WO2004042095A1 - Procede servant a preparer de la poudre de niobium et/ou de tantale presentant une surface importante - Google Patents
Procede servant a preparer de la poudre de niobium et/ou de tantale presentant une surface importante Download PDFInfo
- Publication number
- WO2004042095A1 WO2004042095A1 PCT/BR2003/000122 BR0300122W WO2004042095A1 WO 2004042095 A1 WO2004042095 A1 WO 2004042095A1 BR 0300122 W BR0300122 W BR 0300122W WO 2004042095 A1 WO2004042095 A1 WO 2004042095A1
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- WO
- WIPO (PCT)
- Prior art keywords
- niobium
- powder
- surface area
- production
- large surface
- Prior art date
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- 239000010955 niobium Substances 0.000 title claims abstract description 55
- 238000000034 method Methods 0.000 title claims abstract description 39
- 229910052758 niobium Inorganic materials 0.000 title claims abstract description 35
- GUVRBAGPIYLISA-UHFFFAOYSA-N tantalum atom Chemical compound [Ta] GUVRBAGPIYLISA-UHFFFAOYSA-N 0.000 title claims abstract description 28
- 238000004519 manufacturing process Methods 0.000 title claims abstract description 21
- ZYTNDGXGVOZJBT-UHFFFAOYSA-N niobium Chemical compound [Nb].[Nb].[Nb] ZYTNDGXGVOZJBT-UHFFFAOYSA-N 0.000 title claims abstract description 14
- 150000003839 salts Chemical class 0.000 claims abstract description 78
- 239000000843 powder Substances 0.000 claims abstract description 52
- GUCVJGMIXFAOAE-UHFFFAOYSA-N niobium atom Chemical compound [Nb] GUCVJGMIXFAOAE-UHFFFAOYSA-N 0.000 claims abstract description 23
- 229910052783 alkali metal Inorganic materials 0.000 claims abstract description 22
- 150000001340 alkali metals Chemical class 0.000 claims abstract description 22
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 claims abstract description 16
- 229910052715 tantalum Inorganic materials 0.000 claims abstract description 12
- 239000007864 aqueous solution Substances 0.000 claims abstract description 9
- 150000004678 hydrides Chemical class 0.000 claims abstract description 8
- 229910052757 nitrogen Inorganic materials 0.000 claims abstract description 8
- 229910000484 niobium oxide Inorganic materials 0.000 claims abstract description 4
- BPUBBGLMJRNUCC-UHFFFAOYSA-N oxygen(2-);tantalum(5+) Chemical compound [O-2].[O-2].[O-2].[O-2].[O-2].[Ta+5].[Ta+5] BPUBBGLMJRNUCC-UHFFFAOYSA-N 0.000 claims abstract description 3
- 238000011084 recovery Methods 0.000 claims abstract description 3
- 229910001936 tantalum oxide Inorganic materials 0.000 claims abstract description 3
- 239000000203 mixture Substances 0.000 claims description 32
- 239000003638 chemical reducing agent Substances 0.000 claims description 30
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 17
- 239000011575 calcium Substances 0.000 claims description 12
- 229910052791 calcium Inorganic materials 0.000 claims description 10
- 229910052751 metal Inorganic materials 0.000 claims description 10
- 239000002184 metal Substances 0.000 claims description 10
- 239000011777 magnesium Substances 0.000 claims description 9
- 239000000243 solution Substances 0.000 claims description 9
- OYPRJOBELJOOCE-UHFFFAOYSA-N Calcium Chemical compound [Ca] OYPRJOBELJOOCE-UHFFFAOYSA-N 0.000 claims description 8
- 238000001914 filtration Methods 0.000 claims description 8
- 239000007789 gas Substances 0.000 claims description 8
- 238000010907 mechanical stirring Methods 0.000 claims description 8
- 229910052749 magnesium Inorganic materials 0.000 claims description 7
- 230000008018 melting Effects 0.000 claims description 7
- 238000002844 melting Methods 0.000 claims description 7
- 238000003756 stirring Methods 0.000 claims description 7
- 238000002386 leaching Methods 0.000 claims description 6
- FYYHWMGAXLPEAU-UHFFFAOYSA-N Magnesium Chemical compound [Mg] FYYHWMGAXLPEAU-UHFFFAOYSA-N 0.000 claims description 5
- 239000011261 inert gas Substances 0.000 claims description 5
- 238000002347 injection Methods 0.000 claims description 5
- 239000007924 injection Substances 0.000 claims description 5
- FAPWRFPIFSIZLT-UHFFFAOYSA-M Sodium chloride Chemical compound [Na+].[Cl-] FAPWRFPIFSIZLT-UHFFFAOYSA-M 0.000 claims description 4
- 150000004673 fluoride salts Chemical class 0.000 claims description 3
- 230000007928 solubilization Effects 0.000 claims description 3
- 238000005063 solubilization Methods 0.000 claims description 3
- 239000003513 alkali Substances 0.000 claims description 2
- 150000001875 compounds Chemical class 0.000 claims description 2
- 238000004320 controlled atmosphere Methods 0.000 claims description 2
- 239000011780 sodium chloride Substances 0.000 claims description 2
- 229910000102 alkali metal hydride Inorganic materials 0.000 claims 2
- 150000003841 chloride salts Chemical class 0.000 claims 2
- 150000004681 metal hydrides Chemical class 0.000 claims 2
- 230000002378 acidificating effect Effects 0.000 claims 1
- WUKWITHWXAAZEY-UHFFFAOYSA-L calcium difluoride Chemical compound [F-].[F-].[Ca+2] WUKWITHWXAAZEY-UHFFFAOYSA-L 0.000 claims 1
- 229910001634 calcium fluoride Inorganic materials 0.000 claims 1
- 238000001035 drying Methods 0.000 claims 1
- 229910017464 nitrogen compound Inorganic materials 0.000 claims 1
