical class 0.000 description 1
- 230000000977 initiatory Effects 0.000 description 1
- 229910052500 inorganic mineral Inorganic materials 0.000 description 1
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- 229910001068 laves phase Inorganic materials 0.000 description 1
- 239000011344 liquid material Substances 0.000 description 1
- 239000011159 matrix material Substances 0.000 description 1
- 238000000691 measurement method Methods 0.000 description 1
- 238000010309 melting process Methods 0.000 description 1
- 150000001247 metal acetylides Chemical class 0.000 description 1
- 229910001092 metal group alloy Inorganic materials 0.000 description 1
- 239000007769 metal material Substances 0.000 description 1
- 239000011707 mineral Substances 0.000 description 1
- 229910001000 nickel titanium Inorganic materials 0.000 description 1
- 150000004767 nitrides Chemical class 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 229910052574 oxide ceramic Inorganic materials 0.000 description 1
- 239000011224 oxide ceramic Substances 0.000 description 1
- 239000004848 polyfunctional curative Substances 0.000 description 1
- 238000005036 potential barrier Methods 0.000 description 1
- 238000010248 power generation Methods 0.000 description 1
- 238000004886 process control Methods 0.000 description 1
- 230000001681 protective Effects 0.000 description 1
- 239000011241 protective layer Substances 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 239000011819 refractory material Substances 0.000 description 1
- 238000009877 rendering Methods 0.000 description 1
- 230000001846 repelling Effects 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 238000000365 skull melting Methods 0.000 description 1
- 239000012265 solid product Substances 0.000 description 1
- 238000000638 solvent extraction Methods 0.000 description 1
- 241000894007 species Species 0.000 description 1
- 238000005507 spraying Methods 0.000 description 1
- 229910001220 stainless steel Inorganic materials 0.000 description 1
- 239000007858 starting material Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 238000006467 substitution reaction Methods 0.000 description 1
- 230000002459 sustained Effects 0.000 description 1
- GUVRBAGPIYLISA-UHFFFAOYSA-N tantalum Chemical compound [Ta] GUVRBAGPIYLISA-UHFFFAOYSA-N 0.000 description 1
- 229910052715 tantalum Inorganic materials 0.000 description 1
- 230000036962 time dependent Effects 0.000 description 1
- 230000001131 transforming Effects 0.000 description 1
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- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
Classifications
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B22—CASTING; POWDER METALLURGY
- B22D—CASTING OF METALS; CASTING OF OTHER SUBSTANCES BY THE SAME PROCESSES OR DEVICES
- B22D23/00—Casting processes not provided for in groups B22D1/00 - B22D21/00
- B22D23/003—Moulding by spraying metal on a surface
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B22—CASTING; POWDER METALLURGY
- B22D—CASTING OF METALS; CASTING OF OTHER SUBSTANCES BY THE SAME PROCESSES OR DEVICES
- B22D30/00—Cooling castings, not restricted to casting processes covered by a single main group
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B22—CASTING; POWDER METALLURGY
- B22D—CASTING OF METALS; CASTING OF OTHER SUBSTANCES BY THE SAME PROCESSES OR DEVICES
- B22D35/00—Equipment for conveying molten metal into beds or moulds
- B22D35/02—Equipment for conveying molten metal into beds or moulds into beds
-
- 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
- B22F2009/0836—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 with electric or magnetic field or induction
-
- 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
- B22F2009/084—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 combination of methods
-
- 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
- B22F2009/0848—Melting process before atomisation
-
- 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
- B22F2009/086—Cooling after atomisation
-
- 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
- B22F3/00—Manufacture of workpieces or articles from metallic powder characterised by the manner of compacting or sintering; Apparatus specially adapted therefor ; Presses and furnaces
- B22F3/115—Manufacture of workpieces or articles from metallic powder characterised by the manner of compacting or sintering; Apparatus specially adapted therefor ; Presses and furnaces by spraying molten metal, i.e. spray sintering, spray casting
-
- 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
-
- 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
-
- C—CHEMISTRY; METALLURGY
- C22—METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
- C22C—ALLOYS
- C22C19/00—Alloys based on nickel or cobalt
- C22C19/03—Alloys based on nickel or cobalt based on nickel
- C22C19/05—Alloys based on nickel or cobalt based on nickel with chromium
- C22C19/051—Alloys based on nickel or cobalt based on nickel with chromium and Mo or W
- C22C19/055—Alloys based on nickel or cobalt based on nickel with chromium and Mo or W with the maximum Cr content being at least 20% but less than 30%
-
- C—CHEMISTRY; METALLURGY
- C22—METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
- C22C—ALLOYS
- C22C19/00—Alloys based on nickel or cobalt
- C22C19/03—Alloys based on nickel or cobalt based on nickel
- C22C19/05—Alloys based on nickel or cobalt based on nickel with chromium
- C22C19/051—Alloys based on nickel or cobalt based on nickel with chromium and Mo or W
- C22C19/056—Alloys based on nickel or cobalt based on nickel with chromium and Mo or W with the maximum Cr content being at least 10% but less than 20%
-
- C—CHEMISTRY; METALLURGY
- C23—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
- C23C—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; SURFACE TREATMENT OF METALLIC MATERIAL BY DIFFUSION INTO THE SURFACE, BY CHEMICAL CONVERSION OR SUBSTITUTION; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL
- C23C26/00—Coating not provided for in groups C23C2/00 - C23C24/00
-
- C—CHEMISTRY; METALLURGY
- C23—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
- C23C—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; SURFACE TREATMENT OF METALLIC MATERIAL BY DIFFUSION INTO THE SURFACE, BY CHEMICAL CONVERSION OR SUBSTITUTION; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL
- C23C4/00—Coating by spraying the coating material in the molten state, e.g. by flame, plasma or electric discharge
- C23C4/12—Coating by spraying the coating material in the molten state, e.g. by flame, plasma or electric discharge characterised by the method of spraying
-
- C—CHEMISTRY; METALLURGY
- C23—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
- C23C—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; SURFACE TREATMENT OF METALLIC MATERIAL BY DIFFUSION INTO THE SURFACE, BY CHEMICAL CONVERSION OR SUBSTITUTION; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL
- C23C4/00—Coating by spraying the coating material in the molten state, e.g. by flame, plasma or electric discharge
- C23C4/12—Coating by spraying the coating material in the molten state, e.g. by flame, plasma or electric discharge characterised by the method of spraying
- C23C4/123—Spraying molten metal
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P60/00—Technologies relating to agriculture, livestock or agroalimentary industries
- Y02P60/20—Reduction of greenhouse gas [GHG] emissions in agriculture, e.g. CO2
- Y02P60/21—Dinitrogen oxide [N2O], e.g. using aquaponics, hydroponics or efficiency measures
Abstract
Processes, systems, and apparatuses are disclosed for forming products from atomized metals and alloys. A stream of molten alloy and/or a series of droplets of molten alloy are produced. The molten alloy is atomized to produce electrically-charged particles of the molten alloy by impinging electrons on the stream of molten alloy and/or the series of droplets of molten alloy. The electrically-charged molten alloy particles are accelerated with at least one of an electrostatic field and an electromagnetic field. The accelerating molten alloy particles are cooled to a temperature that is less than a solidus temperature of the molten alloy particles so that the molten alloy particles solidify while accelerating. The solid alloy particles are impacted onto a substrate and the impacting particles deform and metallurgically bond to the substrate to produce a solid alloy preform. on the stream of molten alloy and/or the series of droplets of molten alloy. The electrically-charged molten alloy particles are accelerated with at least one of an electrostatic field and an electromagnetic field. The accelerating molten alloy particles are cooled to a temperature that is less than a solidus temperature of the molten alloy particles so that the molten alloy particles solidify while accelerating. The solid alloy particles are impacted onto a substrate and the impacting particles deform and metallurgically bond to the substrate to produce a solid alloy preform.
Description
TITLE
PROCESSES, S, AND APPARATUS FOR FORMING PRODUCTS FROM
ATOMIZED METALS AND ALLOYS
TECHNICAL FIELD
[0001 ] This disclosure relates to melting, atomizing, and sing metals and
alloys, and to forming metal and alloy products using atomized metals and alloys.
BACKGROUND
Metals and alloys, such as, for example, iron, nickel, titanium, cobalt, and
alloys based on these metals, are often used in critical engineering applications in which
fine-grained microstructures, homogeneity, and/or substantially defect free compositions
are ageous or necessary. Problems such as undesired grain growth and
segregation in metal and alloy castings and ingots may be detrimental to end—use
applications and can significantly increase the costs associated with high y alloy
production. Conventional alloy production techniques, such as vacuum induction
g, electroslag refining, and vacuum arc remelting, may be used to reduce the
amount of impurities and contaminants in alloy castings. However, in various instances,
tional nd—wrought alloy production processes cannot be used to produce
alloys having the fine—grained microstructures, homogeneity, and/or substantially defect
free compositions desired or required for various critical engineering applications.
Powder metallurgy processes can allow for the tion of metals and
alloys having fine—grained microstructures that cannot be achieved with cast—and-
wrought alloy production processes. However, powder metallurgy processes are more
complex than nd-wrought alloy tion processes and may produce metals and
alloys having relatively high levels of voids and porosity. Powder metallurgy processes
also have the potential to introduce impurities and contaminants into metal and alloy
products during the production, handling, and processing of the powder feed stocks
used to form the products.
SUMMARY
[0003a] According to the present invention, there is provided a process
comprising: producing at least one of a stream of molten alloy and a series of droplets of
molten alloy; producing electrically-charged les of the molten alloy by impinging
electrons on at least one of the stream of molten alloy and the series of droplets of molten
alloy to atomize the molten alloy; accelerating the electrically-charged molten alloy particles
with at least one of an electrostatic field and an electromagnetic field; cooling the molten
alloy particles to a temperature that is no greater than a solidus temperature of the alloy so
that the molten alloy particles solidify while rating and form solid alloy particles;
impacting the solid alloy particles onto a substrate, wherein the impacting les deform
and metallurgically bond to the ate to produce a solid alloy preform.
[0003b] The present invention also provides a process comprising: ing at
least one of a stream of molten alloy and a series of ts of molten alloy; producing a
three-dimensional electron field; impinging electrons from the three-dimensional electron
field on at least one of the stream of molten alloy and the series of droplets of molten alloy to
atomize the molten alloy and produce electrically-charged particles of the molten alloy;
accelerating the electrically-charged molten alloy particles with a electrostatic field;
cooling the molten alloy particles to a temperature that is no greater than a solidus
temperature of the molten alloy particles so that the molten alloy particles solidify while
accelerating; impacting the solid alloy particles onto a ate, wherein the impacting
particles deform and metallurgically bond to the substrate to produce a solid alloy preform.
In a non—limiting embodiment, a process according to the present
disclosure comprises ing at least one of a stream of molten alloy and a series of
droplets of molten alloy. Electrically—charged particles of the molten alloy are produced
by impinging electrons on at least one of the stream of molten alloy and the series of
droplets of molten alloy to atomize the molten alloy. The electrically-charged molten alloy
particles are accelerated with at least one of an electrostatic field and an
electromagnetic field. The molten alloy particles are cooled to a temperature less than a
solidus temperature of the molten alloy particles so that the molten alloy particles solidify
while accelerating. The solid alloy les are impacted onto a ate, wherein the
impacting particles deform and metallurgically bond to the substrate to produce a solid
alloy preform.
It is understood that the invention disclosed and described in this
specification is not limited to the embodiments summarized in this summary.
BRIEF DESCRIPTION OF THE GS
s features and characteristics of the non-limiting and non-
exhaustive embodiments disclosed and described in this specification may be better
understood by reference to the accompanying figures, in which:
Figure 1 is a schematic illustration of an alloy processing system;
WO 22552 2012/046838
Figure 2 is a schematic diagram of an atomizing assembly, wherein
a generally rectangular-shaped field of electrons is produced in the pathway of molten
alloy passing through the atomizing assembly;
Figure 3 is a schematic m of an atomizing assembly,
wherein a ing apparatus produces a field of electrons in the pathway of molten
alloy passing through the atomizing assembly;
Figure 4 is a schematic diagram of an ing assembly, wherein
electrons used to produce an on field in the pathway of molten alloy passing
through the atomizing assembly are produced from the outer surface of a filament;
Figure 5 is a tic diagram of the atomization of a molten alloy
droplet in an on beam atomizing ly;
s 6, 7, 7A, 8, 8A, 9, and 9A are schematic diagrams of
systems and apparatus configured to form an alloy preform by a solid-spray—forming
process;
Figures 10—13 are schematic diagrams of melting assemblies that
produce molten alloy;
Figures 14-1 7 and 17A are schematic diagrams of systems and
apparatus configured to form an alloy preform by a solid-spray—forming process;
Figure 18 is a flow diagram of a solid-spray-forming process;
Figures 19A-19F are schematic diagrams that collectively show a
spray—forming system implementing a solid—spray—forming process;
Figure 20 is a schematic diagram of various components of a wire-
discharge ion plasma emitter;
Figure 21 is a schematic diagram of an electron beam cold hearth
melting assembly including multiple wire—discharge ion plasma emitters;
; 72,—. .1: ..
Figure 22 is a schematic diagram of Various components of a wire-
discharge ion plasma emitter;
PCT/U82012/046838
Figure 23 is a schematic diagram of an electron beam g
apparatus including a wire—discharge ion plasma emitter;
Figure 24 is a perspective view of a wire-discharge ion plasma
emitter;
Figure 25 is a schematic m illustrating the operation of the
wire—discharge ion plasma emitter shown in Figure 24; and
Figure 26 is a schematic diagram of an electron beam cold hearth
melting assembly including multiple wire-discharge ion plasma emitters.
The reader will iate the foregoing details, as well as others,
upon considering the following detailed description of various non—limiting and non-
exhaustive embodiments according to the present disclosure.
DESCRIPTlON
Various embodiments are described and rated in this
ication to provide an overall understanding of the structure, function, operation,
manufacture, and use of the disclosed processes and products. It is understood that
the s embodiments bed and illustrated in this ication
are non-limiting
and non—exhaustive. Thus, the invention is not limited by the description of the various
non—limiting and non-exhaustive embodiments sed in this specification. Rather,
the invention is defined solely by the claims. The features and characteristics illustrated
and/or described in tion with various embodiments
may be combined with the
features and characteristics of other embodiments. Such modifications and variations
are intended to be included within the scope of this specification. As such, the claims
may be amended to recite any features or characteristics sly or inherently
bed in, or othenivise expressly or inherently supported by, this specification.
Further, Applicant reserves the right t‘d‘éft‘imfififieréiaiffisto affirmatively disclaim
features or characteristics that may be present in the prior art. Therefore, any such
amendments comply with the requirements of 35 U,S.C. § 112, first paragraph, and 35
PCTfU82012/046838
U.S.C. § 132(a). The various embodiments disclosed and described in this specification
can comprise, consist of, or consist essentially of the features and characteristics as
variously described herein.
Any patent, publication, or other disclosure material identified
herein is incorporated by reference into this specification in its ty unless othen/vise
ted, but only to the extent that the incorporated material does not ct with
ng definitions, statements, or other sure material expressly set forth in this
ication. As such, and to the extent ary, the express disclosure as set forth
in this specification supersedes any conflicting material incorporated by reference
herein. Any material, or portion thereof, that is said to be incorporated by reference into
this ication, but which cts with existing definitions, statements, or other
disclosure material set forth herein, is only incorporated to the extent that no conflict
arises between that incorporated material and the existing disclosure material.
Applicant reserves the right to amend this specification to expressly recite any subject
matter, or portion thereof, incorporated by reference herein.
Reference throughout this specification to "various non-limiting
embodiments," or the like, means that a particular feature or characteristic may be
included in an embodiment. Thus, use of the phrase “in various non-limiting
embodiments," or the like, in this specification does not necessarily refer to a common
embodiment, and may refer to different ments. Further, the particular features or
characteristics may be combined in any suitable manner in one or more embodiments.
