US2111470A - Process for electrolytic preparation of alkaline-earth alloys - Google Patents
Process for electrolytic preparation of alkaline-earth alloys Download PDFInfo
- Publication number
- US2111470A US2111470A US75240A US7524036A US2111470A US 2111470 A US2111470 A US 2111470A US 75240 A US75240 A US 75240A US 7524036 A US7524036 A US 7524036A US 2111470 A US2111470 A US 2111470A
- Authority
- US
- United States
- Prior art keywords
- calcium
- alkaline earth
- bath
- alkaline
- electrolysis
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Lifetime
Links
- 229910045601 alloy Inorganic materials 0.000 title description 9
- 239000000956 alloy Substances 0.000 title description 9
- 238000000034 method Methods 0.000 title description 4
- 238000002360 preparation method Methods 0.000 title description 4
- 229910052791 calcium Inorganic materials 0.000 description 15
- 239000011575 calcium Substances 0.000 description 15
- OYPRJOBELJOOCE-UHFFFAOYSA-N Calcium Chemical compound [Ca] OYPRJOBELJOOCE-UHFFFAOYSA-N 0.000 description 14
- 229910052784 alkaline earth metal Inorganic materials 0.000 description 12
- 150000001342 alkaline earth metals Chemical class 0.000 description 12
- 238000005868 electrolysis reaction Methods 0.000 description 11
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 9
- 229910052799 carbon Inorganic materials 0.000 description 9
- 229910001385 heavy metal Inorganic materials 0.000 description 8
- UXVMQQNJUSDDNG-UHFFFAOYSA-L Calcium chloride Chemical compound [Cl-].[Cl-].[Ca+2] UXVMQQNJUSDDNG-UHFFFAOYSA-L 0.000 description 7
- 239000001110 calcium chloride Substances 0.000 description 7
- 229910001628 calcium chloride Inorganic materials 0.000 description 7
- 235000011148 calcium chloride Nutrition 0.000 description 7
- WUKWITHWXAAZEY-UHFFFAOYSA-L calcium difluoride Chemical compound [F-].[F-].[Ca+2] WUKWITHWXAAZEY-UHFFFAOYSA-L 0.000 description 7
- 229910001634 calcium fluoride Inorganic materials 0.000 description 7
- 235000008733 Citrus aurantifolia Nutrition 0.000 description 5
- 235000011941 Tilia x europaea Nutrition 0.000 description 5
- 229910052788 barium Inorganic materials 0.000 description 5
- DSAJWYNOEDNPEQ-UHFFFAOYSA-N barium atom Chemical compound [Ba] DSAJWYNOEDNPEQ-UHFFFAOYSA-N 0.000 description 5
- 239000011133 lead Substances 0.000 description 5
- 239000004571 lime Substances 0.000 description 5
- 239000000203 mixture Substances 0.000 description 5
- 229910052712 strontium Inorganic materials 0.000 description 5
- CIOAGBVUUVVLOB-UHFFFAOYSA-N strontium atom Chemical compound [Sr] CIOAGBVUUVVLOB-UHFFFAOYSA-N 0.000 description 5
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 4
- HCHKCACWOHOZIP-UHFFFAOYSA-N Zinc Chemical compound [Zn] HCHKCACWOHOZIP-UHFFFAOYSA-N 0.000 description 4
- 229910052802 copper Inorganic materials 0.000 description 4
- 239000010949 copper Substances 0.000 description 4
- 239000003792 electrolyte Substances 0.000 description 4
- 238000004519 manufacturing process Methods 0.000 description 4
- 229910052725 zinc Inorganic materials 0.000 description 4
- 239000011701 zinc Substances 0.000 description 4
- VEXZGXHMUGYJMC-UHFFFAOYSA-M Chloride anion Chemical compound [Cl-] VEXZGXHMUGYJMC-UHFFFAOYSA-M 0.000 description 3
- FYYHWMGAXLPEAU-UHFFFAOYSA-N Magnesium Chemical compound [Mg] FYYHWMGAXLPEAU-UHFFFAOYSA-N 0.000 description 3
- OMRRUNXAWXNVFW-UHFFFAOYSA-N fluoridochlorine Chemical compound ClF OMRRUNXAWXNVFW-UHFFFAOYSA-N 0.000 description 3
- 239000011777 magnesium Substances 0.000 description 3
- VTYYLEPIZMXCLO-UHFFFAOYSA-L Calcium carbonate Chemical compound [Ca+2].[O-]C([O-])=O VTYYLEPIZMXCLO-UHFFFAOYSA-L 0.000 description 2
- BVKZGUZCCUSVTD-UHFFFAOYSA-L Carbonate Chemical compound [O-]C([O-])=O BVKZGUZCCUSVTD-UHFFFAOYSA-L 0.000 description 2