- 150000002830 nitrogen compounds Chemical class 0.000 claims 1
- 239000000047 product Substances 0.000 claims 1
- 239000012265 solid product Substances 0.000 claims 1
- 239000002245 particle Substances 0.000 abstract description 15
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 abstract description 9
- 238000004090 dissolution Methods 0.000 abstract description 9
- 239000001301 oxygen Substances 0.000 abstract description 9
- 229910052760 oxygen Inorganic materials 0.000 abstract description 9
- 239000003990 capacitor Substances 0.000 abstract description 3
- 238000006243 chemical reaction Methods 0.000 description 22
- 239000008367 deionised water Substances 0.000 description 15
- 229910021641 deionized water Inorganic materials 0.000 description 15
- 239000000463 material Substances 0.000 description 8
- 239000012298 atmosphere Substances 0.000 description 7
- UXVMQQNJUSDDNG-UHFFFAOYSA-L Calcium chloride Chemical compound [Cl-].[Cl-].[Ca+2] UXVMQQNJUSDDNG-UHFFFAOYSA-L 0.000 description 6
- 239000001110 calcium chloride Substances 0.000 description 6
- 229910001628 calcium chloride Inorganic materials 0.000 description 6
- 238000010438 heat treatment Methods 0.000 description 6
- 239000007788 liquid Substances 0.000 description 6
- 150000002739 metals Chemical class 0.000 description 6
- 239000007790 solid phase Substances 0.000 description 6
- 239000000126 substance Substances 0.000 description 6
- PXHVJJICTQNCMI-UHFFFAOYSA-N Nickel Chemical compound [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 description 5
- 239000002994 raw material Substances 0.000 description 5
- 229910052708 sodium Inorganic materials 0.000 description 5
- 239000011734 sodium Substances 0.000 description 5
- DGAQECJNVWCQMB-PUAWFVPOSA-M Ilexoside XXIX Chemical compound C[C@@H]1CC[C@@]2(CC[C@@]3(C(=CC[C@H]4[C@]3(CC[C@@H]5[C@@]4(CC[C@@H](C5(C)C)OS(=O)(=O)[O-])C)C)[C@@H]2[C@]1(C)O)C)C(=O)O[C@H]6[C@@H]([C@H]([C@@H]([C@H](O6)CO)O)O)O.[Na+] DGAQECJNVWCQMB-PUAWFVPOSA-M 0.000 description 4
- WCUXLLCKKVVCTQ-UHFFFAOYSA-M Potassium chloride Chemical compound [Cl-].[K+] WCUXLLCKKVVCTQ-UHFFFAOYSA-M 0.000 description 4
- 239000012300 argon atmosphere Substances 0.000 description 4
- 238000000265 homogenisation Methods 0.000 description 4
- 238000013021 overheating Methods 0.000 description 4
- 229910020312 KCl—KF Inorganic materials 0.000 description 3
- 239000003153 chemical reaction reagent Substances 0.000 description 3
- 150000001805 chlorine compounds Chemical class 0.000 description 3
- 238000011109 contamination Methods 0.000 description 3
- 238000001816 cooling Methods 0.000 description 3
- 229910052744 lithium Inorganic materials 0.000 description 3
- 229910052759 nickel Inorganic materials 0.000 description 3
- XKRFYHLGVUSROY-UHFFFAOYSA-N Argon Chemical compound [Ar] XKRFYHLGVUSROY-UHFFFAOYSA-N 0.000 description 2
- 229910020549 KCl—NaCl Inorganic materials 0.000 description 2
- WHXSMMKQMYFTQS-UHFFFAOYSA-N Lithium Chemical compound [Li] WHXSMMKQMYFTQS-UHFFFAOYSA-N 0.000 description 2
- 229910052784 alkaline earth metal Inorganic materials 0.000 description 2
- 230000015572 biosynthetic process Effects 0.000 description 2
- 239000003795 chemical substances by application Substances 0.000 description 2
- 230000003247 decreasing effect Effects 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 150000004767 nitrides Chemical class 0.000 description 2
- 239000011574 phosphorus Substances 0.000 description 2
- 229910052698 phosphorus Inorganic materials 0.000 description 2
- 229910052700 potassium Inorganic materials 0.000 description 2
- 239000001103 potassium chloride Substances 0.000 description 2
- 235000011164 potassium chloride Nutrition 0.000 description 2
- 239000003870 refractory metal Substances 0.000 description 2
- 229910001220 stainless steel Inorganic materials 0.000 description 2
- 239000010935 stainless steel Substances 0.000 description 2
- 229910019675 CsCl—LiCl Inorganic materials 0.000 description 1
- 229910020302 KBr—LiBr Inorganic materials 0.000 description 1
- 229910013618 LiCl—KCl Inorganic materials 0.000 description 1
- 229910020999 NaCl—RbCl Inorganic materials 0.000 description 1
- 229910052779 Neodymium Inorganic materials 0.000 description 1
- OAICVXFJPJFONN-UHFFFAOYSA-N Phosphorus Chemical compound [P] OAICVXFJPJFONN-UHFFFAOYSA-N 0.000 description 1
- ZLMJMSJWJFRBEC-UHFFFAOYSA-N Potassium Chemical compound [K] ZLMJMSJWJFRBEC-UHFFFAOYSA-N 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 229910052786 argon Inorganic materials 0.000 description 1
- 229910052788 barium Inorganic materials 0.000 description 1
- 230000004888 barrier function Effects 0.000 description 1
- AIYUHDOJVYHVIT-UHFFFAOYSA-M caesium chloride Inorganic materials [Cl-].[Cs+] AIYUHDOJVYHVIT-UHFFFAOYSA-M 0.000 description 1
- 229910052804 chromium Inorganic materials 0.000 description 1
- 230000001627 detrimental effect Effects 0.000 description 1
- 239000003085 diluting agent Substances 0.000 description 1
- 238000009826 distribution Methods 0.000 description 1
- 239000001307 helium Substances 0.000 description 1
- 229910052734 helium Inorganic materials 0.000 description 1