Thus, the particular features or characteristics illustrated or described in tion with
various embodiments may be combined, in whole or in part, with the features or
characteristics of one or more other embodiments without limitation. Such modifications
and variations are intended to be included within the scope of the present ication.
ln this specification, other than where ise indicated, all
numerical parameters are to be understood as being prefaced and modified inall " "
instances by the term "about", in which the numerical parameters possess the inherent
variability characteristic of the ying measurement techniques used to determine
PCTfUS2012/046838
the numerical value of the parameter. At the very least, and not as an attempt to limit
the application of the doctrine of equivalents to the scope of the claims, each cal
parameter described in the present description should at least be ued in light of
the number of reported significant digits and by applying ordinary rounding techniques.
Also, any numerical range recited in this specification is intended to
include all sub-ranges of the same numerical precision subsumed within the recited
range. For example, a range of "1.0 to 10.0“ is intended to include all sub—ranges
between (and including) the d minimum value of 1.0 and the recited maximum
value of 10.0, that is, having a minimum value equal to or greater than 1.0 and a
maximum value equal to or less than 10.0, such as, for example, 2.4 to 7.6. Any
m numerical limitation recited in this ication is intended to e all lower
numerical limitations subsumed therein and any minimum numerical limitation recited in
this specification is intended to e all higher numerical limitations subsumed
therein. Accordingly, Applicant reserves the right to amend this specification, including
the claims, to expressly recite any sub-range subsumed within the
ranges expressly
recited herein. All such ranges are intended to be inherently described in this
specification such that amending to expressly recite any such sub—ranges would comply
with the requirements of 35 U.S.C. § 112, first paragraph, and 35 U.S.C. § 132(a).
The tical articles "one", "a“, "an", and "the", as used in this
specification, are intended to include "at least one" or “one or more", unless othenNise
indicated. Thus, the articles are used in this specification to refer to one or more than
one (i.e., to "at least one") of the grammatical objects of the e. By way of e,
"a ent" means one or more components, and thus, ly, more than one
component is contemplated and may be employed or used in an implementation of the
described embodiments. Further, the use of a singular noun includes the plural, and the
use of a plural noun includes the singular, unless the context of the usage requires
otherwise.
in various critical applications, ents must be manufactured
from alloys, such as, for example, nickel—base superalloys, in the form of large diameter
PCT/U82012/046838
ingots that lack significant segregation. Such ingots should be substantially free of
ve and negative segregation. “Freckles" are a common manifestation of ve
segregation and are metallographically observable as dark etched regions enriched in
solute elements. es result from the flow of solute—rich interdendritic liquid in the
mushy zone of a cast ingot during soiidification. Freckles in Alloy 718, for example, are
enriched in niobium compared to the overall alloy matrix, have a high density of
carbides, and usually contain Laves phase. As such, freckles are ularly
disadvantageous in alloys to be used in critical applications.
“White spots" are a common type of negative segregation. White
spots are metallographically observable as tight etched regions, which are depleted in
hardener solute elements, such as m. White spots are typically classified into
tic, discrete, and solidification white spots. While there may be some tolerance
for dendritic and solidification white spots, discrete white spots are of major concern
because they frequently are associated with a cluster of oxides and nitrides that can act
as crack initiation sites in cast alloy articles.
lngots and preforms substantially lacking positive and ve
segregation and that are also free of freckles may be referred to as "premium quality"
ingots and ms. Premium quality nickel-base superalioy ingots and preforms are
required in s al applications including, for example, rotating components in
aeronautical or land-based power generation turbines and in other applications in which
segregation-related metallurgical defects may result in catastrophic failure of the
component during operation. As used herein, an ingot or preform "substantially lacks"
positive and negative ation when such types of segregation are wholly absent or
are present only to an extent that does not make the ingot or preform unsuitable for use
in critical applications, such as use for fabrication into rotating components for
aeronautical and land-based e applications.
Nickel—base superalloys subteetatosignificant positive and negative
segregation during casting e, for example, Alloy 718 (UNS N07718) and Alloy 706
(UNS N09706). in order to minimize segregation when casting these alloys for use in
PCT/U82012/046838
critical applications, and to better ensure that the cast alloy is free of deleterious non-
metallic inclusions, the molten ic material is appropriately refined before being
finally cast. A que for refining Alloy 718, as well as various other segregation—
prone nickel-base superalloys such as Alloy 706, is the "triple melt" technique, which
combines, sequentially, vacuum induction melting (VIM), oslag refining/remelting
(ESR), and vacuum arc remelting (VAR). Premium quality ingots of these segregation~
prone materials, however, are difficult to produce in large diameters by VAR melting, the
last step in the triple melt sequence. In some cases, large diameter ingots are
ated into single components, in which case areas of unacceptable segregation in
st ingots cannot be selectively removed prior to component fabrication.
Consequently, the entire ingot or a portion of the ingot may need to be scrapped.
ingots of Alloy 718, Alloy 706, and other nickel—base superalloys
such as Alloy 600 (UNS N06600), Alloy 625 (UNS N06625), Alloy 720, and Waspaloy®
(UNS N07001) are increasingly required in larger weights and correspondingly larger
diameters for various emerging applications. Such applications e, for example,
rotating components for larger land-based and aeronautical turbines. Larger ingots are
needed not only to achieve the final component weight economically, but also to
facilitate sufficient thermomechanical working to adequately break down the ingot
structure and e all final ical and structural requirements.
The g and casting of large diameter superalloy ingots
accentuates a number of basic urgical and processing related issues. For
example, heat extraction during melt solidification becomes more difficult with
increasing ingot diameter, ing in longer fication times and deeper molten
pools. This increases the tendency towards positive and negative segregation. Also,
larger ingots and ESR/VAFl electrodes can te higher thermal stresses during
heating and cooling. Alloy 718 is particularly prone to these problems. To allow for the
production of largediameter VAR ingots ofacceptable metallurgical qualityfrom Alloy.— Max
‘\ ”Hagen“, _ .:
,. ._:. ,-. winds:
1'1““zfigg:
718 and various other segregationprone nickel-base superalloys, specialized melting
and heat treatment sequences have been developed. One such specialized melting
PCT/U82012/046838
and heat ent sequence is described in United States Patent No. 6,416,564, which
is hereby incorporated by reference into this ication.
hstanding, powder metallurgy techniques may be used to
produce m quality alloy products such as large diameter nickel-base superalloy
ingots. Spray g is one powder metallurgy que for producing large diameter
superalloy ingots. During spray forming, a stream of molten alloy is atomized to form a
spray of fine molten alloy droplets or particles. The molten particles are then directed to
a collector where they coalesce and solidify into a coherent, near-fully—dense preform.
in various applications, controlled movement of the collector and atomizer, along with
control of the molten-metal transport process, allows high quality large preforms to be
produced. The spray forming process is capable of ing fine-grained
homogeneous microstructures with equiaxed grains and more than 98 t
theoretical density for a wide range of alloys. However, conventional spray forming
generally employs fluid impingement atomization techniques, which present a number
of drawbacks.
in fluid ement atomization techniques, either a
gas or a liquid
is impinged on a stream of a molten metallic material. impingement using liquid or
gases may introduce contaminants into the atomized material. Given that fluid
impingement does not occur in a vacuum nment, even impingement techniques
using inert gases can introduce significant levels of impurities into the atomized
material. Various non—fluid impingement atomization techniques that
may be ted
in a vacuum environment have been developed. These ques include, for
example, the atomization techniques described in US. Patent No. 6,772,961 (referred
to is this specification as "US-6,722,961"), which is hereby incorporated by reference
into this specification.
US-6,722,961 describes techniques wherein molten alloy droplets
or a molten alloy stream producedsbyea'melting"device coupled with a controlled
dispensing device are rapidly ostatically charged by applying a high voltage to the
droplets at a high rise rate. The electrostatic forces set up within the charged droplets
PCT/U82012/046838
cause the droplets to break up or atomize into smaller secondary particles. In one
technique described in US-6,722,961, primary molten droplets produced by the nozzle
of a dispensing device are treated by an ic field from a ring-shaped electrode
adjacent to and ream of the nozzle. Electrostatic forces developed within the
primary droplets exceed the surface n forces of the particles and result in
formation of smaller secondary particles. Additional ring—shaped field—producing
electrodes may be provided downstream to treat the secondary particles in the same
way, producing yet smaller molten particles.
Electron beam atomization is r non-fluid impingement
technique for atomizing molten material that is conducted in a vacuum. in general, the
que involves using an electron beam to inject a charge into a region of a molten
alloy stream and/or a series of molten alloy ts. Once the region or droplet
accumulates sufficient charge exceeding the Rayleigh limit, the region or droplet
becomes unstable and is disrupted into fine particles (i.e., atomizes). An electron beam
atomization technique is described in US. Patent Nos. 6,772,961; 7,578,960;
7,803,212; and 7,803,211; which are hereby incorporated by reference into this
ication.
22,961 also discloses techniques using electrostatic and/or
electromagnetic fields to control the acceleration, speed, and/or direction of molten alloy
particles formed by atomization in the process of producing spray formed preforms or
powders. As described in US—6,722,961, such techniques provide substantial
downstream l of ed molten material and can reduce
overspray and other
material wastage, improve quality, and enhance the density of solid preforms made by
spray forming techniques.
Methods of collecting atomized molten materials as unitary
preforms include spray forming and ted casting. With respect to nucleated
, .casting, specific nce is drawn to US; Patent Nos. 5,381,847; 6,264f75f‘7";‘~‘a‘no”9‘“'i“ ‘ “
6,496,529, which are hereby incorporated by reference into this specification. in
general, ted casting involves atomizing a molten alloy stream and then directing
W0 2013/022552 PCTfUS2012/046838
the resultant molten alloy les into a casting mold having a desired shape. The
droplets coalesce and solidify as a unitary article shaped by the mold, and the casting
may be further processed into a desired component. in general, spray g es
directing atomized molten material onto a surface of, for example, a platen or a cylinder
to coalesce, solidify, and form a free—standing preform that may be further sed
into a desired component.
[0043} As noted, many of the techniques for melting, atomizing, and
processing metals and alloys to produce solid preforms are deficient in one or more
respects. Such deficiencies include, for e, process complexity and cost; the
existence of high residual stresses, voids, porosity, oxides, and other contaminants in
the preform; yield losses due to overspray; limitations on applicable metals and ;
and inherent size limitations. These deficiencies are particularly problematic in the
production of s alloys such as -base superailoys. The various non-limiting
embodiments disclosed and described in this specification are directed, in part, to
processes, systems, and tus that overcome at least some of these deficiencies,
among others, and provide improved techniques for the production of metal and alloy
ts such as, for example, large diameter ingots and other m quality
The various non-limiting embodiments disclosed and described in
this specification are directed, in part, to processes, systems, and apparatus for melting
and ing metals and metallic (i.e., metal-containing) alloys to produce atomized
molten materials that may be at least partially solidified into alloy particles used to
produce unitary and monolithic alloy preforms and other articles. As used herein, the
term “alloy“ refers to both metals and metallic alloys such as, for example, iron, nickel,
titanium, cobalt, and alloys based on these metals.
The various non-limiting embodiments disclosed herein
employ equipmentgandztechniques that e electrons to melt alloys and/or atomizer" -. 2 Stir—var: J“
molten alloys to produce molten alloy particles that are solidified and solid-spray—formed
to produce unitary and monolithic preforms and other alioy articles. In various non-
PCT/U82012/046838
limiting embodiments, the processes, systems, and apparatus disclosed herein may be
useful in -base superalloy preform and article production, where cast-and-wrought
metallurgy, triple melt, and powder metallurgy techniques have attendant disadvantages
as discussed above.
in various non-limiting embodiments, a solid-spray—forming
process
comprises producing at least one of a stream of molten alloy and a series of droplets of
molten alloy. Electrically—charged particles of the molten alloy are ed by
impinging electrons on at least one of the stream of molten alloy and the series of
droplets of molten alloy to atomize the molten alloy. The ically-charged molten
alloy particles are accelerated with at least one of an electrostatic field and an
electromagnetic field. The molten alloy particles are cooled to a temperature less than
a s temperature of the molten alloy particles so that the molten alloy particles
soiidify while accelerating. The solidified alloy particles are impacted onto a substrate,
wherein the impacting particles deform and metallurgically bond to the substrate and to
each other to produce a solid alloy preform.
Referring to Figure 1, various non-limiting embodiments of a
system 100, configured to perform a solid-spray~forming process as described in this
specification, includes: a melting assembly 110 (also referred to herein as a “melting
apparatus" or ng device") that produces at least one of a stream and a series of
droplets of molten alloy; an on beam atomizing assembly 112 (also referred to
herein as an "atomizing apparatus" or “atomizing device") that atomizes molten alloy
received from the melting assembly 110 and es relatively small molten alloy
particles; a field producing ly 114 (also ed to herein as a "field producing
apparatus" or "field producing device") that produces at least one of an electrostatic field
and an electromagnetic field that influences at least one of the acceleration, speed, and
direction of one or more of the alloy particles ed by the atomizing assembly 112;
and a collector 116 onto which solidified alloy particlesimpact, deform, and
metallurgically bond to term a preform.
PCT/U82012/046838
In various non-limiting embodiments, a solid-spray—torming
process
comprises: producing a stream of molten alloy and/or a series of droplets of molten
alloy in a g assembly, which may be substantially free from ceramic in regions of
the melting assembly contacted by the molten alloy; producing molten alloy particles in
an ing assembly by impinging electrons on molten alloy received from the g
assembly; producing at least one of an ostatic field and an electromagnetic field,
wherein molten alloy particles from the atomizing assembly interact with the field, and
the field influences at least one of the acceleration, speed, and direction of the molten
alloy particles; cooling the molten alloy particles during the transport of the particles
from the atomizing assembly to form solid alloy particles; and collecting the solid alloy
particles in a collector as a solid preform.
As used herein, the term “melting assembly" and the like refer to a
source of a stream and/or a series of droplets of a molten alloy, which may be produced
from a charge of starting materials, scrap, an ingot, a consumable electrode, and/or
another source of the alloy. The melting assembly is in fluid communication with and
feeds molten alloy to an atomizing assembly. The g ly
may substantially
lack ceramic material in s of the assembly that are contacted by molten material.
As used herein, the phrase "substantially lacks ceramic" and the like means that
ceramic either is absent in regions of the melting assembly that the molten material
ts during operation of the assembly, or is present in regions of the melting
assembly that do contact the molten alloy during normal operation but in a way that
does not result in the inclusion of problematic amounts or sizes of ceramic particles
inclusions in the molten alloy.
in various non-limiting embodiments, it may be important to prevent
or substantially limit contact between molten alloy al and c material in the
melting assembly and other components of the systems and tus described
herein This may be so because ceramic particles can "wash out" of ceramic linings
;%7_
andmixWith molten alloy. Ceramic particles generally have a higher g point
temperature than molten alloy material and may be orated into subsequently
formed preforms. Once incorporated into a solid product, the ceramic particles can
2012/046838
fracture and initiate cracks in the t during low cycle fatigue, for example. Once
initiated, cracks can grow and result in product failure. Thus, depending on the
intended application for the preform material, for e, there
may be little or no
allowance for the presence of ceramic particles in the material.
in cast-and-wrought metallurgy, ceramic particles from a vacuum
induction melting (VIM) step can be removed during a subsequent vacuum arc
remelting (VAR) step or, when using triple-melt practice, during electroslag
refining/remelting (ESR) plus VAR steps. ore, in various non-limiting
embodiments, a melting ly may comprise VAR or ESR ent. Oxide
ceramic cleanliness achieved using various practices
may be evaluated using a semi—
quantitative test known as an "EB button" test, wherein a sample electrode of the
al to be ted is electron beam melted in a le and the resulting floating
raft of oxide is ed for the largest oxide present.
in powder metallurgy, alloy powder is consolidated into product
after final solidification and there is no means of further refining the product to
remove
oxides. instead, the powder is sieved and the t fraction of powder that is made
into product is that which is equivalent to the smallest defect that part designers use in
their design criteria. in the design of the most critical aircraft engine parts from
consolidated metallic powders, for example, the st modeled defect is
approximately 44 microns and, thus, powders having a sieve size no larger than this are
used. For less critical aircraft engine parts, the smallest modeled defect could be
large as approximately 149 microns and, thus, powders having a sieve size no larger
than this are used.