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 2
- 229910000287 alkaline earth metal oxide Inorganic materials 0.000 description 2
- 230000015572 biosynthetic process Effects 0.000 description 2
- 150000001875 compounds Chemical class 0.000 description 2
- 229910052749 magnesium Inorganic materials 0.000 description 2
- 238000007670 refining Methods 0.000 description 2
- QTBSBXVTEAMEQO-UHFFFAOYSA-M Acetate Chemical compound CC([O-])=O QTBSBXVTEAMEQO-UHFFFAOYSA-M 0.000 description 1
- 229910000838 Al alloy Inorganic materials 0.000 description 1
- 229910000600 Ba alloy Inorganic materials 0.000 description 1
- OYPRJOBELJOOCE-IGMARMGPSA-N Calcium-40 Chemical compound [40Ca] OYPRJOBELJOOCE-IGMARMGPSA-N 0.000 description 1
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 description 1
- 229910052684 Cerium Inorganic materials 0.000 description 1
- ZAMOUSCENKQFHK-UHFFFAOYSA-N Chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 description 1
- 229910000861 Mg alloy Inorganic materials 0.000 description 1
- MUBZPKHOEPUJKR-UHFFFAOYSA-N Oxalic acid Chemical compound OC(=O)C(O)=O MUBZPKHOEPUJKR-UHFFFAOYSA-N 0.000 description 1
- 229910001278 Sr alloy Inorganic materials 0.000 description 1
- FDVHJVDLITXALC-UHFFFAOYSA-N [Ca].ClF Chemical group [Ca].ClF FDVHJVDLITXALC-UHFFFAOYSA-N 0.000 description 1
- 229910000941 alkaline earth metal alloy Inorganic materials 0.000 description 1
- 239000004411 aluminium Substances 0.000 description 1
- 229910052782 aluminium Inorganic materials 0.000 description 1
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 229910000019 calcium carbonate Inorganic materials 0.000 description 1
- HAUBPZADNMBYMB-UHFFFAOYSA-N calcium copper Chemical compound [Ca].[Cu] HAUBPZADNMBYMB-UHFFFAOYSA-N 0.000 description 1
- BRPQOXSCLDDYGP-UHFFFAOYSA-N calcium oxide Chemical compound [O-2].[Ca+2] BRPQOXSCLDDYGP-UHFFFAOYSA-N 0.000 description 1
- 239000000292 calcium oxide Substances 0.000 description 1
- ODINCKMPIJJUCX-UHFFFAOYSA-N calcium oxide Inorganic materials [Ca]=O ODINCKMPIJJUCX-UHFFFAOYSA-N 0.000 description 1
- 229910002091 carbon monoxide Inorganic materials 0.000 description 1
- ZMIGMASIKSOYAM-UHFFFAOYSA-N cerium Chemical compound [Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce] ZMIGMASIKSOYAM-UHFFFAOYSA-N 0.000 description 1
- 239000000460 chlorine Substances 0.000 description 1
- 229910052801 chlorine Inorganic materials 0.000 description 1
- 150000001805 chlorine compounds Chemical class 0.000 description 1
- 238000000354 decomposition reaction Methods 0.000 description 1
- 230000007717 exclusion Effects 0.000 description 1
- 229910052500 inorganic mineral Inorganic materials 0.000 description 1
- 229910052742 iron Inorganic materials 0.000 description 1
- 239000002142 lead-calcium alloy Substances 0.000 description 1
- 229910001234 light alloy Inorganic materials 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 238000002844 melting Methods 0.000 description 1
- 230000008018 melting Effects 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 239000011707 mineral Substances 0.000 description 1
- 235000010755 mineral Nutrition 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 229920000136 polysorbate Polymers 0.000 description 1
- 229920006395 saturated elastomer Polymers 0.000 description 1
- 239000000243 solution Substances 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25C—PROCESSES FOR THE ELECTROLYTIC PRODUCTION, RECOVERY OR REFINING OF METALS; APPARATUS THEREFOR
- C25C3/00—Electrolytic production, recovery or refining of metals by electrolysis of melts
Definitions
- Patented Mar. 15, 1938 1 UNITED STATES PATENT OFFICE PROCESS FOR ELECTROLYTIC PREPARA TION OF ALKALINE-EARTH ALLOYS Robert Andre Gadeau, Saint Jean De Maurienne,