- SWQJXJOGLNCZEY-UHFFFAOYSA-N helium atom Chemical compound [He] SWQJXJOGLNCZEY-UHFFFAOYSA-N 0.000 description 1
- 229910052742 iron Inorganic materials 0.000 description 1
- AMXOYNBUYSYVKV-UHFFFAOYSA-M lithium bromide Inorganic materials [Li+].[Br-] AMXOYNBUYSYVKV-UHFFFAOYSA-M 0.000 description 1
- URLJKFSTXLNXLG-UHFFFAOYSA-N niobium(5+);oxygen(2-) Chemical class [O-2].[O-2].[O-2].[O-2].[O-2].[Nb+5].[Nb+5] URLJKFSTXLNXLG-UHFFFAOYSA-N 0.000 description 1
- -1 nitride ions Chemical class 0.000 description 1
- YHBDIEWMOMLKOO-UHFFFAOYSA-I pentachloroniobium Chemical compound Cl[Nb](Cl)(Cl)(Cl)Cl YHBDIEWMOMLKOO-UHFFFAOYSA-I 0.000 description 1
- 230000000737 periodic effect Effects 0.000 description 1
- 150000003018 phosphorus compounds Chemical class 0.000 description 1
- 239000011591 potassium Substances 0.000 description 1
- 238000001556 precipitation Methods 0.000 description 1
- 239000011833 salt mixture Substances 0.000 description 1
- 239000012266 salt solution Substances 0.000 description 1
- 238000005204 segregation Methods 0.000 description 1
- 238000005245 sintering Methods 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 229910052719 titanium Inorganic materials 0.000 description 1
- 238000001291 vacuum drying Methods 0.000 description 1
- 238000009834 vaporization Methods 0.000 description 1
- 230000008016 vaporization Effects 0.000 description 1
Classifications
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01G—CAPACITORS; CAPACITORS, RECTIFIERS, DETECTORS, SWITCHING DEVICES, LIGHT-SENSITIVE OR TEMPERATURE-SENSITIVE DEVICES OF THE ELECTROLYTIC TYPE
- H01G9/00—Electrolytic capacitors, rectifiers, detectors, switching devices, light-sensitive or temperature-sensitive devices; Processes of their manufacture
- H01G9/004—Details
- H01G9/04—Electrodes or formation of dielectric layers thereon
- H01G9/048—Electrodes or formation of dielectric layers thereon characterised by their structure
- H01G9/052—Sintered electrodes
- H01G9/0525—Powder therefor
-
- 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
- B22F9/16—Making metallic powder or suspensions thereof using chemical processes
- B22F9/18—Making metallic powder or suspensions thereof using chemical processes with reduction of metal compounds
- B22F9/24—Making metallic powder or suspensions thereof using chemical processes with reduction of metal compounds starting from liquid metal compounds, e.g. solutions
-
- C—CHEMISTRY; METALLURGY
- C22—METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
- C22B—PRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
- C22B34/00—Obtaining refractory metals
- C22B34/10—Obtaining titanium, zirconium or hafnium
- C22B34/12—Obtaining titanium or titanium compounds from ores or scrap by metallurgical processing; preparation of titanium compounds from other titanium compounds see C01G23/00 - C01G23/08
- C22B34/1263—Obtaining titanium or titanium compounds from ores or scrap by metallurgical processing; preparation of titanium compounds from other titanium compounds see C01G23/00 - C01G23/08 obtaining metallic titanium from titanium compounds, e.g. by reduction
- C22B34/1268—Obtaining titanium or titanium compounds from ores or scrap by metallurgical processing; preparation of titanium compounds from other titanium compounds see C01G23/00 - C01G23/08 obtaining metallic titanium from titanium compounds, e.g. by reduction using alkali or alkaline-earth metals or amalgams
-
- C—CHEMISTRY; METALLURGY
- C22—METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
- C22B—PRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
- C22B34/00—Obtaining refractory metals
- C22B34/20—Obtaining niobium, tantalum or vanadium
-
- C—CHEMISTRY; METALLURGY
- C22—METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
- C22B—PRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
- C22B34/00—Obtaining refractory metals
- C22B34/20—Obtaining niobium, tantalum or vanadium
- C22B34/24—Obtaining niobium or tantalum
-
- C—CHEMISTRY; METALLURGY
- C22—METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
- C22B—PRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
- C22B5/00—General methods of reducing to metals
- C22B5/02—Dry methods smelting of sulfides or formation of mattes
- C22B5/04—Dry methods smelting of sulfides or formation of mattes by aluminium, other metals or silicon
-
- 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
- B22F2998/00—Supplementary information concerning processes or compositions relating to powder metallurgy
- B22F2998/10—Processes characterised by the sequence of their steps
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B22—CASTING; POWDER METALLURGY
- B22F—WORKING METALLIC POWDER; MANUFACTURE OF ARTICLES FROM METALLIC POWDER; MAKING METALLIC POWDER; APPARATUS OR DEVICES SPECIALLY ADAPTED FOR METALLIC POWDER
- B22F2999/00—Aspects linked to processes or compositions used in powder metallurgy
Definitions
- NbxOy, and/or TaxOy a controlled layer of niobium and/or tantalum oxide
- the main problem of the metallothermal reaction is its strongly exothermal and uncontrolled reaction, causing an excessive heating of the system and impairing the characteristics of the powder that is produced (increase in mean particle size and decrease of specific area).
- One of the manners of controlling the reaction is to perform the reduction initially to a sub-oxide of niobium, such as described in some patents, since in this condition the exothermal characteristic of the reaction is less intense.
- the sub-oxide thus produced would then be reduced to metallic niobium, again with less intense exothermal behavior, producing a powder with the recommended characteristics.
- such procedure creates a need to conduct the process in two stages, requiring an increased consumption of energy and time.
- the possibility of contamination of the powder is increased due to the greater number of stages under high temperatures in contact with the oven atmosphere, with the reducing agent and with the container where the reaction takes place.
- 4,725,312 and WO 01/59166 proposes a process for the production of metals in powder form of groups IV-B and V-B of the Periodic Table of Elements (US Patent No. 4,725,312) by reducing the salts of those metals through the use of a bath of molten salts containing lithium as the reducing agent.
- a wide range of binary mixtures of salts is mentioned, among which there should be pointed out: LiCl-KCl, CsCl-LiCl, RbCl-LiBr and KBr-LiBr, LiCl-NaCl-CsCl, LiCl-NaCl-RbCl and LiCl-KCl-KF.
- the bath of salts is kept at a temperature between 400 and 550°C.
- the quantity of lithium present in the bath of molten salts should at least be the stoichiometric amount required for the reduction of the chlorides of Nb, Ti and Nd, and these chlorides may be introduced in solid, liquid or gas form, this latter being preferred.
- WO 01/59166 mention the production of niobium powders by means of the reduction of K2NbF7 using sodium as the reducing agent added to a bath of molten salts (KCl-KF or KCl-NaCl).
- the main advantages of the use of the method of reduction in molten salts are: a) the dissipation of the heat generated in the reaction occurs in the bath of salts thus avoiding localized overheating; b) it is possible to control the reducing potential of the reducing agent by means of the dissolution thereof in a molten salt; c) it is possible to continuously feed both the reducing agent and the raw material containing Nb and/or Ta to the salts bath and thereby to control the speed of reduction and therefore the generation of heat; d) avoiding direct contact between the reducing agent and the source of Nb and/or Ta, decreasing the possibility of sintering and inadequate growth of the powder of Nb and or Ta thus reduced; e) it is possible to stir the bath of salts, and therefore to allow control over the speed of the reaction increasing or decreasing the rate of dissolution both of the reducing agent and of the source of Nb and/or Ta in the molten salt; f) it is possible to control the reaction temperature by proper selection of a salt solution which melting
- the oxide of niobium and/or tantalum may be reduced in a controlled manner with a strong reducing agent producing a power of high purity, with a sponge-like morphology, of low apparent density and large specific surface area.
- the raw material is a metallic niobium and/or tantalum powder and/or hydrides thereof of high purity and adequate size, that was previously oxidized in a controlled manner to have an adequate layer of oxide, the thermal energy generated in the reduction of this layer of oxide is much less than that which would be generated to obtain the same particle if the raw material was to consist entirely in oxide. This lesser generation of energy facilitates the control of the process such that the possibility of contamination by gasses and other metals is significantly reduced, which may be evidenced by the low leakage current of the powder obtained using this process.
- the present invention comprises a process for the production of metallic powder of niobium and/or tantalum by means of metallothermal reduction in molten salts wherein the problems of overheating during the reduction, or of the need to conduct the process in more than one step, are eliminated.
- the reaction is more controlled due to the possibility of controlling the potential of the reducing agent, due to the same being diluted in the salt at the desired concentration. In this manner, the driving force for the reduction may be controlled, allowing increased control of the process.
- oxidized powder a raw material in the form of a powder, of adequate size, consisting basically in metallic niobium and/or tantalum and/or hydrides thereof, of high purity, previously oxidized in a controlled manner (hereinafter referred as "oxidized powder"), leads to a uniform precipitation of the Nb and or the Ta, with the aspect of a sponge, within the medium of liquid salt, producing an adequate distribution of particles without the formation of clusters of undesirable size.
- the reducing agent is an alkali or earth alkali metal, preferably calcium or magnesium and/or a hydride of such metal. Nitrides of alkali metals or earth alkali metals may also be fed to the reactor constituting sources of N2 for the produced niobium and/or tantalum.
- the reduction occurs at temperatures between 300 and 1200°
- the salt may be subjected to mechanical stirring or to the injection of an inert or partially inert gas containing, for example, N2.
- the molten salt may be comprised of mixtures of salts or of pure salts, such as fluorides and chlorides of Ca, Li, Ba, Mg, K and Na.
- the salts evidencing greater solubility of the reducing agent are preferred, such as CaC12 when employing calcium as reducing agent.
- the reducing agent and the oxidized Nb and/or Ta powder may be continuously fed to the molten salt using devices that allow to control the feed rate of both.
- the temperature of the process may be kept constant by controlling the feed rate of the raw materials.
- the quantity of reducing agent that is used should be at least the stoichiometric amount for the reduction of all the oxide of the oxidized powder of Nb and/or Ta that is fed. There may be employed a quantity up to 800% of the stoichiometric amount. Such excess depends, among other parameters, on the quantity of salts bath.
- Both the reducing agent and the "oxidized powder" may be added together with the salt bath to the reduction reactor prior to the melting step or may be fed separately or together to the salt bath upon the prior melting thereof. This feeding may be carried out continuously or otherwise.
- the quantity of reducing agent is substantially less in comparison to the reduction of particles of oxides, and depending on the oxygen content of the oxidized powder, the required quantity of reducing agent may be previously added to the salt bath.
- the following salts or mixtures thereof are employed to control the reaction: CaC12, NaCl, KC1 and MgC12.
- the mixture of salts allows the reduction to occur at a lower temperature, allowing to obtain smaller particle sizes and larger surface areas.
- the quantity of salt or mixture of salts will have an effect on the control of the reaction temperature, the greater is the quantity of salt the easier it will be to control the temperature.
- the quantity of salt used may vary between 5 and lOOg/g of oxidized powder fed.
- the reaction may be carried out in stainless steel, nickel, tantalum or niobium reactors, depending on the degree of contamination that can be tolerated in the product obtained.
- the resulting salt mixture containing metallic niobium and/or tantalum is dissolved in deionized water and is subsequently filtered and leached with a solution containing HC1 and which may also contain HF, HN03 and H2S04. After the leaching the material is rinsed and dried.
- the amount of water for solubilization of the salt varies between 10 and 100 liters for every 5 kg of salt.
- For the acid leaching step there are used 1 to 100 ml of solution for every gram of powder obtained from dissolution of the salt.
- the control of the nitrogen content in the Nb and/or Ta may be effected by controlling the partial pressure of N2 in the atmosphere of the oven, by an injection of N2 gas or of mixtures of gasses containing N2 into the molten salt, or yet, by the addition of N2 carrier elements, such as nitrides soluble in the molten salt.
- N2 carrier elements such as nitrides soluble in the molten salt.
- a part of the nitrogen is dissolved in the solution of salts allowing that nitride ions may be available to allow the solubilization of nitrogen in the particles of Nb and/or Ta.
- it is possible to dope with phosphorus by adding phosphorus compounds soluble in the salt bath.
- the particles of powder of Nb and or Ta produced using the present process have a reduced size, have a large surface area and a sponge-like morphology, and are adequate for the production of capacitors.
- the reducing procedure consists in melting the salt initially in a stainless steel, nickel, niobium or tantalum reactor, either or not in the presence of the oxidized powder, and of the reducing agent in an inert gas atmosphere.
- the oven chamber Before the heating of the reactor, the oven chamber should be evacuated and then pressurized with the inert gas at pressures that may vary from 400 to 1200 torr.
- the temperature is stabilized between 30 and 150° C above the melting point of the salt or of the reducing metal, whichever has the higher melting point. From this moment on there is started the stirring process of the bath using a mechanical agitator or by means of injection of an inert or reactive gas (N2 or a mixture of N2 with an inert gas). If the reducing agent and/or the "oxidized powder" have not been previously added, there is initiated the addition of both or of one of them using an adequate system that allows to control the feed rate to the salt bath.
- the stirring is discontinued and the oven is turned off to allow the cooling of the salt containing metallic Nb and or Ta.
- the time required for the reduction will depend on the feed rate of the reducing agent or the oxidized powder, or yet of the quantity of powder and reducer fed together with the salt prior to the beginning of the reaction.
- the feed rate of the oxidized powder is an important parameter for the control of the process, since it may control the localized generation of heat. However, as previously explained, this amount of heat is substantially less when compared to the use of oxide of Nb and/or Ta as source of Nb and/or Ta.
- the reduction temperature may have an influence on the surface area of the produced powder. Higher temperatures may lead to larger particles with lesser specific surfaces. Therefore, the selection of the mixture of salts is important with a view to lowering the temperature of the process.
- Stirring the salt is also important to avoid localized overheating and to disperse the oxidized powder, avoiding its segregation in the bath.
- Figure 1 is a schematic drawing of a reactor for reduction of the oxidized powder
- Figure 2 depicts a detail of the support stem inside the crucible
- Figure 3 illustrates back-scattered electrons of the typical morphology of powders produced using the processes set forth herein.
- Figure 1 is a schematic drawing of the reactor used for the reduction in molten salts where the oxidized powder is continuously fed in a crucible containing a molten salt. In the same crucible that contains the salt, there is placed another container, submerged in the salt, containing the liquid alkali metal or earth alkali metal.
- the identifications of Figure 1 are: 1- Crucible containing the liquid alkali metal or earth alkali metal; 2- Crucible containing the molten salt; 3- Stirring stem; 4- Molten salt; 5- Inert or reactive gas inlet; 6- "oxidized powder"; 7- Container with the "oxidized powder” contained therein; 8- Thermocouple; 9- Oven chamber and 10- Vacuum system outlet.
- the mechanical stirring may be substituted by stirring caused by injection of an inert or reactive gas.
- the produced material is dissolved in deionized water.
- the solution obtained in the dissolution of the salt is filtered, and is then leached in a solution containing HC1, HN03, H2S04 and HF.
- the amount of leaching solution employed is 1 to 100 ml/g of filtered product, preferably 10 to 40 ml/g. After this leaching, there is performed a final rinsing with deionized water, filtration and subsequently, vacuum-drying.
- Ta obtained has contents of Mg and Ca below 500 ppm, sodium content below 50 ppm, oxygen content between 1,000 and 4,000 ppm/(m2/g), sum total of contents of Fe, Cr and Ni below 300 ppm and a specific surface area between 1 and 30 m2/g.
- the material was removed from the reactor and subjected to dissolution in deionized water.
- the solid phase was leached with an aqueous solution containing HCl and HF for 90 minutes. This mixture was then filtered and rinsed with 10 liters of deionized water. The cake obtained from filtration was subsequently vacuum-dried.
- the chemical analysis of the obtained powder evidenced that the oxygen content had fallen from 18,000 ppm to 3,850 ppm.
- the material was removed from the reactor and subjected to dissolution in deionized water.
- the solid phase was leached with an aqueous solution containing HCl and HF for 90 minutes. This mixture was then filtered and rinsed with 10 liters of deionized water. The cake obtained from filtration was subsequently vacuum-dried.
- the chemical analysis of the obtained powder evidenced that the oxygen content had fallen from 6,300 ppm to 785 ppm.
- the material was removed from the reactor and subjected to dissolution in deionized water.
- the solid phase was leached with an aqueous solution containing HCl and HF for 90 minutes. This mixture was then filtered and rinsed with 10 liters of deionized water. The cake obtained from filtration was subsequently vacuum-dried.
- the chemical analysis of the obtained powder evidenced that the oxygen content had fallen from 52,210 ppm to 10,500 ppm (equivalent to 4,565 ppm/(m2/g)).
- the material was removed from the reactor and subjected to dissolution in deionized water.
- the solid phase was leached with an aqueous solution containing HCl and HF for 90 minutes. This mixture was then filtered and rinsed with 10 liters of deionized water. The cake obtained from filtration was subsequently vacuum-dried.
- the chemical analysis of the obtained powder evidenced that the oxygen content had fallen from 39,620 ppm to 6,700 ppm (equivalent to 4,188 ppm/(m2/g)).
- Example 5 The oxidized powder (11 g) was placed on a metallic screen, attached to the support stem (11), inside a crucible 1, as shown in Figure 2.
- the metallic magnesium (25 g) was placed in the reducer container (Ca/Mg, NbH), also attached to the support stem (2).
- the mixture of calcium chloride (240 g) and potassium chloride (60 g) was placed inside the crucible, together with the oxidized powder and the metallic magnesium.
- the crucible was sealed, there being welded a cover thereon.
- the mixture was heated to a temperature of 900° C for 2 hours. After the reduction, the mixture was cooled down to ambient temperature.
- the material was removed from the crucible and dissolved in deionized water.
- the solid phase was leached with an aqueous solution containing HCl and HF for 90 minutes. This mixture was then filtered and rinsed with deionized water.
- the cake obtained from filtration was subsequently vacuum-dried.
- the chemical analysis of the obtained powder evidenced that the oxygen content had fallen from 52,210 ppm to 5,850 ppm (equivalent to 3,250 ppm/(m2/g)).
- the oxidized powder (11 g) was placed on a metallic screen, attached to the support stem (11), inside a crucible (1), as shown in Figure 2.
- the metallic calcium (25 g) was placed in the reducer container (Ca/Mg, NbH), also attached to the support stem.
- the calcium chloride (300 g) was placed inside the crucible, together with the oxidized powder and the metallic calcium.
- the crucible was sealed, there being welded a cover thereon.
- the mixture was heated to a temperature of 900° C for 2 hours. After the reduction, the mixture was cooled down to ambient temperature.
- the material was removed from the crucible and dissolved in deionized water.
- the solid phase was leached with an aqueous solution containing HCl and HF for 90 minutes. This mixture was then filtered and rinsed with deionized water.
- the cake obtained from filtration was subsequently vacuum-dried.
- the chemical analysis of the obtained powder evidenced that the oxygen content had fallen from 52,210 ppm to 5,520 ppm (equivalent to 3,070 ppm/(m2/g)).
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- Mechanical Engineering (AREA)
- Materials Engineering (AREA)
- Manufacturing & Machinery (AREA)
- General Life Sciences & Earth Sciences (AREA)
- Environmental & Geological Engineering (AREA)
- Geology (AREA)
- Life Sciences & Earth Sciences (AREA)
- Power Engineering (AREA)
- General Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
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- Manufacture Of Metal Powder And Suspensions Thereof (AREA)
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Abstract
Priority Applications (5)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB0508844A GB2409466B (en) | 2002-11-04 | 2003-08-27 | A process for the production of niobium and/or tantalum powder with large surface area |
JP2004548947A JP2006516039A (ja) | 2002-11-04 | 2003-08-27 | 大きな表面積を有するニオブ粉末及び/又はタンタル粉末の製造方法 |
DE10393407T DE10393407T5 (de) | 2002-11-04 | 2003-08-27 | Ein Verfahren zur Herstellung von Niob- und/oder Tantalpulver mit großer Oberfläche |
AU2003254646A AU2003254646A1 (en) | 2002-11-04 | 2003-08-27 | A process for the production of niobium and/or tantalum powder with large surface area |
US10/533,791 US20060096418A1 (en) | 2002-11-04 | 2003-08-27 | Process for the production of niobium and/or tantalum powder with large surface area |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
BRPI0204587-7 | 2002-11-04 | ||
BR0204587-7A BR0204587A (pt) | 2002-11-04 | 2002-11-04 | Processo de produção de pó de nióbio e/ou de tântalo de elevada área superficial |
Publications (1)
Publication Number | Publication Date |
---|---|
WO2004042095A1 true WO2004042095A1 (fr) | 2004-05-21 |
Family
ID=32303987
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PCT/BR2003/000122 WO2004042095A1 (fr) | 2002-11-04 | 2003-08-27 | Procede servant a preparer de la poudre de niobium et/ou de tantale presentant une surface importante |
Country Status (8)
Country | Link |
---|---|
US (1) | US20060096418A1 (fr) |
JP (1) | JP2006516039A (fr) |
CN (1) | CN1694973A (fr) |
AU (1) | AU2003254646A1 (fr) |
BR (1) | BR0204587A (fr) |
DE (1) | DE10393407T5 (fr) |
GB (1) | GB2409466B (fr) |
WO (1) | WO2004042095A1 (fr) |
Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2005028370A1 (fr) * | 2003-09-25 | 2005-03-31 | Companhia Brasileira De Metalurgia E Mineracão | Methode de production d'une poudre d'oxyde de niobium utilisable dans des capacites |
DE102004043343A1 (de) * | 2004-09-08 | 2006-03-23 | H.C. Starck Gmbh | Desoxidation von Ventilmetallpulvern |
WO2006101850A1 (fr) * | 2005-03-22 | 2006-09-28 | H.C. Stark Inc. | Methode de preparation d’un metal refractaire de premiere fusion |
US8999500B2 (en) | 2006-08-16 | 2015-04-07 | H.C. Starck Gmbh | Semifinished products with a structured sinter-active surface and a process for their production |
US9393623B2 (en) | 2009-02-13 | 2016-07-19 | Metalysis Limited | Method for producing metal powders |
US10081847B2 (en) | 2012-10-17 | 2018-09-25 | University Of Bradford | Method for metal production |
Families Citing this family (6)
Publication number | Priority date | Publication date | Assignee | Title |
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JP3610942B2 (ja) * | 2001-10-12 | 2005-01-19 | 住友金属鉱山株式会社 | ニオブおよび/またはタンタルの粉末の製造法 |
EP2709784A4 (fr) * | 2011-05-16 | 2015-11-18 | Boston Electronic Materials Llc | Fabrication et applications de poudres et alliages métalliques |
KR101911871B1 (ko) * | 2016-12-23 | 2018-10-29 | 한국기초과학지원연구원 | 탄탈륨 분말의 제조방법 |
CN108217596B (zh) * | 2018-01-29 | 2021-03-30 | 吉林大学 | 使用非氢源溶液法制备铌氢化物和钽氢化物的方法 |
KR102359159B1 (ko) * | 2019-12-30 | 2022-02-08 | 충남대학교산학협력단 | 연소 반응을 이용한 금속 나노분말 제조방법 |
CN113500204A (zh) * | 2021-07-08 | 2021-10-15 | 安徽理工大学 | 一种氯化钙熔盐中钙热还原氯化铌制备细微铌粉的方法 |
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DE19831280A1 (de) | 1998-07-13 | 2000-01-20 | Starck H C Gmbh Co Kg | Verfahren zur Herstellung von Erdsäuremetallpulvern, insbesondere Niobpulvern |
WO2000015555A1 (fr) | 1998-09-16 | 2000-03-23 | Cabot Corporation | Procedes permettant de reduire partiellement un oxyde metallique de niobium et oxydes de niobium a reduction d'oxygene a teneur reduite en oxygene |
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JP2001143970A (ja) * | 1999-11-16 | 2001-05-25 | Showa Kyabotto Super Metal Kk | タンタル粉末およびその製造方法と、このタンタル粉末を用いた多孔質焼結体および固体電解コンデンサー |
JP2004052003A (ja) * | 2002-07-16 | 2004-02-19 | Cabot Supermetal Kk | ニオブ粉末またはタンタル粉末の製造方法および製造装置 |
-
2002
- 2002-11-04 BR BR0204587-7A patent/BR0204587A/pt not_active IP Right Cessation
-
2003
- 2003-08-27 US US10/533,791 patent/US20060096418A1/en not_active Abandoned
- 2003-08-27 AU AU2003254646A patent/AU2003254646A1/en not_active Abandoned
- 2003-08-27 DE DE10393407T patent/DE10393407T5/de not_active Withdrawn
- 2003-08-27 CN CNA038248115A patent/CN1694973A/zh active Pending
- 2003-08-27 GB GB0508844A patent/GB2409466B/en not_active Expired - Lifetime
- 2003-08-27 WO PCT/BR2003/000122 patent/WO2004042095A1/fr active Application Filing
- 2003-08-27 JP JP2004548947A patent/JP2006516039A/ja active Pending
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US1728941A (en) | 1927-02-19 | 1929-09-24 | Westinghouse Lamp Co | Production of rare metals |
US2516863A (en) | 1946-07-15 | 1950-08-01 | Gardner Daniel | Process of producing tantalum, columbium, and compounds thereof |
US4487677A (en) * | 1983-04-11 | 1984-12-11 | Metals Production Research, Inc. | Electrolytic recovery system for obtaining titanium metal from its ore |
US4687632A (en) | 1984-05-11 | 1987-08-18 | Hurd Frank W | Metal or alloy forming reduction process and apparatus |
US4725312A (en) | 1986-02-28 | 1988-02-16 | Rhone-Poulenc Chimie | Production of metals by metallothermia |
US4684399A (en) | 1986-03-04 | 1987-08-04 | Cabot Corporation | Tantalum powder process |
US4923531A (en) * | 1988-09-23 | 1990-05-08 | Rmi Company | Deoxidation of titanium and similar metals using a deoxidant in a molten metal carrier |
GB2233349A (en) * | 1989-06-26 | 1991-01-09 | Cabot Corp | Powders and products of tantalum, niobium and their alloys |
US5234491A (en) * | 1990-05-17 | 1993-08-10 | Cabot Corporation | Method of producing high surface area, low metal impurity |
US6171363B1 (en) | 1998-05-06 | 2001-01-09 | H. C. Starck, Inc. | Method for producing tantallum/niobium metal powders by the reduction of their oxides with gaseous magnesium |
DE19831280A1 (de) | 1998-07-13 | 2000-01-20 | Starck H C Gmbh Co Kg | Verfahren zur Herstellung von Erdsäuremetallpulvern, insbesondere Niobpulvern |
WO2000015555A1 (fr) | 1998-09-16 | 2000-03-23 | Cabot Corporation | Procedes permettant de reduire partiellement un oxyde metallique de niobium et oxydes de niobium a reduction d'oxygene a teneur reduite en oxygene |
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WO2001059166A1 (fr) | 2000-02-08 | 2001-08-16 | Cabot Super Metals K.K. | Production de poudres azotees de tantale ou de niobium et condensateur a electrolyte solide |
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Cited By (10)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2005028370A1 (fr) * | 2003-09-25 | 2005-03-31 | Companhia Brasileira De Metalurgia E Mineracão | Methode de production d'une poudre d'oxyde de niobium utilisable dans des capacites |
GB2421945A (en) * | 2003-09-25 | 2006-07-12 | Cbmm Sa | A process for the production of niobium oxide power for use in capacitors |
DE102004043343A1 (de) * | 2004-09-08 | 2006-03-23 | H.C. Starck Gmbh | Desoxidation von Ventilmetallpulvern |
WO2006101850A1 (fr) * | 2005-03-22 | 2006-09-28 | H.C. Stark Inc. | Methode de preparation d’un metal refractaire de premiere fusion |
US7399335B2 (en) | 2005-03-22 | 2008-07-15 | H.C. Starck Inc. | Method of preparing primary refractory metal |
AU2006227768B2 (en) * | 2005-03-22 | 2011-10-13 | H.C. Starck Gmbh | Method of preparing primary refractory metal |
US8999500B2 (en) | 2006-08-16 | 2015-04-07 | H.C. Starck Gmbh | Semifinished products with a structured sinter-active surface and a process for their production |
US9393623B2 (en) | 2009-02-13 | 2016-07-19 | Metalysis Limited | Method for producing metal powders |
US9579725B2 (en) | 2009-02-13 | 2017-02-28 | Metalysis Limited | Method for producing metal powders |
US10081847B2 (en) | 2012-10-17 | 2018-09-25 | University Of Bradford | Method for metal production |
Also Published As
Publication number | Publication date |
---|---|
CN1694973A (zh) | 2005-11-09 |
GB0508844D0 (en) | 2005-06-08 |
US20060096418A1 (en) | 2006-05-11 |
BR0204587A (pt) | 2004-06-29 |
DE10393407T5 (de) | 2005-10-06 |
GB2409466B (en) | 2006-06-21 |
AU2003254646A1 (en) | 2004-06-07 |
JP2006516039A (ja) | 2006-06-15 |
GB2409466A (en) | 2005-06-29 |
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