Examples of melting techniques that do not introduce ceramic
inclusions and that may be included in an apparatus or system configured to perform
solid-spray-forming process as described in this specification include, but are not
limited:- -melting devices comprising vacummselouble—eiectrode remelting device's; ’
melting devices comprising a combination of a cold induction guide and either an
eiectroslag refining/remelting device or a vacuum arc remelting device; plasma arc
WO 22552 2012/046838
melting devices; electron beam melting devices; and electron beam cold hearth g
devices.
As used herein, the term "atomizing assembiy" and the like refers
to an apparatus that impinges at least one stream of electrons (i. a, an electron beam)
or a field of ons on molten alloy received from the melting assembly. As used
herein, "impinges" means to bring into contact. In this manner, the electrons impart a
net negative charge to the impinged region of the stream and/or to the impinged
individual molten alloy droplets. As discussed in 72,961 and below,
once the
charge in a droplet or a particular region of a stream s a sufficient magnitude, the
region or droplet becomes unstable and is disrupted (‘1'.e;, ed) into smaller molten
alloy particles. As used herein, "molten alioy particles" refers to particles that include
some t of molten material, but which are not necessarily entirely molten. As used
herein, "solid alloy particles" refers to particles that are at a temperature below the
soiidus temperature of the material and, therefore, are entirely soiid.
in various embodiments, an atomizing assembly
may comprise an
electron beam atomizing assembly, apparatus, device, or the like. As discussed in US-
6,772,961, an electron beam atomizing apparatus may rapidly apply an electrostatic
charge to a stream or droplets of molten alloy. An electron beam atomizing apparatus
may be configured so that the electrostatic charge imparted to a molten alloy physically
disrupts the stream or droplet and produces one or more smaller molten alloy les
from the molten alloy, thereby atomizing the material. Atomization of molten alloy
material using rapid electrostatic ng through impingement by electrons
may result
in the rapid breakup of the alloy into relatively small particles due to electrostatic
repulsion forces imparted within the material. More specifically, a region or droplet of
molten alloy is rapidly electrostatically charged beyond the “Rayleigh " such that
the electrostatic forces within the region or droplet exceed the surface tension of the
molten alloy and the al breaks up into smaller particles.
,. ,
> .. . ea;
The Rayleigh iimit refers the maximum charge a material can
sustain before the electrostatic repulsion forces within the material exceed the surface
PCT/U82012/046838
tension holding the material together. Advantages of an atomization technique utilizing
the impingement of electrons on a al to set
up electrostatic charge repulsion with
the material include the capability to conduct the technique within a vacuum
environment. in this manner, al reactions between molten alloy material and the
atmosphere or an ing fluid can be limited or eliminated. This capability contrasts
with conventional fluid atomization, wherein the al being atomized necessarily
contacts an atomizing gas or liquid and is typically conducted in ambient air
or in inert
gas atmosphere.
A stream or ts of molten alloy atomized by an atomizing
assembly is produced by an upstream melting ly. A melting assembly may
e, for example, a dispenser that forms a suitable stream or droplets of molten
alloy. in various miting embodiments, a dispenser
may include a melt chamber
having an orifice. An example of such a dispenser is shown in US-6,772,96'l, hereby
incorporated by reference into this specification. A stream and/or droplets of molten
alloy are forced or othen/vise emerge from an orifice and pass downstream to an
atomizing assembly. In various non-limiting embodiments, a molten alloy stream or
droplets emerge from an orifice of a melt chamber under the influence of mechanical
action or pressure. In various non-limiting embodiments, pressure may be applied to
the molten alloy in a dispenser of a melting assembly at a ude greater than the
pressure at the e of the dispenser orifice to e molten alloy droplets at the
orifice in the dispenser. The pressure may be cycled or otherwise varied
so as to
selectively interrupt the flow of molten alloy streams and/or droplets.
Various non—limiting embodiments of a melting assembly
may be
designed to “pre-charge" a molten alloy stream or droplets that travel to an atomizing
assembly with a net negative charge. Pre—charging a stream or droplets may reduce
the amount of negative charge required from an electron beam atomizing ly
exceed the Rayleigh limitand atomize the stream ordroplets into r particles. A
melting assembly at a high negative potential relative to other elements of the overall
apparatus. This may be accomplished, for example, by electrically isolating a melting
~16-
WO 22552 2012/046838
assembly from other elements of the apparatus, and then raising the negative potential
of the melting assembly to a high level using a
power supply electrically coupled to the
melting assembly. Another non—limiting pre-charging technique is to position an
induction ring or plates upstream of an atomizing assembly in
a on close to an
outlet orifice of a g assembly. The ring or plates
may be configured to induce a
negative charge in the droplets or stream passing downstream to an atomizing
assembly. An atomizing assembly may then impinge electrons on the pre—charged
material to further negatively charge and atomize the material.
in various non—limiting embodiments, an atomizing assembly
comprise a thermo-ionic electron beam emitter or a like device. The thermo-ionic
emission phenomenon, also known as the "Edison effect," refers to the flow of ons
(referred to as "thermions") from a metallic e when l vibrational
energy
overcomes the electrostatic forces holding electrons to the surface. The effect
increases dramatically with increasing temperature, but is always present to
some
degree at temperatures above absolute zero. A thermo—ionic electron beam emitter
utilizes the thermo-ionic on enon to produce a stream of electrons
with a
d kinetic energy.
Thermo—ionic electron beam emitters generally comprise: (i) a
heated electron-producing filament; and (ii) an electron accelerating region, which is
d by a cathode and an anode. The filament typically consists of
a length of
refractory material wire, which is heated by passing an electric current h the
filament. Suitable thermo-ionic electron beam emitter filament materials generally have
the following properties: low potential barrier (work function); high melting point; stability
at high temperatures; low vapor re; and chemical stability. Various non—limiting
embodiments of thermo-ionic electron beam emitters include, for example,
tungsten,
lanthanum hexaboride (LaBs), or cerium hexaboride (CeBG) filaments.
in a thermo-ionic electron beam emitter, electrons "boil away" from
the surface of the filament upon application of sufficient thermal
energy produced by the
applied current. The electrons ed at the nt drift through a hole in
WO 22552 PCT/U82012/046838
cathode, and the electric field in the region n the vely-charged anode and
the negatively-charged cathode rates the electrons across the
gap to the anode,
where the electrons pass through a hole in the anode with a final
energy corresponding
to the applied voltage between the electrodes.
In order to negatively charge a molten alloy stream or droplets to a
level ary to overcome e n and atomize the material, the droplets or
stream must be subjected to a flow or field of electrons of sufficient
energy and intensity
for a finite period of time. An atomizing assembly may produce a three-dimensional
electron field, which extends a le distance along the path traveled by the ts
or stream through the atomizing assembly. A three—dimensional electron field, wherein
the electrons are spatially distributed, may be contrasted with a point source electron
beam emitter, wherein the electrons are focused in a narrow essentially two-
dimensional beam. A three-dimensional spatial bution of ing electrons
increases the impingement and charging efficiency and effectiveness of molten alloy
traveling through an atomizing assembly under the influence of gravity, for example.
Without intending to be bound by any particular , it is
believed that electron beam-atomized alloy particles may be formed from a molten
droplet or stream by one or both of the following mechanisms. In a first non-limiting
mechanism, atomized particles are sequentially stripped from the surface of a droplet or
stream as negative charge is added to the droplet or stream. In a second non-limiting
mechanism, atomized particles are formed by a cascading effect in which the initial
molten stream or droplet breaks up into small particles, the particles are recharged to
ve potential and break up into yet smailer particles, and the s repeats
during the time in which electrons are added to the successively smaller atomized
particles. Regardless of the physical atomization mechanism, molten alloy must be
exposed to an electron field for a sufficient time so that sufficient negative charge
accumulates in and disrupts the material.
A,“ —. raw“; :3; ~-
_.,. , “‘4
a. __.. .1. :5. . h.=~.—--
nus-t. »
‘ ,H. _; a r
A non-limiting spatial distribution of electrons within an electron field
produced in an atomizing assembly is in the form of a cylinder of electrons. The
PCT/U82012/046838
longitudinal axis of the er may be oriented in the general direction of travel of
molten alloy material through the atomizing assembly. The minimum length of the
cylinder (along the longitudinal axis) required for complete ation will depend on
the velocity of the molten alloy material traveling through the ation assembly and
the energy and intensity of the electron field within the assembly. Non-cylindrical
electron field shapes also may be used, such as, for example, fields having a transverse
cross-section (transverse to the molten alloy material's general direction of travel
through the atomizing ly) that is rectangular, triangular, or some other polygonal
or otherwise bounded shape. More generally, fields of any combination of
energy,
intensity, and three-dimensional shape capable of suitably atomizing molten alloy
material may be used. Van'ous non-limiting embodiments of an electron beam
atomizing assembly for an apparatus constructed ing to the present disclosure
are discussed below.
in various non-limiting ments, an atomizing ly
comprise a heated tungsten filament on source. Electrons thermo-ionically
emitted from a heated tungsten filament may be manipulated using ostatic and/or
electromagnetic fields to form a rectangular-shaped beam of electrons. The
rectangular-shaped beam may be ted into an ing chamber as a generally
block-shaped three-dimensional field across the path of travel of molten alloy material
through the atomizing assembly. Figure 2 schematically illustrates an atomizing
assembly 210 including a tungsten filament 212 that is heated by flow of current from a
power supply 214. The heated filament 212 produces free electrons 216. The
electrons 216 may be produced, for example, by a -ionic electron beam r.
The electrons 216 are shaped by an electrostatic field produced by
plates 220 to form a three-dimensional electron beam 222 having a generally
gular-shaped cross-section. The electron beam 222 is projected into the interior
of the atomizing assembly 210 to produce agenerally block-shaped three-dimensional
electron field 226. Molten alloydroplets 230 dispensed an the upstream melting
assembly 232 travel through the electron field 226 and are atomized to smaller particles
2012/046838
238 through disruption by accumulation of negative charge. The atomized particles 238
pass in the direction of arrow A toward a collector (not shown).
In various embodiments, atomizing assemblies may se
electron-producing devices other than or in addition to thermo—ionic electron beam
emitters. For example, in s embodiments, an atomizing assembly may se
a wire-discharge ion plasma electron emitter, also known as a cold cathode wire ion
generator and/or a plasma ion emitter. Wire-discharge ion plasma electron emitters
produce an electron field having a generally rectangular cross-section. One advantage
of a wire-discharge ion plasma electron emitter is that it produces an electron emission
at temperatures lower than a thermo-ionic electron emitter. Electrons ed by a
particular electron-producing device or devices within an ing assembly may be
suitably manipulated, for e, using electromagnetic and/or electrostatic fields, to
form a beam of electrons having a suitable cross—section. The electron beam may then
be projected into an atomizing chamber across the path of travel of molten alloy
material to be atomized.
Figure 3 illustrates another non-limiting embodiment of an
ing assembly 310. One or more tungsten filaments 312 are heated by power
supply 314 and e electrons 316 having sufficient energy to atomize molten alloy
when impinged on the molten alloy. The electrons may be produced, for example, by a
thermo-ionic electron beam emitter. The electrons 316 may be manipulated by
structures such as, for example, plates 320 to form a diffuse spot 322. A rastering
apparatus 324 rasters the electron spot 322 at a high raster rate within the region of the
atomizing assembly through which molten alloy material s, for example, under the
influence of gravity. The effect of the high raster rate is to provide a three—dimensional
electron field 326 having a lled shape in the atomizing chamber of the ing
assembly 310 that is configured to atomize the molten alloy droplets 330 received from
a melting assembly332 to smaller atomized particles 338 The atomized particles 338
k- ~—~-»~
wigs» 3‘erLVu‘»
pass in the direction of arrow A toward a collector (not shown)
PCT/U82012/046838
Referring to Figure 4, an atomizing assembly 410 produces an
electron field having a generally rectangular cross-section. The ons are produced
from the surface of a generally straight length of tungsten filament 412 heated by
power
supply 414. This method of producing electrons contrasts with the technique of
producing electrons from a point source, as is typically done in electron beam guns.
The electrons 416 emanating from the surface of the nt 412 may be manipulated
using electrostatic and/or electromagnetic fields, such as, for e, a field produced
by piates 420, to form a beam 422 having a generally rectangular cross—section. The
rectangular electron beam 422 may be rastered at a high raster rate by a rastering
tus into the atomizing assembly 410 to form an electron field through which
molten alloy material 430 travels when received from a melting assembly 432.
Alternatively, as shown in Figure 4, the rectangular electron beam
422 may be projected into the atomizing assembly 410 by a projecting device 424 to
form an electron field 426, having a generally rectangular cross section, through which
molten alloy material 430 travels when received from the melting ly 432. The
alloy material 430 is disrupted by accumulation of negative charge into ed
particles 438, which pass toward a collector (not shown) in the direction of arrow A.
in various embodiments, an atomizing assembly may comprise
multiple sources of electrons. An atomizing assembly may also comprise multiple
electron manipulating and projecting/rastering devices to e and control a suitable
on field. For example, a number of thermo-ionic or non-thermo—ionic electron
beam emitters or other electron sources may be oriented at specific angular positions
(for e, three emitters/sources at 120 s to one another) about the pathway
of molten alloy material in an atomizing chamber and produce a dimensional field
of electrons by projecting the electrons from the multiple sources into the y.
in various embodiments, components and es of the several
atomizing assemblyembodiments described above may be combined. For exampl “,- 7 “:34:
with reference to Figures 2 and 3, the rectangular beam 222 of the atomizing assembly
210 may be rastered using the rastering apparatus 324 in ing assembly 310 to
PCT/U52012/046838
e an electron field to atomize the molten alloy material. ve to electron spot
322, rastering the relatively high aspect ratio rectangular electron beam 222 may
provide a larger three—dimensional field disposed along the path of the molten alloy
material in the atomizing chamber.
ln various non-limiting embodiments of an electron beam atomizing
assembly, a first flow or stream of electrons may be impinged on molten alloy material
emerging from a melting assembly, y atomizing the ailoy material to primary
molten alloy particles having a first average size. ing a second stream of
ons on the y les may further atomize the particles to a smaller average
particle size. Further ions in average size may be achieved by impinging
onal electron flows or streams on the successively atomized particles. in this
manner, several size refinements are possible using rapid electrostatic charging by
impingement of electrons.
In various non-limiting embodiments, rapid electrostatic charging by
an electron beam is d two, three, or more times aiong a pathway to achieve a final
desired average molten alloy particle size. ln this manner, the original size of molten
alloy droplets produced by the melting assembly need not limit the size of the final
atomized particles produced in the atomizing assembly. The multiple electron sources
in such an ement may be, for example, individual thermo-ionic electron beam
emitters, cold cathode wire ion generators, and/or plasma ion emitters.
In various non—limiting embodiments of an ing assembly, a
droplet or a portion of a stream of molten alloy undergoes two or more stages of
atomization to successively reduce the average the size of the resulting atomized
particles. This may be accomplished, for example, by appropriately positioning two or
more electron guns or other sources of flows or streams of electrons along a pathway in
a region between the atomizing assembly and the collector. An atomizing assembly
having this general construction is schematically illustratedas assembiy 500 in Figure 5.
A melting assembly 512 includes a dispenser 514 that produces a molten alloy droplet
523a. The ser 514 may use, for example, mechanical devices, pressure, or
PCT/U82012/046838
gravity to produce the molten alloy droplet 523a from molten material produced from an
ingot, charge, scrap, and/or other source in the melting assembly 512.
Primary electron beam guns 524a produce streams of electrons
525a that impinge on droplet 523a and impart a negative charge to the droplet. The
electrostatic forces set up within the droplet 523a eventually exceed the droplet's
surface n, disrupting the droplet and g primary molten alloy particles 523b.
ary electron beam guns 524b focus streams of electrons 525b on primary
molten alloy particles 523b, similarly imparting negative charge to the particles and
disrupting them into smaller secondary molten alloy particles 523C. Tertiary electron
beam guns 524C focus s of electrons 5250 on secondary molten alloy particles
5230, also ing negative charge to the particles and disrupting them into yet
smaller tertiary molten alloy particles 523d. in a non-limiting embodiment of this
arrangement, the several electron beam guns are thermo-ionic electron beam guns,
although any other suitable device for producing suitable streams of electrons may be
used, such as, for e, a cold cathode wire ion generator and/or a plasma ion
As discussed in US-6,772,961, incorporated by reference herein,
"rapid" electrostatic charging refers to charging to a desired magnitude within 1 to 1000
microseconds, or any sub-range subsumed therein, such as, for example, 1 to 500
microseconds, 1 to 100 microseconds, or 1 to 50 microseconds. The rapid electrostatic
charging of molten alloy ed by a melting assembly produces charges exceeding
the Rayleigh limit of the material, and thereby produces a ity of smaller molten
alloy particles. The particles may have a lly uniform diameter of, for example, 5
to 5000 microns, or any sub—range subsumed therein, such as, for example 5 to 2500
microns or 5 to 250 microns.
An atomizing assembly es molten alloy particles, which are
" further processedto form a unitary and monolithic (i.e., ece) preform;aAs'used"'*-W " ' '
herein, the term rm" refers to a workpiece, ingot, or other article that is formed by
collecting together metallurgicaliy bonded solid alloy particles produced from atomized
PCT/U52012/046838
molten alloy particles. In the processes, systems, and tus described herein, all
or a portion of the molten alloy particles ed by the atomizing assembly are
controlled and solidified downstream of the atomizing assembly and collected as a
preform in a collector. For example, in various non—limiting embodiments, a system or
apparatus may include at least one field producing assembly that produces an
electrostatic field and/or an electromagnetic field that is at least partially present in a
region downstream of the atomizing ly. The electrostatic field and/or
omagnetic field produced by the field producing assembly may be structured
and/or manipulated so as to influence at least one of the acceleration, speed, and
direction of the molten alloy particles that interact with the field.
As used herein, the term "field producing assembly" refers to a
system or apparatus that es and, optionally, manipulates, one or more
electrostatic and/or electromagnetic fields that may be used to control at least one of the
acceleration, speed, and direction of molten and solidified alloy particles in a region
downstream of the atomizing assembly. Examples of field producing assemblies
suitable for use in the processes, systems, and apparatus described herein are
bed in US—6,772,961, which is incorporated by reference into this specification.
As used herein, the term "electrostatic field" can refer to a single
electrostatic field or a plurality of (two or more) electrostatic . An electrostatic field
may be produced, for example, by charging a point, plate, or other source to high
potential. Also as used herein, the term “electromagnetic field" can refer to a single
electromagnetic field or a plurality of electromagnetic fields. An electromagnetic field
may be created by, for example, passing electric current through a conductor, such as,
for example, a conductor coil.
in s non-limiting embodiments, a field ing assembly
es one or more electrostatic and/or omagnetic fields that interact with and
‘ t solid alloy particles to‘various'remu“
6‘ E‘fiéfiffifiififi preform at various times
during a forming process. The electrostatic and/or electromagnetic fields may also be
used to direct solid alloy particles to areas of a developing preform where it is desired to
PCT/U$2012/046838
add or remove heat, thereby influencing the macrostructure of the preform. In
conducting solid-spray-forming, the shape of the one or more electrostatic and/or
omagnetic fields can also be manipulated to produce near-net shape preforms by
directing particles to predetermined regions on the developing preform at various times
during the forming process. By employing one or more electrostatic and/or
electromagnetic fields using the field producing assembly, it is possible to enhance the
yield of the forming process, as well as e (and control) the density of the resulting
preform.
in various non-limiting ments, a field ing ly
produces an electrostatic field in a’region~ between an atomizing assembly and a
collector by electrically coupling the collector to a high voltage DC power supply and
grounding the ing assembly. Given that electron beam atomization may be used
in the processes, systems, and apparatus described herein, and given that the atomized
particles will be vely charged, a negative polarity is used so that the negatively
d atomized and solidified particles are repelled from the ing assembly and
attracted to the collector. An electrostatic field may interact with negatively charged
alloy particles produced by an atomizing assembly and the particles may be directed
under the influence of the field to move in the general direction of the electrostatic field
lines. This ction may be used to control one or more of the acceleration, speed,
and direction of the molten and solidified alloy particles toward the collector.
in addition to a high voltage DC power supply, a field producing
assembly may comprise one or more electrodes located at suitable positions and in
suitable orientations so as to produce suitable field(s) between an ing assembly
and a collector. The electrodes may be oned and configured to shape an
electrostatic field between an ing assembly and a collector in a desired manner.
An electrostatic field provided under the influence of the one or more electrodes can
have a shape that directs molten and soiidified alloy particleswin a desired manner to a
collector.
. PCT/U82012/046838
A field producing ly may also comprise a plurality of high
voltage DC power supplies, each operatively connected to one or more electrodes
disposed at suitable positions and in suitable orientations between an atomizing
assembly and a collector, and that influence the shape of an electrostatic field produced
by the field producing assembly n the ing assembly and the collector in a
time-dependent manner. in this manner, the field may be manipulated to suitably direct
alloy particles produced by the atomizing assembly to specific areas or locations on the
collector or on the developing preform over time.
For example, a field producing assembly including a plurality of
electrodes and associated power supplies
may be incorporated in a system or
tus configured to solid-spray-form near net shape solid articles having high
densities relative to preforms produced by conventional
spray forming and nucleated
casting ses. ln such embodiments, the electrostatic field
may be varied in terms
of strength and/or shape to suitably direct the solidified alloy particles to the collector.
In various miting embodiments, an electromagnetic field
be produced between an atomizing ly and a collector by
one or more magnetic
coils positioned intermediate the atomizing assembly and the tor. The
magnetic
coils may be electrically connected to a
power , which energizes the coils. Alloy
particles produced by an atomizing assembly may be directed along the field lines of the
omagnetic field to the collector. The position and/or orientation of the one or more
magnetic coils may be configured to direct the particles to specific areas or locations on
a collector or a developing preform. In this manner, alloy particles may be ed to
enhance the y of preforms or even produce near-net shape preforms during solid-
spray-forming.
in various non-limiting embodiments, a plurality of magnetic coils
may be positioned between an ing assembly and a collector. The
electromagnetic fields profdaseobbygthe'plurality of magnetic coils, which may be singly ”magmas
or multiply zed to different magnetic field intensities, influence the direction of
movement of the alloy particles produced by the atomizing assembly, directing the
PCT/U82012/046838
particles to specific predetermined areas or iocations on the collector or on a developing
preform. in this manner, the alloy particles can be directed in predetermined patterns to
e, for example, solid pretorms having near—net shape and/or relatively high
density.
In various non-limiting embodiments, the fields produced by a field
producing assembly may be used to improve or refine the ional control already
available through the use of translatable atomizing nozzles in an atomizing ly.
In various non-limiting embodiments, the substantial directional control attainable solely
by appropriately manipulating field shape, direction, and/or intensity, can ly
replace. the movement of atomizing nozzles in an atomizing assembly.
In various non-limiting embodiments, all or a portion of molten alloy
particles produced by an atomizing assembly and passing within or through fie|d(s)
produced by a field producing assembiy are collected on a collector as a solid preform.
As used , the term "collector" refers to a substrate, apparatus, element, or portion
or region of a substrate, apparatus, or element, or an assemblage of ts, that is
configured to receive all or a n of the fied alloy tes produced by cooling
of the molten alloy particles produced by an atomizing assembly. Non-limiting
examples of a collector that may be incorporated into embodiments of a system or
apparatus configured to m a solid-spray-forming process e the entirety or a
portion or region of a chamber, a mold, a platen, a mandrel, or other surface.
A collector may be held at ground ial or, in various non-
limiting embodiments, at a high positive potential so as to attract the negatively d
atomized particles produced by the atomizing assembly. The System illustrated in
Figure 1, 1.9., comprising a melting assembly, an atomizing assembly, a fieid producing
assembly, and a collector, may be configured and operated to soiid-spray-form an ingot
or other solid m on a surface of the collector, which in such case may be, for
exampie, a platen or a mandrel. in various spastimiting embodiments, a'systemrorv" -
apparatus configured to solid—spray—form an ingot or other m may comprise a
PCT/U52012/046838
collector sing a platen or a mandrel, which may be d to rotate or otherwise
translate to suitably form a solid e of the desired geometry.
in various non-limiting embodiments, overspray of solid alloy
particles is reduced or eliminated by suitably charging a tor. Atomizing a molten
stream and/or molten particles using an electron beam produces particles that are
negatively charged due to the excess of electrons within the atomized particles. By
suitably charging a collector to a positive ty, the collector will attract the particles
and thereby significantly reduce or eliminate overspray. Overspray is a problematic
ck of conventional spray g that can result in icantly compromised
process yields.
Figure 6 schematically illustrates various elements of a non-limiting
ment of an apparatus 600 configured to solid-spray-fonn a solid preform. An
electron beam atomizing assembly 610 produces negatively charged molten alloy
particles 612. An electrostatic field 614 is produced n the atomizing assembly
610 and a collector 616. The atomizing assembly 610 receives at least one of a stream
and a series of droplets of molten alloy from a melting assembly (not shown). The
charged molten alloy particles interact with the electrostatic field 614, which rates
the alloy particles 612 toward the collector 616. The molten alloy particles 612 are
solidified to form solid alloy particles while traveling from the atomizing assembly 610 to
the collector 616. The'solid alloy particles impact the collector 616 and form a solid
preform 618 on a surface of the collector 616. The field's influence on speed and/or
direction of the molten alloy particles 612 and, in turn, the solidified alloy particles,
be used to reduce or eliminate over-spray from the preform 618, thereby enhancing the
yield of the solid—spray-forming process, and possibly also increasing the density of the
preform 618 relative to a density possible without the use of a field producing assembly.
Figure 7 schematically illustrates various elements of a non-limiting
embodime‘ataoféanrapparatus'700 configured to perform asolid-spray-formingprams?“*“aw“
Melting assembly 710 supplies at least one of a stream and a series of ts of
molten alloy to electron beam atomizing assembly 712, which produces a
spray of
~28-
PCT/U82012/046838
negatively charged molten alloy particles 714. An electrostatic and/or electromagnetic
field 716 is produced by a field producing assembly n the atomizing assembly
712 and a suitably shaped collector 718. The field 716 interacts with the charged
molten alloy particles 714 to accelerate the particles 714 toward the collector 718. The
molten alloy particles 714 solidify and form solid alloy particles 715 while traveling from
the atomizing assembly 712 to the collector 718. The alloy particles 5
may be
acceierated to a greater extent if the collector 718 is held at a high ve potential.
The accelerating force and directional control exerted by the field 716
on the charged
particles 714/715 may be used to enhance the density of the solid preform 720, and
also may be utilized to e a near-net shape preform 720. The collector 718
be stationary, or may be adapted to rotate or othenNise ly translate. The solid
alloy les 715 impact the collector 718 and the developing preform 720, deform
upon impact, and metallurgicaliy bond together to form the solid m 720.
As shown in Figure 7A, an alternative non-limiting embodiment of
an apparatus 700 includes a non—equilibrium plasma—producing assembly configured to
e non-equilibrium plasma 722 in the path of the molten particles 714 between
two heat sink electrodes 724. The electrodes 724 thermally communicate with
outside thermal mass 726 by way of a dielectric liquid which circulates through conduit
728 under the influence of pumps 730. The thermal coupling between the heat sink
electrodes 724 and the outside thermal mass 726 by
way of the dielectric fluid allows
heat to be removed from the molten particles 714 and communicated to the l
mass 726. The non-equilibrium plasma 722 between the heat sinks 724
may be
produced, for example, by means of an AC glow discharge or a corona discharge. The
non-equilibrium plasma 722 transfers heat from the molten particles 714 to the two heat
sink electrodes 724, which transfer the heat to the e thermal
mass 726. The
removal of heat from the molten alloy particles 714 allows the particles to solidify and
form solid alloy particles 715.
:‘fiw‘u‘w:2; -
Heattransfer systemsand devices that produce uiiibrium
plasma to transfer heat to or from atomized molten alloy particles are describedIn US-
6,772,961, which is incorporated by reference into this specification. Heat transfer
PCT/U520121046838
systems and s that produce non-equilibrium plasma to transfer heat to or from
alloy materials are also described in US. Patent No. 7,114,548, which is hereby
incorporated by reference into this specification.
Figure 8 schematically illustrates various elements of a non-limiting
embodiment of an apparatus 800 configured to perform a solid-spray-forming
process.
Melting assembly 810 provides at least one of a flow and a series of droplets of a
molten alloy to an electron beam atomizing assembly 812. The melting assembly 810
optionally may be held at a high negative potential, such as by optional power supply
822, so as to negatively harge" the molten material before it passes to the
atomizing assembly 812, y reducing the amount of negative charge that the
atomizing assembly 812 must convey to the molten material to atomize the material.
This harging“ feature also may be used with the other embodiments described
herein to reduce the amount of negative charge that must be added to the molten
material to atomize the material in the atomizing assembly.
The electron beam atomizing ly 812 produces a
spray of
charged molten alloy particles 814. An electromagnetic field 816 is produced by a
magnetic coil 818 (shown sectioned). The charged molten alloy particles 814 interact
with the field 816 and are thereby directed toward a collector 820. The molten alloy
particles 814 solidify and form solid alloy particles 815 while traveling from the atomizing
assembly 812 to the tor 820. The directional control of the alloy particles 814/815
exerted by field 816 can reduce over-spray, thereby enhancing yield of the solid—spray—
torming process, and also can enhance the density of the solid preform 822. The sold
alloy particles 815 impact the collector 820 and the developing preform 822, deform
upon impact, and metallurgically bond together to form the solid m 822.
As shown in Figure 8A, non-equilibrium plasma 842 optionally may
be ed in the path of the alloy les 814/815 between two heat sink electrodes
~ Ft:=~::-£i'844;-Whl0h‘are thermally connected to an outside thermal mass 84Gbyf-a die’lectritfii‘quid‘ '
that is ated through ts 848 by pumps 850. The thermal communication
maintained between the heat sink odes 844 and the outside thermal mass 846
PCT/U52012/046838
allows heat to be removed from or added to the alloy particles 5. The
non-
equilibrium plasma 842 n the heat sink electrodes 844 may be produced, for
example, by an AC glow discharge or a corona discharge.
The non-equilibrium plasma 842 may also extend from the heat
sink electrodes 844 to the solid preform 822 and the collector 820, providing for heat
removal from or heat addition to the preform 822 and the collector 820. Accordingly, in
apparatus 800, heat may transferred from the molten alloy particles 814, solid alloy
particles 815, the solid m 822, and the tor 820 by the non-equilibrium
plasma 842 to the heat sink electrodes 844, and then to the outside thermal mass 846.
The removal of heat from the molten alloy les 814 allows the particles to solidify
and form the solid alloy particles 815.
Figure 9 schematically illustrates various elements of a non—limiting
embodiment of an apparatus 900 configured to pen‘orm a solid—spray—fonning
process.
Melting ly 910 provides at least one of a stream and a series of droplets of a
molten alloy to an electron beam atomizing assembly 912. Atomizing assembly 912
produces charged molten alloy particles 914. Electromagnetic field 916 produced by a
magnetic coil 918 (shown sectioned) interacts with the charged molten alloy particles
914 to spread out the particles 914 and reduce the probability of their collision, thereby
ting formation of larger molten particles and, consequently, larger solid alloy
particles 942. A second electromagnetic field 940 produced by a magnetic coil 943
(shown ned) interacts with and directs the solidified particles 942 toward a
collector 944. A solid preform 946 is formed on the collector 944 by impacting the solid
alloy particles 942 onto the collector 944 and into the preform 946, wherein the solid
alloy les 942 deform upon impact and metallurgically bond together to form the
solid preform 946.
As shown in Figure 9A, a non-limiting embodiment of an apparatus
900 may figured‘so'thatnon-equilibrium plasma 922 is created in the path of the twat-er “Lisa‘s
molten particles 914, between two heat sink electrodes 924 that thermally communicate
with an outside thermal mass 926 by a dielectric fluid that circulates through conduit 928
WO 22552 ‘ PCT/U52012/046838
by way of the pumps 930. The arrangement of the heat sink odes 924 thermally
communicating with outside thermal mass 926 allows heat to be removed from the
molten alloy particles 914 to solidify the molten alloy particles and form the solid alloy
particles 942.
In various non-limiting embodiments, an apparatus or system
configured to perform a spray-torming process may include a chamber or the like
that encloses or ns all or a portion of the melting ly, atomizing assembly,
field producing assembly, plasma producing assembly, collector, and/or ece (e.g.,
preform). If, for example, a heat transfer device employing non-equilibrium plasma is
incorporated in an apparatus or system, all or a portion of the heat transfer device and
its associated odes, as well as the non-equilibrium plasma, also
may be
encompassed within the chamber. Such a chamber can be ed to allow for
regulating the atmosphere within the chamber, including the species and partial
pressures of gases present and/or the overall gas pressure within the chamber.
For example, the chamber may be ted to provide a vacuum
(as used herein, “vacuum" refers to a complete or partial vacuum) and/or may be
completely or partially filled with an inert gas (e.g., argon and/or nitrogen) to limit
oxidation of the materials being processed and/or to inhibit other undesired chemical
reactions, such as nitridation. in a non-limiting embodiment of an apparatus
incorporating a chamber, the pressure within the chamber may be maintained at less
than atmospheric pressure, such as from 0.1 to 0.0001 torr, or any sub-range
subsumed therein, such as, for example from 0.01 to 0.001 torr.
Molten alloy particles produced by impinging electrons on molten
material, as bed in this specification, generally are highly negatively charged.
Various non-limiting embodiments described herein also include devices to pre-charge
molten material with a ve charge, before impinging electrons on and atomizing the
ten~material. There-may exist a tendencyfonthemgativelychargedM
les/material to accelerate toward nearby structures held at ground potential. Such
structures may include chamber walls and other apparatus components adjacent the
PCT/U82012/046838
molten al’s path of travel downstream of the melting assembly. in s non-
limiting embodiments, the atomizing assembly of the apparatus includes plates or other
suitably—shaped structures held at negative potential and disposed so as to deflect
vely charged particles/material and inhibit undesirable acceleration of the
particles/material toward the chamber walls and/or other structures held at ground
potential.
Various non—limiting ments of an apparatus or system
configured to perform a solid-spray—forming process may include a melting assembly
substantially free from ceramic in regions that would contact, and therefore could
contaminate, molten alloy produced by the g assembly during operation of the
apparatus. Each such apparatus may also include an electron beam atomizing
assembly to e the molten material and produce molten alloy particles. Each such
apparatus may also include a field producing assembly, which produces one or more
electromagnetic and/or electrostatic fields between the atomizing ly and a
collector and influences at least one of the acceleration, speed, and direction of the
particles as they traverse all or a portion of the distance between the atomizing
assembly and the collector.
Various non—limiting embodiments of an apparatus or system
configured to perform a spray—forming s may include one or more non-
equilibrium plasma producing lies that e non-equilibrium plasma for
transferring heat to or from the molten and/or solid alloy particles after they are
produced by an atomizing assembly, but before the solid particles impact a
collector/developing workpiece to form a solid preform. atively, or in addition,
non-limiting embodiments of an apparatus ured to perform a solid—spray-forming
process may produce one or more non—equilibrium plasmas to transfer heat to or from
solid alloy material after it impacts a collector and may be applied to a preform
developing on or in the collector.
.-_v-. WL;7‘;;Z r41“
~ 7; *zifg—v'
new“. ,7
Figures 10-13 schematically illustrate various non—limiting
embodiments of melting assemblies that may be included as a component of an
PCT/U52012/046838
apparatus or system configured to perform a solid-spray—forming process. Each such
melting assembly embodiment may be used to produce at least one of a stream and a
series of droplets of molten alloy from a consumable electrode or other alloy feedstock.
Each such melting assembly embodiment below may be constructed so that it lacks
ceramic in regions of the assembly that would be ted by the molten alloy
produced in the assembly.
Figure 10 illustrates the use of a vacuum —electrode
remelting device as a component of a melting assembly producing molten alloy that is
fed to an electron beam atomizing assembly. The vacuum double-electrode remelting,
or "VADER," technique is described, for e, in U.S. Patent No. 4,261,412, which
is hereby incorporated by reference into this specification. In a VADER apparatus,
molten material is produced by striking an arc in a vacuum between two consumable
electrodes, which melt. An advantage of the VADER technique over conventional
vacuum arc remelting (VAR) is that the VADER technique allows fortighter control of
temperature and melting rate.
With reference to Figure 10, vacuum chamber well 1010 surrounds
the d able electrodes 1014 and an atomizing assembly 1016. Electric
current passes between and h the opposed electrodes 1014, melting the
odes to produce droplets 1018 (or, alternatively, a stream) of molten alloy. The
molten alloy droplets 1018 fall from the electrodes 1014 to the atomizing assembly
1016. Alternatively, a melt pool in fluid communication with a cold ion guide or
like dispensing device (not shown) may be oned between the electrodes 1014 and
the atomizing assembly 1016. The ed molten alloy particles produced by the
atomizing assembly 1016 pass through and are influenced by one or more
electromagnetic and/or electrostatic fields produced by a field ing ly (not
shown), solidify, impact onto a collector or a developing workpiece (not shown),
metallurgically bond together, and form a solid preform.
~sfiflwwfimfi~ ”
Figure 11 illustrates use of an electron beam melting device as a
component of a melting assembly producing molten alloy that is fed to an electron beam
PCT/U82012/046838
atomizing ly. ln electron beam melting, a feedstock is melted by impinging high-
energy electrons on the feedstock. Contamination of the molten product may be
reduced or eliminated by melting in a controlled vacuum. The energy efficiency of
electron beam melting can exceed that of competing ses because of the
available control of the electron beam spot dwell time and distribution to the
areas to be
melted. Also, power losses of the electron beam inside the gun and between the gun
nozzle and the target material are relatively small.
As discussed above, the melting devices described herein,
ing the melting device shown in Figure 11, for example, may be configured to be
maintained at a high negative potential and thereby impart a negative charge to the
molten al before it passes downstream to the atomizing assembly of the
apparatus. As an example, the melting device shown in Figure 11 may be configured to
e a melt chamber that is electrically conductive and maintained at
a high negative
ial, and which the molten material contacts before passing to the atomizing
assembly.
Referring to Figure 11, vacuum chamber 1110 nds the
melting device’s electron beam sources 1112, the consumable ode 1114 that is
being , an on beam atomizing assembly 1116, and a collector (not shown).
The electron beams impact the electrode 1114, g and melting the electrode to
produce droplets 1118 (or, alternatively, a stream) of molten alloy. The droplets 1118
fall from the electrode 1114 to the atomizing assembly 1116. The atomized molten alloy
les produced by the atomizing assembly 1116 pass through and are nced by
one or more electromagnetic and/or electrostatic fields produced by a field producing
assembly (not shown), solidify, impact onto a collector or a developing workpiece (not
shown), metallurgically bond together, and form a solid preform.
Figure 12 illustrates use of an electron beam cold hearth melting
a:arer~=““"~>'*‘*"deviC'e as a component of a melting assembly producing motten’—“altoythat’is‘ted to an“
electron beam atomizing assembly. in a typical electron beam cold hearth melting
technique, a first electron beam gun melts the charge, which can have a variety of forms
PCT/U82012/046838
(9.9., ingot, sponge, or scrap). The molten material flows into a shallow water-cooled
crucible (the cold hearth), where one or more electron
guns in the temperature of
the molten material. A major function of the cold hearth is to separate inclusions lighter
or heavier than the liquid material, while at the same time increasing the residence time
of lower density les that have a high melting point in order to
ensure their complete
dissolution. All of the operations may be ted in a vacuum environment to
ensure
proper operation of the electron guns and to avoid alloy contamination by the t
environment. An advantage of the electron beam cold hearth melting technique is that it
may effectively eliminate volatile elements, such as chloride and hydrogen (due in part
to the optional vacuum), and inclusions in the melt. The que is also flexible with
respect to the form of the feed materials.
Referring to Figure 12, vacuum chamber 1210 nds the
electron beam sources 1212 and a water-cooled
copper cold hearth 1216 of the melting
assembly, the consumable electrode 1214 that is being melted, an electron beam
atomizing assembly 1218, and a collector (not shown). Molten al 1220, in the
form of a stream and/or a series of droplets, falls from the water-cooled
copper cold
hearth 1216 to the atomizing assembly 1218. The atomized molten alloy particles
produced by the atomizing assembly 1218 pass through and are influenced by one or
more electromagnetic and/or electrostatic fields produced by a field producing assembly
(not shown), solidify, impact onto a collector or a developing ece (not shown),
urgically bond together, and form a solid preform.
Figure 13 illustrates use of a melting assembly comprising a
combination of an electrosiag refining/remelting (ESR) device and a cold induction
guide (ClG) to produce molten alloy that is fed to an electron beam atomizing assembly.
atively, a melting device combining vacuum arc remelting (VAR) and a CIG may
be used in place of an ESR/CIG combination. Devices combining ESR or VAR devices
and a ClG are described, for example, in US. Patent No. 5,325,906, which is hereby
incorporated by referenceéihtohthis specification. '
PCT/U82012/046838
in a typical ESR technique, electric current is passed through a
consumable electrode and an electrically conductive slag disposed within a refining
vessel and in contact with the ode. Droplets melted from the ode pass
through and are refined by the conductive slag, and may then be passed to a
downstream apparatus. The basic components of an ESR apparatus include a
_ power
supply, an electrode feed mechanism, a water cooled copper refining vessel, and the
slag. The specific slag type used will depend on the ular material being refined.
The VAR process involves the melting of a consumable electrode composed of the alloy
by striking an arc with the electrode in a vacuum. in addition to reducing dissolved
nitrogen and hydrogen, the VAR process removes many oxide inclusions in the arc—
plasma.
in the ESR/CIG and VAR/ClG ations, the ClG, which is also
variously referred to a "cold finger" or “cold wall induction guide," can maintain the
molten material in molten form as the al passes from the VAR or ESR apparatus
downstream to the atomizing assembly. The 016 also protects the molten material from
contact with the atmosphere. The CIG may be directly coupled am to the ESR
VAR apparatus and downstream to the atomizing assembly to protect the d
molten al from the here, preventing oxides from g in and
contaminating the melt. A ClG also may be used to control the flow of molten material
from an ESR or VAR apparatus to a downstream atomizing assembly.
The construction and manner of operation of CIG devices is
bed, for example, in U.S. Pat. Nos. 5,272,718; 5,310,165; 5,348,566; and
,769,151, which are hereby incorporated by reference into this specification. A CIG
lly includes a melt container for receiving molten material. The melt container
includes a bottom wall containing an aperture. A transfer region of the ClG is
configured to include a passage (which may be, for example, generally funnel—shaped)
constructed to receive molten material from the re in the melt container in one
v_~=mm—v**-»~'~
conventional design of a ClG, the wall of the funnelshaped
passage is defined by a
number of fluid-cooled metallic segments, and the fluid—cooled segments define an inner
contour of the passage that may generally decrease in cross-sectional area from
PCT/U82012/046838
inlet end to an outiet end of the region. One or more electrically conductive coils are
associated with the wall of the funnel-shaped passage, and a source of electrical
current is in selective electrical tion with the conductive coils. During the time
that the molten material is flowing from the melt container of the ClG through the
passage of the ClG, electrical current is passed through the conductive coils at an
intensity sufficient to inductively heat the molten material and maintain it in molten form.
A portion of the molten material contacts the cooled wall of the
funnel-shaped passage of the ClG and may solidity to form a skull that insulates the
remainder of the molten material flowing through the ClG from contacting the wall. The
cooling of the wall and the formation of the skull assures that the molten material
g through the ClG is not contaminated by the metals or other constituents from
which the inner walls of the ClG are formed. As disclosed, for example, in US Pat. No.
,649,992, the thickness of the skull at a region of the —shaped portion of the ClG
may be controlled by appropriately ing the temperature of the coolant, the flow
rate of the coolant, and/or the intensity of the current in the ion coils to l or
entirely shut off the flow of the melt though the ClG; as the ess of the skull
increases, the flow through the transfer region is correspondingly reduced. Although a
ClG apparatus may be ed in various forms, each lly includes: (1) a passage
utilizing gravity to guide a melt; (2) cooling means in at least a region of the wall to
promote skull ion on the wall; and (3) electrically tive coils associated with
at least a portion of the passage, for inductively heating molten material within the
passage.
Referring to Figure 13, vacuum chamber 1310 surrounds an
G melting assembly, an electron beam atomizing assembly 1312, and a
collector (not shown). The ESR/CIG melt source includes a consumable electrode 1314
of the desired alloy and a water-cooled copper crucible 1316. A heated molten slag
1318 acts to melt the electrode 1314 to torm a molten alloy pooi 1320 The molten alloy
fromthemoltenpooi 1320 flows through the ClG nozzle 1324, I 7
in the form otamolten“
stream and/or a series of droplets 1322, and passes to the atomizing assembly 1312.
The atomized molten alloy particles produced 'by the atomizing assembly 1312 pass
W0 2013/022552 2012/046838
h and are influenced by one or more electromagnetic and/or eiectrostatic fields
produced by a field producing assembly (not shown), ty, impact onto a collector or
a developing workpiece (not shown), metallurgically bond together, and form a solid
preform.
Alternative techniques for melting feedstock in a melting assembly
of an apparatus or system configured to perform a solid-spray-torming
process include,
but are not limited to, ion melting, plasma arc melting, and the like. For e,
in induction melting, a coiled primary electrical conductor
may surround a bar of metallic
feed material. By passing electrical current through the y tor a secondary
electric current is induced within thebar through electromagnetic induction. The
secondary current heats the bar to a ature greater than its melting temperature.
Figures 14-17 illustrate various non-limiting embodiments of
systems and apparatus configured to perform a solid—spray—forming process.
Figure 14 schematically illustrates atomized and solidified alloy
particles being impacted and metallurgically bonded onto a deveioping workpiece to
form a solid preform. A vacuum chamber 1410 es an electron beam atomizing
assembly 1412. A series of droplets of molten alloy 1414 produced by a melting
assembly (not shown), which may be, for example, one of the s melting
assemblies discussed above, passes into the atomizing ly 1412. The atomizing
assembly 1412 produces atomized alloy particles 1416, which pass h, interact
with, and are influenced by the electromagnetic and/or electrostatic field(s) 1413
ed by electromagnetic coil 1417 (shown sectioned) of a field producing
assembly. The coil 1417 is positioned to produce the field(s) in the region 1418
downstream of the atomizing assembly 1412. The atomized alioy particles 1416 solidify
while traveling from the atomizing assembly 1412, impact, and metallurgically bond to
the developing workpiece to form a solid preform.
. “hwy“;ua; .3
Figure;1_75 tically illustrates the production of a solid—spray-
formed ingot from an ed molten and solidified alioy produced by electron beam
atomization. Vacuum chamber 1510 encloses a melting assembly (not shown) and an
electron beam atomizing assembly 1512. The melting assembly
may be, for example,
one of the various melting assemblies discussed above. Droplets of molten alloy 1514
produced by the melting assembly (not shown) pass into the atomizing assembly 1512.
The droplets of molten alloy 1514 are atomized within the ing ly 1512 to
form a spray of atomized alloy les 1516.
The atomized alloy les 1516 pass through, interact with, and
are influenced by one or more omagnetic and/or electrostatic fields (not ted)
produced by plates 1518 of a field producing assembly. The plates 1518 are connected
to a power source (not shown) by wires 1520 passing through the walls of the r
1510. The atomized alloy particles 1516 solidify and are ed onto a rotating
collector plate 1524 under influence of the field(s) produced by the field producing
ly to form a solid preform 1525. The rotating collector plate 1524 can be
withdrawn downwardly at a rate that maintains the deposition interface at a substantially
constant distance from the atomizing assembly. To enhance yield and improve
deposition density, the collector plate 1524 may be charged to a high positive potential
by connecting the plate 1524 to a power supply (not shown) by wires 1526 passing
h the wall of the chamber 1510.
Figure 16 schematically illustrates an embodiment of an apparatus
or system configured to perform a solid—spray—fonning process wherein atomized molten
alloy particles are solidified and impact a collector/workpiece in a first chamber of the
apparatus. Vacuum chamber 1610 encloses a melting assembly (not shown) and an
electron beam atomizing assembly 1612. The melting assembly may be, for example,
one of the various melting assemblies discussed above. A series of droplets of molten
alloy 1614 produced by the melting assembly (not shown) pass into the atomizing
assembly 1612. The droplets of molten alloy 1614 are atomized within the atomizing
assembly 1612 to form alloy particles 1616 The alloy particles 1616 pass through,
interact with, and are nced by one or more electromagnetic and/or electrostatic
. ”7“ egg?15’'fla. _._ as.
g“. fields1618 produced by electromagnetic coil 1620 (shown sectioned)dialfields—we
producing assembly. The ed particles 1616 solidify and are directed into a
collector in the form of a container 1621 under influence of the field 1618.
W0 2013/022552 PCT/U82012/046838
The solid alloy particies impact a ece 1625 g in the
container 1621, deform, and metallurgically bond to the workpiece 1625 to form a solid
preform. When the solid preform is formed, it may transferred into a chamber 1626,
which may be sealed by vacuum lock 1628. The container 1621 and preform may be
released to the atmosphere via a second vacuum lock 1630 for thermomechanical
processing according to known techniques. Optionally, the apparatus of may
include a heat transfer device, such as is generally described above, configured to
remove heat from the atomized molten alloy les to form solid alloy particles. Also,
optionally, the container 1621 may be electrically connected to a power supply 1624 by
wire 1622 and is held at a positive potential while the negatively charged solid particles
1616 are impacting in the container 1621. The wire 1622 may be remotely
disconnected from the container 1621 before the container is moved into r
1626.
Figure 17 schematically illustrates a non-limiting embodiment of an
apparatus or system 1700 configured to perform a solid-spray-forming process. In
Figure 17 a solid-spray—formed article is produced in a mold by spraying solid alloy
les produced by solidifying molten alloy les provided by electron beam
ation. Vacuum chamber 1710 encloses elements including a melting assembly
(not shown) and an electron beam atomizing assembly 1712. The melting assembly
may be, for example, one of the various g assemblies sed above. A series
of droplets of molten alloy 1714 producedby the melting assembly pass into the
atomizing assembly 1712. The droplets of molten alloy 1714 are atomized within the
atomizing ly 1712 to form a spray of atomized alloy particles 1716. The
atomized alioy particles 1716 pass through, interact with, and are influenced by the one
or more electromagnetic and/0r electrostatic fields 1718 produced by the electrically
energized coil 1720 (shown sectioned) of a field ing assembly. The atomized
al 1716 solidifies and is directed into mold 1724 under influence of the field 1718
produced by the, field producing assembly, and the resulting solid-spray—formed article (2,—2.2.
1730 is withdrawn from the mold 1724 by downward movement of the mold base (not
shown). Optionally, the mold base may be configured to rotate or othenNise translate.
PCT/U52012/046838
in an alternative non-limiting embodiment of apparatus 1700 shown
in Figure 17A, power supplies 1732 are ed and create a potential difference
so as
to form a non—equilibrium plasma between the electrodes 1734. Heat is conducted by
the plasma from the solidifying alloy particles and/or the surface of the solid article 1730
to the electrodes 1734, which are cooled with a dielectric liquid that circulates through
heat exchangers 1736 and the electrodes 1734.
Figure 18 illustrates a non—limiting embodiment of a spray-
forming process that may be med using the systems and apparatus described
herein. An alloy feedstock 1801 is melted in a melting step 1805 to produce at least
one of a stream of molten alloy and a series of droplets of molten alloy. The g
step 1805 may e multiple successive melting, refining, and re-melting sub-steps.
For example, the alloy feedstock may comprise
scrap, sponge, recycled, and/or virgin
sources of base metal and ng ts, as applicable, which are melted down to
form an initial melt. The initial melt may be produced using VAR, plasma arc melting,
electron beam melting, Or any other suitable g technique.
The initial melt chemistry may be analyzed and modified as
necessary to achieve a predetermined chemistry. Once acceptable melt chemistry is
ed, the melt may be cast into a consumable electrode for further ng and/or
remelting operations or used to produce at least one of a stream of molten alloy and a
series of droplets of molten alloy. in various embodiments, the alloy feedstock
se a consumable electrode or other consumable article of acceptable alloy
chemistry that is melted to produce at least one of a stream of molten alloy and a series
of droplets of molten alloy.
As noted above, as used herein, the term "alloy" refers both to
pure
metals and to alloys and includes, for e, iron, cobalt, nickel, aluminum, titanium,
niobium, zirconium, and alloys based on any of these metals, such as stainless steels,
nickel-basesuperalloys, cobalt-base superalloys:fitaniun'ratuminide‘s, nickel-titanium:
alloys, and the like. Non-limiting examples of nickel-base superalloys that may be
processed according to embodiments described herein include, but are not limited to, W
PCT/U82012/046838
100 alloy (UNS 13100), Rene 88TM atloy, Alloy 720, Alloy,718 (UNS ), and
718PlusTM alloy (UNS N07818) (available from ATl Allvac, Monroe, North Carolina,
USA). Non-limiting examples of titanium alloys that may be processed according to
ments described herein include, but are not limited to, -4V alloy, T—17
alloy, Ti—55-3 alloy, Ti—Ni alloys, and Ti-Al alloys.
At least one of a stream of molten alloy and a series of droplets of
molten alloy is atomized in step 1810 using electron beam atomization. During step
1810, electrons ed from an electron source, such as, for e, a thermo—ionic
on beam r and/or a wire—discharge ion plasma electron emitter, are
impinged on the least one of a stream of molten alloy and a series of droplets of molten
alloy. The ing electrons rapidly electrostatically charge the stream of molten alloy
and/or the series of droplets of molten alloy until the electrostatic repulsion forces
exceed the e tension of the molten alloy and physically break the stream and/or
droplets into smaller molten alloy particles, thereby atomizing the molten alloy. The
impinging electrons also produce electrically-charged atomized particles of molten alloy.
The size and charge of the atomized molten alloy particles
may be controlled, for
example, by controlling the size, shape, and y of the field of electrons that impinge
on the molten alloy.
The atomized and electrically-charged particles of molten alloy are
. accelerated in step 1815 through interaction with at least one of an electrostatic field
and an electromagnetic field. in various embodiments, an electrostatic field established
between an atomizing assembly and a collector interacts with the atomized and
electrically-charged and alloy particles to accelerate the particles away from the
atomizing assembly and toward a collector. The magnitude of the acceleration may be
controlled, for example, by controlling the magnitude of a voltage difference between an
atomizing assembly and a collector, which directly affects the electrostatic field intensity.
‘ ~‘
~ [00135] The accelerating molten alloy particles are solidified "instep 1820‘ by '
cooling the molten alloy particles to a temperature no greater than the solidus
temperature of the alloy. As used herein, the term "solidus temperature" refers to the
_43_
PCT/U82012/046838
maximum temperature of an alloy at which the alloy is in a completely solid state. in
st, the “liquidus temperature" of an alloy is the maximum temperature at which
solid crystals of the alloy coexist in thermodynamic equilibrium with liquid alloy. At
temperatures above the liquidus temperature, an alloy is completely liquid, and at
temperatures equal to or below the s temperature, an alloy is completely solid. At
temperatures greater than the solid temperature and up to and including the liquidus
temperature, an alloy exists in a two—phase state.
] The cooling of the accelerating alloy particles to a temperature no
greater than the solidus temperature of the alloy ensures that the alloy changes from
the molten state to the solid state before coming into t with a tor. For
example, Alloy 718, a nickel-base lloy, has a liquidus temperature of
approximately 1358°C, and a s temperature of approximately 1214°C. See Wei-
Di Cao, "Solidification and solid state phase transformation of Allvac® 718PlusTM alloy,"
Journal of the Minerals, Metals & Materials Society, 2005, which is incorporated by
reference into this specification. Therefore, in non—limiting embodiments wherein Alloy
718 is solid-spray—formed, the accelerating molten Alloy 718 particles may be cooled to
a temperature no greater than 1214°C to solidify the particles before coming into
contact with a tor.
In various embodiments, accelerating molten alloy particles are
cooled to a temperature no r than the solidus temperature (T3) of the alloy and
greater than 0.50 times the solidus ature (0.50*Ts). Cooling molten alloy
particles to a temperature in the range of 0.50*Ts to Ts may ensure that the particles are
substantially solidified but sufficiently soft to deform upon impact with a substrate and
metallurgically bond in the solid state He, solid state weld) to form a unitary and
monolithic solid preform. For example, the ultimate strength, 2% yield strength, and
ss of Alloy 718 decreases (i.e., the alloy softens) at a higher rate at temperatures
above approximately60090, which is approximately 0.50 times the solidus temperature
—»—--— ‘__.c
-\_ '37:?"ng , _
of the alloy.
W0 2013/022552 PCT/U82012/046838
£00138] in various embodiments, accelerating molten alloy particles are
cooled to a temperature in the range of 0.50*Ts to T5, or any sub—range subsumed
therein, such as, for example, O.50*Ts to 0.99*Ts, 0.50*Ts to O.95*Ts, O.60*Ts to
O.95*T5, O.70*Ts to O.95*Ts, 0.80*TS to O.95*TS, or 0.90*Ts to 0.99*Ts.
in various embodiments, the distance n an atomizing
assembly and a collector, through which molten alloy particles are accelerated, is
predetermined so that the molten alloy particles lose sufficient heat energy h
conduction, convention, and/or radiation to solidify the particles before contacting a
collector. ln various embodiments, a non—equilibrium plasma is produced in the
pathway of accelerating molten alloy particles to actively transfer heat energy from the
molten particles to solidify the particles before contacting a collector.
in various embodiments, accelerating molten alloy particles travel
through a thermal control zone in an apparatus or system configured to perform a solidspray
~forming process. A thermal control zone may comprise heat transfer devices to
actively remove heat from alloy les or to increase the rate of heat loss by way of
conduction, convention, and/or radiation to the nding environment in the thermal
control zone. For example, a thermal control zone may comprise devices such as
cooling coils to maintain a sub-ambient temperature in the thermal control zone, which
ishes a greater temperature differential between the molten alloy particles and the
nding environment. A greater temperature differential may ate with a higher
rate of heat loss from the molten alloy particles, which allows for more effective and/or
efficient solidification before contacting a collector.
] The solid alloy les are impacted onto a substrate at step 1825
to solid-spray-form an alloy m 1830. In various embodiments, the ate may
comprise a collector such as, for example, a platen, a cylinder, a l, a container, a
chamber, a mold, or other surface. In various embodiments, the substrate may
se a developing workpiece or preform that was formed from solid alloy particles
that ed onto an initial collector surface. in this manner, the impacting solid alloy
particles further develop the workpiece and form the preform.
PCT/U52012/046838
In various embodiments, solid alloy particles impact a substrate
after being cooled to a temperature no r than the soiidus temperature of the alloy,
such as, for example, a ature in the range of 0.50*Ts to T3, or
any sub-range
subsumed therein. Impacting solid alloy particles having a temperature no greaterthan
the solidus temperature of the alloy, for example, a temperature in the
range of 0.50*Ts
to Ts, may ensure that the particles are substantially solidified but iently soft to
deform upon impact with the substrate and metallurgically bond in the solid state (i.e.,
solid state weld) to form a unitary and monolithic solid preform.
in various embodiments, the initial collector may comprise a solid
e formed from the same or a similar alloy as the alloy forming the atomized and
solidified particles. This may ensure that the impacting solid alloy particles are
urgically compatible with the initial collector so that the solid alloy particles
metallurgically bond (1.9., solid state weld) to the substrate, and to each other, to form a
unitary and thic preform. In various embodiments, the material forming the initial
collector may be removed from a solid-spray—formed alloy preform by cutting, grinding,
or the like.
s 19A-19F collectively illustrate a miting embodiment of
a solid—spray-forming process and system 1900. Referring to Figure 19A, an alloy
melting apparatus 1910 produces a series of droplets 1915 of molten alloy, however, it
is understood that the alloy melting apparatus 1910
may produce a stream of molten
alloy and/or a series of droplets of molten alloy. An atomizing apparatus 1920 produces
a field of electrons 1925 that intersects the pathway of the molten alloy droplets 1915
traveling through the spray-forming system 1900 from the melting apparatus 1910
toward a substrate 1930.
Referring to Figure 198, the electrons comprising the field of
electrons 1925 impinge on the molten alloy ts 1915 and rapidly electrostatically
charge the tsz19.1-5beyondithe Rayleigh limit and the droplets e into
smaller molten alloy particles 1935. The atomized molten alloy particles 1985 have
net negative electrical charged due to the impinging electrons. The atomized molten
ZOIZ/046838
alloy particles 1935 may be formed by a cascading effect in which the molten alioy
droplets 1915 break up into smaller particles, the smaller les are recharged to
negative potential by impinging electrons and break up into yet smaller les, and
the process repeats during the time in which electrons are added to the successively
smaller atomized particles. Alternatively, or in addition, the atomized molten alloy
particles 1935 may be sequentiaiiy stripped from the surface of the moiten alloy ts
1915. Regardless of the physical atomization mechanism, molten alloy droplet 1915 is
exposed to the ing electron field 1925 for a sufficient time so that sufficient
negative charge accumulates in and disrupts the alloy into atomized molten alloy
particles 1935.
Referring to Figure 190, the atomized and electrically-charged
molten alloy particles 1935 are accelerated with at least one of an electrostatic field and
an electromagnetic field 1940. The field 1940 is configured to l the acceleration,
speed, and/or direction of the atomized and electricaliy-charged molten alioy particles
1935 so that the particles travel h the soiid—spray-forming system 1900 from the
atomizing apparatus 1920 toward the substrate 1930 in a controlled manner.
Referring to Figure 19D, the atomized and electrically-charged
molten alloy particles 1935 are cooled to a temperature no greater than the solidus
temperature of the alloy so that the molten alloy particles 1935 solidify whiie
accelerating and form solid alloy particles 1945. The aiioy particies 1935/1945 are
cooled and solidified before contacting ate 1930. Figure 19D shows a thermai
control zone comprising a cooling coil 1950. A cooiant fluid flows through the cooiing
coil to maintain a lower ature in the thermal control zone, which establishes a
greater temperature differential between the molten alloy particles 1935 and the
surrounding nment. A greater temperature differential may correiate with a higher
rate of heat loss from the molten aiioy les 1935, which allows for more effective
and/or efficient solidification into solid alloy particles 1945 before contacting the
substrate 1930. A; -
ism.a W“flaws“... .5“ i
PCT/U52012/046838
if is understood, however, that different cooling means
may be
utilized in a thermal control zone in the solid—spray-forming system 1900. For example,
a non-equilibrium plasma producing assembly (not shown), as described herein,
may be
used to cool and solidify the molten alloy particles 1935. Alternatively, or in addition, the
distance (d) between the atomizing apparatus 1920 and the substrate 1930
may be
configured with controlled atomized particle sizes and controlled particle acceleration to
cause solidification without variable heating or cooling in a thermal l
zone.
Referring to Figure 19E, the solid alloy particles 1945 impact onto
the substrate 1930, which comprise a collector having a positive electrical polarity
described herein. The impacting solid alloy les 1945 deform and metallurgically
bond to the substrate 1930 and produce a developing workpiece 1955. Referring to
Figure 19F, the solid alloy particles 1945 continue to impact onto the substrate 1930,
which comprise the ping workpiece 1955, deform and metallurgically bond to the
substrate 1930 and to each other to form a unitary and monolithic solid alloy preform.
One or more of the various components of the solid—spray-forming
system 1900 shown in s F may be enclosed in a vacuum vessel or
multiple operatively ted vacuum vessels. In various non—limiting embodiments, a
large voltage difference may be established between a positively biased substrate and a
negatively biased atomizing apparatus, which may facilitate the acceleration of
atomized molten alloy particles and the cooled solid alloy particles. The magnitude of
the voltage difference may correlate with the ing ration and impact velocity
of the alloy particles.
In various embodiments, the temperature of the solid alloy particles
at impact and the impact ty of the solid alloy particles are important ing
ters that affect the developing workpiece/preform. Control of these operating
ters may be accomplished by controlling the ed particle size, electrostatic
accetemfing‘voltage';"atomizing"apparatus-substrate distance, and/or variableWfifigor “ t
cooling the a thermal control zone between the atomizing apparatus and the substrate.
PCTfUSZOlZ/046838
In addition, aspects of the initial alloy melting operation may
present various disadvantages to an overall solid-spray—forming process. An initial alloy
g operation involves preparing a charge of suitable materials and then melting the
charge. The molten charge or “melt" may then be refined and/or treated to modify melt
chemistry and/or remove undesirable components from the melt. Melting furnaces may
be powered by means including electricity and the combustion of fossil fuels, and
selection of a suitable apparatus is largely influenced by the relative costs and
applicable environmental tions, as well as by the identity of the material being
prepared. General classes of melting techniques include, for example, induction
melting (including vacuum induction melting), arc melting (including vacuum arc skull
melting). crucible melting, and electron beam melting.
Melts ed in ceramic—lined furnaces may become
contaminated with oxides. Various melting techniques have been developed that
employ a vacuum environment and do not use a c-lined furnace. These
techniques result in significantly less oxide contamination in the melt ve to forming
the melt in a conventional ceramic-lined furnace. es of such techniques include,
for example, electron beam (EB) melting, vacuum arc remelting (VAR), vacuum double—
ode remelting (VADER), and electroslag ng/remelting (ESR). VAR, VADER,
and ESR techniques are bed, for e, in US. Patent Nos. 4,261,412;
,325,906; and 5,348,566; which are incorporated by reference into this specification.
Electron beam melting involves ing thermo-ionic electron beam
guns to produce high energy, substantially linear streams of ons which are used to
heat the target materials. Thermo—ionic electron beam guns operate by passing current
to a filament, thereby heating the filament to high temperature and "boiling" electrons
away from the filament. The electrons produced from the filament are then focused and
accelerated toward the target in the form of a very narrow (nearly two-dimensional),
substantially linear electron beam. A type ofion plasma electron beam gun also has
been used for preparingall‘oy‘melts ically, a "glow discharge" electron beam gun»
describedin VA. Chernov, “Powerful High-Voltage Glow Discharge Electron Gun and
Power Unit on Its Base," 1994 lntem. Conf. on on Beam Melting (Reno, Nevada),
WO 22552 PCT/U52012/046838
pp. 259-267, has been incorporated in certain melting es available from Antares,
Kiev, Ukraine. Such devices operate by producing a cold plasma including cations that
bombard a cathode and produce ons that are focused to form a substantially two-
dimensional, linear on beam.
The substantially linear electron beams ed by the foregoing
types of electron beam guns may be directed into an evacuated melting chamber of an
electron beam melting furnace and impinged on the materials to be melted and/or
maintained in a molten state. The conduction of electrons through the electrically
conductive materials quickly heats them to a temperature in excess of the particular
melting temperature. Given the high energy of the substantially linear electron beams,
which can be, for example, about 100 kW/cmg, linear electron beam
guns are very high
temperature heat sources and are readily able to exceed the melting temperatures and,
in some cases, the vaporization atures of the materials on which the substantially
linear beams e. Using magnetic deflection or similar ional means, the
substantially linear electron beams may be .rastered at high frequency across target
materials within a g chamber, allowing the beam to be ed across a wide
area and across targets having multiple and complex .
An electron beam cold hearth melting technique may be used in the
spray—forming processes, systems, and apparatus described herein. A feedstock
may be drip melted by impinging a ntially linear electron beam on an end of a
feedstock bar. The melted feedstock drips into an end region of a water-cooled
copper
hearth, forming a protective skull. As the molten material collects in the hearth, it
overflows and falls by gravity into an atomizing assembly. During the molten alloy
material’s dwell time within the hearth, substantially linear electron beams
may be
quickly rastered across the surface of the material, retaining it in a molten form. This
also has the effects of degassing and refining the molten alloy material through
evaporation of high vapor pressure components. The hearth also may be sized to
.. promote
gravity separation between high-density and low-densitysolid inclusions, in
which case oxide and other relatively low-density inclusions remain in the molten metal
WG 2013/022552 PCT/U82012/046838
for a time sufficient to allow dissolution, while high y particles sink to the bottom
and become entrapped in the skull.
g ques that are le for use in the solid—spray—
forming processes, systems, and tus described herein also include on
beam cold hearth g techniques that incorporate wire-discharge ion plasma
on emitters. These techniques are described, for example, in US. Patent No.
7,803,211 and in US. Patent Publication Nos. 2008/0237200 and 2010/0012629, which
are orated by reference into this specification.
As used herein, the term “wire-discharge ion plasma electron
emitter" refers to an apparatus that produces a relatively wide, three—dimensional field of
electrons by impinging positively charged ions onto a cathode and thereby releasing
electrons from the cathode. The electron beam produced by a wire-discharge ion
plasma electron emitter is not a two-dimensional beam, but instead is a three-
dimensional field or "flood" of electrons that, when impinged on the target, covers a two-
dimensional surface region on the target that is very large ve to the small point
d by impinging a substantially linear electron beam onto the target. As such, the
electron field produced by wire-discharge ion plasma electron emitters is referred to
herein as a “wide—area" electron field, with reference to the relatively much smaller point
of contact produced by conventional on guns used in electron beam melting
furnaces. Wire—discharge ion plasma electron emitters have been used for unrelated
applications are sly referred to, for example, as "wire ion plasma (WlP) electron"
guns or emitters, "WlP electron" guns or emitters and, somewhat confusingly, as "linear
electron beam emitters" (referring to the linear nature of the plasma—producing wire
electrode(s) in various embodiments of the devices).
Wire-discharge ion plasma electron emitters are available in a
variety of designs, but all such emitters share certain fundamental design attributes.
Each such emitte'rzincludes’a plasma or ionization region including a positive ion souseeas -» ~- '
in the form of an elongate wire anode to produce plasma including cations, and a
cathode that is spaced from and positioned to intercept positive ions generated by the
PCT/U82012/046838
wire. A large negative voltage is applied to the cathode, causing a fraction of the
positive ions in the plasma generated by the wire positive ion source to be accelerated
toward and to collide with the e surface such that secondary electrons are
emitted from the e (the "primary" ons being present within the plasma along
with the positive ions). The secondary electrons ed from the cathode surface
form an electron field that lly has the three-dimensional shape of the positive ion
plasma impacting the e. The secondary electrons are then accelerated from the
vicinity of the cathode back toward the anode, experiencing few collisions in the process
of passing through the essure gas within the emitter.
By properly configuring the various components of a wire—discharge
ion plasma electron emitter, a wide field of tic secondary electrons can be formed
at the cathode and accelerated from the r and toward a target. Figure 20 is a
simplified ion of components of a wire-discharge plasma ion electron emitter,
wherein a current is applied to a thin wire anode 12 to generate plasma 14. Positive
ions 16 within plasma 14 accelerate toward and collide with negatively—charged cathode
18, liberating wide—area secondary electron cloud 20, which is rated in the
ion of anode 12 by action of the electric field between the electrodes and toward
the target.
In various non-limiting embodiments, a system or apparatus
ured to perform a solid-spray-forming process may comprise a melting assembly
for melting an alloy that includes a pressure-regulated chamber (melting chamber) and
a hearth disposed in the melting chamber and configured to hold molten alloy. At least
one wire—discharge ion plasma eiectron emitter may be disposed in or adjacent to the
melting chamber and may be positioned to direct a three-dimensional, wide-area field of
electrons generated by the emitter into the chamber. The wire-discharge ion plasma
electron emitter produces a three-dimensional field of electrons having sufficient energy
to heat the electrically conductive alloy to its melting temperature.
in various non—limiting embodiments, an ing assembly is
configured to receive at least one of a stream and a series of droplets of molten alloy
WO 22552 PCT/U82012/046838
from the hearth. The melting assembly may be used to melt
any alloy that may be
melted using a tional electron beam melting furnace, such as, for e,
alloys based on aluminum, tantalum, titanium, tungsten, niobium, zirconium, nickel, iron,
and cobalt. In various non-iimiting embodiments, a melting assembly is configured to
' melt a charge comprising materials that make up the chemistry of cobalt—base
superalloys or nickel-base superalloys. in various other non-limiting embodiments, the
melting assembly is ured to melt a preformed alloy ingot or other structure, which
may have previously been produced and processed by one or more of VIM, VAR, and
ESR, for example.
A melting assembly may e one or more material feeders
d to introduce electrically conductive metals or other alloying additives into a
melting chamber. Feeder types may include, for example, bar feeders and wire
feeders, and the feeder type selected will depend upon the particular design
ements for a furnace. A material feeder and at least one wire—discharge ion
plasma electron emitter of a melting ly may be configured so that the electron
field emitted by the ischarge ion plasma electron emitter at least partially impinges
on the material introduced into the chamber by the . if the material that is
introduced into the melting chamber by the feeder is electrically conductive, then the
electron field may heat and melt the material.
A hearth incorporated in a melting assembly may be selected from
the various hearth types known in the art. For e, a melting assembly may be in
the nature of an electron beam cold health melting furnace by orating a cold
hearth or, more specifically, for example, a water—cooled copper cold hearth in the
melting chamber. As is known to those of ordinary skill, a cold hearth includes cooling
means causing molten material within the hearth to freeze to the hearth surface and
form a protective layer or skull. As another non—limiting example, a hearth
comprise an "autogenous" hearth, whichis a hearth thatIS plated with or fabricated from
"bathealloythatIs being meltedin the furnace, hwy-awr— -~
in which case the bottom stirface of the
hearth also may be cooled to prevent burn—through.
PCT/U82012/046838
The particular hearth ed in a melting r
may include a
molten material holding region, in which the molten material resides for a certain dwell
time before passing to a ream atomizing device in fluid communication with the
melting chamber. A hearth and at least one wire—discharge ion plasma electron emitter
may be positioned in a melting assembly so that the electron field emitted by the wire-
discharge ion plasma on emitter at least partially impinges on the molten al
holding region. In this , the electron field may be applied to maintain the alloy
material within the molten material holding region in a molten state.
In various embodiments, a melting ly includes a
pressure—
regulated melting r and a hearth ed in the re-regulated melting
chamber, wherein the hearth includes a molten material holding region. The melting
assembly may further include one or more wire-discharge ion plasma electron emitters
disposed in or adjacent the pressure—regulated melting chamber. The hearth and the at
least one wire-discharge ion plasma electron emitter are positioned so that
an electron
field produced by the emitter at least partially impinges on the molten material holding
region. An atomizing assembly in fluid communication with the pressure-regulated
g chamber may be positioned to receive molten material from the . A least
one feeder may be included in the e and may be configured to introduce material
into the pressure-regulated melting chamber in a position over at least a region of the
hearth.
Any suitable ischarge ion plasma electron emitter may be
used in systems and apparatus configured to pen‘orm a solid—spray—forming
process.
Suitable embodiments of ischarge ion plasma electron emitters are described, for
example, in US. Patent Nos. 4,025,818; 4,642,522; 4,694,222; 4,755,722; and
4,786,844, which are incorporated by reference into this specification. Suitable emitters
include those capable of producing a three—dimensional, wide-area electron field that
may be directed into a melting chamber ofafurnace and that will heat electrically
conductive feed materials placedin the melting chamber to the desired temperature.
Suitable emitters also include those capable of producing a three-dimensional, wide-
PCT/U82012/046838
area electron field that may be directed into an atomizing chamber and atomize molten
alloy material as discussed above.
] In various non-limiting embodiments of a wire-discharge ion plasma
electron emitter, the emitter includes a plasma region and a cathode region. The
plasma region includes at least one elongate wire anode adapted to produce a plasma
including positive ions. The cathode region includes a cathode which is electrically
connected to a high voltage power supply adapted to negatively charge the cathode. in
the wire-discharge ion plasma on r, the ode used to e the
plasma may be one wire or multiple wires positioned along a length of the plasma
region. At least a portion of the cathode impacted by the positive ions is composed of a
material suitable for ting electrons. s non-limiting embodiments of the
cathode disposed in the cathode region of the r also may include an insert, such
as, for example, a molybdenum insert, having a high melting temperature and a low
work function so as to facilitate generation of electrons. The cathode and the anode
positioned relative to one another so that the positive ions in the plasma generated by
the wire anode accelerate toward and impinge on the cathode under influence of the
electric field between the electrodes, liberating the wide—area field of secondary
electrons from the cathode.
Various miting embodiments of a wire-discharge ion plasma
electron r include at least one suitably electron transmissive window, such
as a
thin electron transmissive titanium or aluminum foil, that
opens through a wall of a
melting chamber and/or an ing chamber. Suitable electron transmissive windows
may also include, for example, windows comprising boron nitride or carbon (e.g.,
diamond) materials. Electron transmissive windows may further comprise als
including low atomic number elements generally known in the art to be transmissive to
electrons. Various non-limiting embodiments of a wire-discharge ion plasma electron
emitter do not include an electron transmissive window, in which case the plasma
region of the emitter fluidly communicates with a ggghamber and/or an atomizing
r. in either case, a wide-area electron field enters a melting chamber and/or
atomizing chamber and may be impinged on the material within the chamber(s). in
PCT/USZOlZ/046838
various non—limiting embodiments, a ischarge ion plasma electron emitter
may be
‘rastered to increase the volume of the wide area electron field produced
by the emitter.
if an electron transmissive window does separate the interior of the
electron emitter from a melting chamber or an atomizing chamber, then the electron
field passes through the window as it is projected from the electron emitter into the
chamber. In various non-liming embodiments of a ischarge ion plasma electron
emitter, a high e power supply electrically coupied to the cathode powers the
cathode to a negative voltage greater than 20,000 volts. The negative voltage
serves
the functions of accelerating the positive ions in the plasma toward the cathode, and
also repelling the secondary electron field from the cathode and toward the anode.
] An on transmissive window may be ary if the pressure
within the ischarge ion plasma electron emitter differs significantly from the
pressure within a melting chamber and/or atomizing chamber, in which case the foil
window serves to isolate the two adjacent regions of differing
pressure. An advantage
of ischarge ion plasma electron emitters relative to
non-gas containing electron
emitters, such as thermo—ionio electron beam guns, is that wire-discharge ion plasma
electron emitters must include gas within the plasma region to serve as the plasma
source. Although wire—discharge ion plasma electron emitters can operate at very low
gas pressures, such devices also can operate effectively at relatively high gas
pressures.
Figure 21 schematically illustrates a non—limiting embodiment of an
on beam melting assembly. The melting assembly 2210 es melting
r 2214 at least partially defined by chamber wall 2215. Wire-discharge ion
piasma electron emitters 2216 are positioned outside and adjacent chamber 2214. The
ischarge ion plasma electron emitters 2216 project wide-area electron fields 2218
into the interior of the r 2214. An alloy bar 2220 is introduced into the chamber
2214 by a bar feeder722‘1-9. Molten alloy 2226 is produced by ing the wide-area
electron field 2218 of at least one wire-discharge ion plasma electron emitter 2216 onto
the alloy bar 2220. The molten alloy 2226 melted from the alloy bar 2220 drops into
PCT/U82012/046838
water-cooled copper hearth 2224 and is resident in the hearth 2224 for a dwell time,
where it is heated, degassed, and refined by one or more of the wide-area electron
fields 2218 produced by the emitters 2216. The molten alloy 2226 ultimately drops from
the hearth 2224 into an atomizing assembly 2231 where the molten alloy is atomized to
alloy particles 2232, which are influenced by a field generating ly 2230,
solidified, and impacted onto a collector 2233.
As discussed above, the ischarge ion plasma electron
emitters 2216 of the melting assembly 2210 are configured to generate a field or "flood"
of energetic electrons covering a wide area relative to the spot coverage of a
substantially linear beam produced by a thermo-ionic electron beamgun. The electron
field emitters 2216 spread electrons over a wide area and impinge on the materials to
be melted and/or maintained in the molten state within the melting assembly 2210.
Likewise, wire-discharge ion plasma on emitters (not shown) may establish a
wide-area electron field in the atomizing assembly 2231 that impinges on molten alloy
received from the melting assembly 2210 and atomizes the molten alloy.
As noted above, various miting ments of wire—
rge ion plasma electron emitter generally include one or more elongate wire
anodes producing positive ion plasma, wherein the plasma is impinged upon a cathode
to te a field of secondary electrons that may be accelerated to impinge on a
target to be heated. A tic representation of one design of a wire-discharge ion
plasma electron emitter is shown in Figure 22. ' The emitter 2310 es an ionization
or plasma region 2314 in which a positive ion plasma is produced, and a e region
2316 that includes cathode 2318. The plasma region 2314 is filled with an ionizable gas
at low pressure, and the gas is ionized in the plasma region to produce -
containing plasma. For example, the ionization region 2314 may be filled with helium
gas at, for example, approximately 20 mTorr.
A small diameterxelcngate wire anode 2319 passes through a
length of the plasma chamber 2314. A positive voltage is applied to wire anode 2319 by
power supply 2322, and this initiates ionization of the helium gas into a plasma
WO 22552 PCT/U82012/046838
comprising helium cations and free electrons (the “primary" electrons). Once ionization
of the helium gas is initiated, the plasma is sustained by applying a voltage to the thin
wire anode 2319. Positively charged helium ions within the plasma are extracted from
the ionization chamber 2314 through an extraction grid 2326 maintained at a high
negative electrical potential and accelerated through a high voltage gap into the cathode
region 2316, where the cations in the plasma impact high negative e cathode
2318.
] Cathode 2318 may be, for example, a coated or uncoated metal or
alloy. lmpingement of helium ions on cathode 2318 releases secondary electrons from
cathode 2318. The high voltage gap 2328 accelerates the secondary electrons in a
direction opposite the direction of nt of the helium cations, h the
extraction grid 2326 and into the plasma region chamber 2314, and then through a thin
ic toil window 2329 made of material relatively transparent to electrons. As noted
above, depending on the relative gas pressures within the electron emitter and the
melting chamber and/or atomizing chamber, it may be possible to omit the foil window
2329, in which case the electrons ed by the r would enter the chamber
directly. The wide—area three-dimensional field of energetic electrons exiting the emitter
2310 may be directed to impinge on a target oned opposite toil window 2329 and
within a g chamber or an atomizing r.
One or more wire—discharge ion plasma electron emitters, such, for
example, emitter 231 0, may be provided to supply the electron field into a melting
chamber of an electron beam melting furnace and/or into an atomizing chamber of an
on beam atomizing assembly. As shown in Figure 6, a non—limiting embodiment of
an electron beam melting apparatus includes one or more wire—discharge ion plasma
electron emitters 2310 positioned adjacent a melting chamber 2330. A wide-area
electron field 2332 exits the emitter 2310 through a film window 2329 and floods at least
a region of the surface of a molten alloy 2334in a hearth 2336, thereby heatingthe alloy
to maintain it in a molten state.
PCT/USZOIZ/O46838
The film window 2329 may be omitted if the operating pressure
differential between the emitter 2310 and the melting chamber 2330 is not significant.
The melting r 2330 may be operated at a pressure higher than is conventional
in order to further reduce or ate undesirable elemental vaporization, and in such
case the need for a film window partitioning the electron emitter from the melting
chamber will, again, depend on the particular pressure ential used in the
configuration. ally, components 2340 for ostatically and/or
electromagnetically controlling the wide-area electron field are provided to allow further
ed control of the melting process within the melting chamber 2330.
Although Figure, 6 provides a simplified view of an embodiment of a
wire—discharge ion plasma on melting furnace including a single electron emitter,
multiple wire—discharge ion plasma electron emitters may be employed in various non—
limiting embodiments. One or more wire—discharge ion plasma electron emitters may be
incorporated in such an apparatus to: (1) melt raw materials introduced into the melting
r, in the form of, for example, an alloy ingot, slab, bar, wire, or other ; and
(2) maintain molten alloy resident in the furnace hearth at a temperature above the alloy
melting temperature (and possibly degas and/or refine the molten alloy). Also, in
various non-limiting ments, one or more wire-discharge ion plasma on
emitters may be used along with one or more electron beam guns producing
substantially two-dimensional, linear electron beams.
Figures 24 and 25 provide additional details of a non—limiting
embodiment of a wire-discharge ion plasma on emitter that
may be configured for
use as the source of energetic electrons in an embodiment of an electron beam melting
tus according to the present disclosure. Figure 24 is a perspective view, partly in
section, of a wire—discharge ion plasma electron emitter embodiment. Figure 25 is a
schematic diagram illustrating the operation of the emitter 2510 in Figure 24. The
emitter 2510 includes an electrically grounded enclosure 2513, which includes a
cathode region 2511, an ionization cr plasma region 2514, and an electron transmissive
foil window 2515. An elongate wire electrode 2516 extends through a length of the
ionization region 2514. The foil window 2515 is electrically coupled to the chamber
2513 and forms an anode that operates to accelerate electrons within the chamber
2513, which exit the chamber 2513 in the general direction of arrows “A". The chamber
2513 is filled with helium gas at low pressure, such as 1'10 mTorr, and is supptied with
the gas by a gas supply 2517. The gas supply 2517 is connected to the ure 2513
by a conduit 2519, which passes through a valve 2521. re regulation in the
chamber 2513 is controlled by a pump 2523, which is connected to the chamber 2513
by the conduit 2519.
The cathode region 251 1 includes a cathode 2518, which in turn
es an insert 2520 mounted on a lower surface thereof. The insert 2520 may
se, for example, molybdenum, but may comprise any material with a suitably
high ary electron emission coefficient. The cathode 2518 is suitably uniformly
spaced from the walls of enclosure 2513 to prevent Paschen breakdown. The cathode
2518 is coupled to a high voltage power supply 2522 by a cable 2525, which passes
through tor 2526 and into or 2528. The power supply 2522 supplies high
negative potential, for example, 200-300 W, to the cathode 2518. The cathode 2518
and the insert 2520 may be suitably cooled, such as, for example, by circulating a
cooling fluid through conduits 2524.
The ionization region 2514 includes a plurality of thin metallic ribs
2530, which are d both electrically and mechanically. Each rib 2530 es a
' central cut—out region to allow a wire ode 2516 to pass through the ionization
chamber 2514. The sides of the ribs 2530 facing the cathode 2518 form an extraction
grid 2534. The opposed side of all or a portion of the ribs 2530 provide a support grid
2536 for an electron transmissive foil window 2515. Cooling channels 2540 may be
provided to circulate a cooling fluid through and in the vicinity of ribs 2530 to allow for
heat removal from the ionization region 2514.
The electron transmissive foil window 2515, which may comprise,
for example, aluminum or titanium foil, is supported on the grid'2534 and issealed to
the ure 2513 by an O-ring or other structures sufficient to maintain the high
vacuum helium gas environment within the enclosure 2513. An electrical control device
WG 2613/022552 PCT/U82012/046838
2548 is connected to the wire electrode 2516 h a connector 2549. On activation
of the control device 2548, the wire eiectrode 2516 is energized to a high positive
iai, and the helium within the ionization region 2514 is ionized to e plasma
including helium cations. Once the plasma is ted in the ionization region 2514, the
cathode 2518 is energized by the power supply 2522. Helium cations in the ionization
region 2514 are electrically attracted to the e 2518 by the electric field that
extends from the cathode 2518 into the plasma region 2514. The helium cations travel
along the field lines, through the extraction grid 2534, and into the cathode region 2511.
E00184] In the cathode region 2511, the helium s accelerate across
the full potential of the electric field generated'by the energized cathode 2518 and
forcefully impinge on the cathode 2518 as a collimated beam of cations. The impacting
cations tree secondary electrons from the inset 2520. The secondary electron field
produced by the insert 2520 is rated in a direction opposite the direction of travel
of the helium cations, toward the wire electrode 2516 and through foil window 2515
Means may be provided to monitor the gas pressure within the
chamber 2513 as s in pressure may affect the density of the helium ion plasma
and, in turn, the density of the secondary electron field generated at the cathode 2518.
An initial pressure may be set within the enclosure 2513 by appropriately adjusting the
valve 2521. Once the cation-containing plasma is initiated in the plasma region 2514, a
e monitor 2550 may be provided to indirectly monitor the instantaneous quiescent
pressure within the chamber 2513. A rise in voltage is indicative of a lower chamber
pressure. The output signal of the voltage monitor 2550 is used to control the valve
2521 through a valve controller 2552. The current supplied to the wire electrode 2516
by the control device 2548 is also controlled by the signal of the voltage monitor 2550.
Utilizing the signal generated by the voltage monitor 2550 to control the gas supply
valve 2521 and to control the device 2548 allows for a stable electron field output from
the emitter 2510.
The current generated by the emitter 2510 may be determined by
the density of the cations ing the cathode 2518. The density of the cations
PCT/U52012/046838
impacting the cathode 2518 may be controlled by adjusting the voltage on the wire
electrode 2516 h the control device 2548. The energy of the electrons d
from the cathode 2518 may be controlled by adjusting the voltage on the e 2518
h the power supply 2522. Both current and energy of the emitted electrons can
be independently controlled, and the relationships between these parameters and the
applied voltages are linear, rendering control of the emitter 2510 both efficient and
effective.
[001 87] Figure 26 is a schematic ration of an electron beam melting
assembly 2610 incorporating two wire~discharge ion plasma electron emitters 2614 and
2616 having a design as shown in s 24 and 25. The melting ly 2610
includes a melting chamber 2620, a material feeder 2622, and is ively connected
to an atomizing assembly 2624. The current required for operation of the emitters 2614
and 2616 is fed to the emitters by power lines 2626, and the interface between the
emitters 2614 and 2616 and the melting chamber 2620 includes electron transmissive
foil windows 2634 and 2636, which allow the electron fields 2638 produced by the
emitters 2614 and 2616 to enter the melting chamber 2620. Electromagnetic control
devices 2639 for magnetically steering the electron fields 2638 may be included within
melting r 2620 to provide additional process control.
A hearth 2640, which may be, for example, a cold hearth, is
positioned in the melting chamber 2620. In operation, the wire-discharge ion plasma
electron emitters 2614 and 2616 are energized and produce the electron fields 2618.
An alloy feed material 2644 is introduced into the g chamber 2620 by the feeder
2622, is melted by the electron field 2638 emitted from the emitter 2614, and drops to
the hearth 2640. The wide-area electron field 2638 emitted by the emitter 2616 heats,
degasses, and refines the molten alloy material 2642 while resident in the hearth 2640.
The molten material 2642 es along the hearth 2640 and drops into the atomizing
assembly 2624 andis solid--spray--formed into a solid prefon'n. The atomizing assembly
«#3.; -
2624 may comprise one or more thermo--ionicelectron beam emitters and/or one or
more wire-dischargeion plasma electron emitters.
PCTIUSZOiZ/04683S
This specification has been written with reference to various non—
limiting and non—exhaustive embodiments. However, it will be recognized by persons
having ordinary skill in the art that various substitutions, cations, or ations
of any of the disclosed embodiments (or portions thereof)
may be made within the
scope of this ication. Thus, it is piated and understood that this
specification supports additional embodiments not expressly set forth herein. Such
embodiments may be obtained, for example, by combining, modifying, or nizing
any of the disclosed steps, components, elements, features, aspects, characteristics,
limitations, and the like, of the various non-limiting embodiments described in this
specification. in this manner, Applicant reserves the right to amend the ciaims during
prosecution to add features as variously described in this specification, and such
amendments comply with the requirements of 35 [1.8.0. § 112, first aph, and 35
U.S.C. § 132(a).
CLAlMS
Claims (4)
1. A process comprising: producing at least one of a stream of molten alloy and a series of droplets of molten alloy; producing electrically-charged particles of the molten alloy by impinging ons on at least one of the stream of molten alloy and the series of droplets of molten alloy to e the molten alloy; accelerating the electrically—charged molten alloy particles with at least one of an electrostatic field and an electromagnetic field; cooling the molten alloy particles to a temperature that is no greater than a solidus temperature of the alloy so that the molten alloy les solidity while accelerating and form solid alloy particles; impacting the solid alloy particles onto a substrate, wherein the impacting particles deform and metallurgically bond to the substrate to produce a solid alloy preform.
2. The process of claim 1, wherein the molten alloy particles are cooled to a ature that is no greater than the solidus temperature of the alloy and that is greater than 0.50 times the s temperature of the alloy.
3. The process of claim 1, n the molten alloy particles are cooled to a temperature that is no greater than 0.95 times the solidus temperature of the alloy and that is greater than 0.50 times the solidus temperature of the alloy.
4. The process of claim 1, wherein cooling the molten alloy particles comprises contacting the molten alloy paFtiEliesLWith’a non-equilibrium plasma. PCT/U
Applications Claiming Priority (3)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US13/207,629 US8747956B2 (en) | 2011-08-11 | 2011-08-11 | Processes, systems, and apparatus for forming products from atomized metals and alloys |
US13/207,629 | 2011-08-11 | ||
PCT/US2012/046838 WO2013022552A2 (en) | 2011-08-11 | 2012-07-16 | Processes, systems, and apparatus for forming products from atomized metals and alloys |
Publications (2)
Publication Number | Publication Date |
---|---|
NZ619930A NZ619930A (en) | 2016-06-24 |
NZ619930B2 true NZ619930B2 (en) | 2016-09-27 |
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