- the process accof'ding to the invention is particularly applicable to the manufacture of alloys of the alkaline earth metals with heavy metals like lead, 'copper, zinc, etc.
- a bath with bottom made of carbon and walls made of carbon or refractory/ material contains at the bottom the molten eavy-metal, which forms the cathode; the anode is a carbon rod which dips into the electrolyteflconsisting of alkaline earth chloro-fluoride, to which from time to time alkaline earth oxide is-added. The oxide becomes electrolyzed; the alkaline earth metal alloys itself with the heavy metal of the cathode, the oxygen burns away the anode, with evolution of carbon monoxide.
- a suitable electrolyte for the preparation of calcium is calcium chloro-fluoride CaClz.CaF2, i. e., a mixture of approximately percent by weight of calcium chloride and 40 percent by' weight of calcium fluoride, in which lime is dissolved.
- the invention however is not limited to that composition; there is no objection to adding an excess of calcium fluoride.
- the only limitation is by the rise of the melting point of the mixture, which is at 950 with 50 percent by weight of calcium fluoride.
- the molte bath is electrolyzed at 6 to 8 volts tension b tween carbon an- .odes and a cathode layer of mo ten lead, which is disposed at the bottom of the bath, wherein the working temperature amounts to about 800".
- the working temperature amounts to about 800".
- alkaline earth metals calcium, barium and strontium to the exclusion of magnesium, the properties of the last differing entirely, from the point of view of electrolysis and the point of view of chemistry from those of calcium, barium and strontium.
- a method of manufacturing an alloy of an alkaline earth metal of the group consisting of calcium, barium and strontium with a heavy metal of the group consisting of lead, zinc and copper, by electrolysis with a carbon anode and a cathode consisting of said heavy metal in the fused state which comprises dissolving a carbonate of said alkaline earth metal in a fused chloro-fiuoride of said alkaline earth metal, to give off by the heat of said chloro-fiuorlde the oxide of said alkaline earth metal, and electrolyzing the fused bath thus obtained.
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- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Electrochemistry (AREA)
- Materials Engineering (AREA)
- Metallurgy (AREA)
- Organic Chemistry (AREA)
- Electrolytic Production Of Metals (AREA)
Description
Patented Mar. 15, 1938 1 UNITED STATES PATENT OFFICE PROCESS FOR ELECTROLYTIC PREPARA TION OF ALKALINE-EARTH ALLOYS Robert Andre Gadeau, Saint Jean De Maurienne,
France, assignor' to Chimiques Compagni'e dc Produits et Electrometallurgiques Alais,
Froges et Camargue, Paris, France, a corporation of France No Drawing. ,Application April 18, 1936, Serial No. 75,240. In Germany May 27, 1935 3 Claims.
which contain the corresponding oxide in solu-- tion. The process appears valuable for the prep-.
aration of cerium, but it could never be applied for the preparation of the alkaline earth metals. My experiments have shown'that the electrolysis of a molten bath of calcium chloride, which contains dissolved lime, leads at once to the formation'of a thick slime, which makes the electrolysis as good as impossible. Moreover it is known that the basic chlorides of calcium dissolve metallic calcium, whereby slimy masses are formed and the resistance of the bath is increased. Since the decomposition voltages of calcium oxide and calcium chloride lie close to one another, there takes place, in a molten bath of these two compounds, always in part an electrolysis of the chloride, even if the bath is saturated with lime, which manifests itself in a troublesome evolution of; chlorine and a costly consumption of chloride.
I have found, and'this is the essential char- 3() acteristic of the present invention, that all these difficulties are avoided and that it is possible easily toobtain alkaline earth metals by electrolysis of their oxides, provided that an alkaline earth chloro-fluoride is utilized as oxide-dissolving electrolyte.
My experiments have shown that in an electrolyte, of which the composition corresponds for example to the formula CaCl2.CaFz, the properties of calcium chloride are so far concealed,-
40 that no appreciable volatilization of the bath takes place at about 800, the chloride no longer takes part in the electrolysis and the hath no longer dissolves any appreciable quantity of metallic calcium, whereby the formation of a *slimeof basic subsalts is suppressed.
The process accof'ding to the invention is particularly applicable to the manufacture of alloys of the alkaline earth metals with heavy metals like lead, 'copper, zinc, etc. A bath with bottom made of carbon and walls made of carbon or refractory/ material contains at the bottom the molten eavy-metal, which forms the cathode; the anode is a carbon rod which dips into the electrolyteflconsisting of alkaline earth chloro-fluoride, to which from time to time alkaline earth oxide is-added. The oxide becomes electrolyzed; the alkaline earth metal alloys itself with the heavy metal of the cathode, the oxygen burns away the anode, with evolution of carbon monoxide.
A suitable electrolyte for the preparation of calcium is calcium chloro-fluoride CaClz.CaF2, i. e., a mixture of approximately percent by weight of calcium chloride and 40 percent by' weight of calcium fluoride, in which lime is dissolved. The invention however is not limited to that composition; there is no objection to adding an excess of calcium fluoride. The only limitation is by the rise of the melting point of the mixture, which is at 950 with 50 percent by weight of calcium fluoride. One may also be satisfied with a lower content-of calcium fluoride; I have indeed ascertained that calcium chloride was already stabilized substantially by 10 to 20 percent by weight of calcium fluoride. added periodically, the molte bath is electrolyzed at 6 to 8 volts tension b tween carbon an- .odes and a cathode layer of mo ten lead, which is disposed at the bottom of the bath, wherein the working temperature amounts to about 800". In this waythere is obtained, with a current yield of-' 50 percent, a lead-calcium alloy, in which the calcium is extremely cheap, and which can be utilized as it is for numerous applications.
It is to be quite understood that the invention is not limited to theexample mentioned; in the same way there can be produced various other alloys other than lead-calcium, for example zinccalcium, copper-calcium and so on. I The process is also applicable under the same conditions to the preparation of alloys of barium and of strontium.
Lastly, it is possible to maintain the electrolysis not with an alkaline earth oxide, but with a compound.whicl'rforms the oxide under the in- While lime is fluence of heat, for example with .a carbonate,
oxalate, acetate, and so on. In particular it is of advantage, for example, to prepare calciumfrom calcium carbonate, consequently an extremely cheap mineral.
I have found that pure calcium can be easily,
prepared by electrolytic refining of its heavy alloys which have been obtained according to the present invention. For this the same electrolyte is very well suited; the poles of the bath can therefore be reversed and the carbon electrode replaced for example by a cooled iron cathode, upon which a tube of calcium is then, obtained. I
I have found further that by electrolytic refining of the heavy alloys, prepared according to the present invention, also alloys of aluminium and magnesium with calcium can be easily prepared. It suffices to reverse the poles of the bath and to dispose on the surface of the bath a molten cathode layer of aluminium or magnesium, into which the current is led by a carbon electrode. