Methods for reducing impurities in magnesium, purified magnesium, and zirconium metal production methods
US-2015329939-A1 · Nov 19, 2015 · US
US10422017B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10422017-B2 |
| Application number | US-201816041928-A |
| Country | US |
| Kind code | B2 |
| Filing date | Jul 23, 2018 |
| Priority date | Aug 14, 2012 |
| Publication date | Sep 24, 2019 |
| Grant date | Sep 24, 2019 |
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A method for reducing impurities in magnesium comprises: combining a zirconium-containing material with a molten low-impurity magnesium including no more than 1.0 weight percent of total impurities in a vessel to provide a mixture; holding the mixture in a molten state for a period of time sufficient to allow at least a portion of the zirconium-containing material to react with at least a portion of the impurities and form intermetallic compounds; and separating at least a portion of the molten magnesium in the mixture from at least a portion of the intermetallic compounds to provide a purified magnesium, wherein the purified magnesium includes an increased level of zirconium compared to the low-impurity magnesium, wherein the purified magnesium includes greater than 1000 ppm zirconium, and wherein the purified magnesium includes a reduced level of impurities other than zirconium compared to the low-impurity magnesium. A purified magnesium including at least 1000 ppm zirconium and methods for producing zirconium metal using magnesium reductant also are disclosed.
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What is claimed is: 1. A method of producing zirconium metal, the method comprising: reacting zirconium tetrachloride with magnesium reductant, wherein the magnesium reductant comprises greater than 1000 up to 3000 ppm zirconium, 0 to 0.007 weight percent aluminum, no more than 50 ppm hafnium, and 0 to 0.005 weight percent nitrogen, to provide reaction products comprising zirconium metal and magnesium chloride salt; and separating at least a portion of the zirconium metal from the reaction products. 2. The method of claim 1 , wherein the magnesium reductant consists essentially of: greater than 1000 up to 3000 ppm zirconium; magnesium; 0 to 0.007 weight percent aluminum; 0 to 0.0001 weight percent boron; 0 to 0.002 weight percent cadmium; 0 to 0.003 weight percent hafnium; 0 to 0.06 weight percent iron; 0 to 0.01 weight percent manganese; 0 to 0.005 weight percent nitrogen; 0 to 0.005 weight percent phosphorus; and 0 to 0.02 weight percent titanium. 3. The method of claim 1 , wherein the magnesium reductant consists of: 1000 to 3000 ppm zirconium; magnesium; no more than 50 ppm hafnium; 0 to 0.005 weight percent nitrogen; and incidental impurities. 4. The method of claim 1 , wherein the magnesium reductant consists of: 1000 to 3000 ppm zirconium; magnesium; 0 to 0.007 weight percent aluminum; 0 to 0.0001 weight percent boron; 0 to 0.002 weight percent cadmium; 0 to 0.003 weight percent hafnium; 0 to 0.06 weight percent iron; 0 to 0.01 weight percent manganese; 0 to 0.005 weight percent nitrogen; 0 to 0.005 weight percent phosphorus; and 0 to 0.02 weight percent titanium. 5. The method of claim 1 , wherein reacting zirconium tetrachloride with magnesium reductant to provide reaction products comprises melting the magnesium reductant in a first chamber and subliming the zirconium tetrachloride in a second chamber, and allowing zirconium tetrachloride vapors to contact and react with molten magnesium and produce the reaction products. 6. The method of claim 1 , wherein the reaction products comprise a layer consisting primarily of zirconium metal and a layer consisting primarily of magnesium chloride salt, and further wherein the two layers are separated. 7. The method of claim 6 , wherein the separated layer consisting primarily of zirconium metal is distilled under vacuum to remove residual salt, providing zirconium sponge including porosity from vacancies left by removed magnesium chloride.
with refining or fluxing agents; Use of materials therefor, {e.g. slagging or scorifying agents}(C22B9/18 takes precedence){(C22B9/006 takes precedence)} · CPC title
Alloys based on magnesium · CPC title
Obtaining zirconium or hafnium {(treatment or purification of solutions by liquid-liquid extraction, by ion exchange or by adsorption C22B3/00, C01G25/003, C01G27/003)} · CPC title
Obtaining magnesium · CPC title
with aluminium as the next major constituent · CPC title
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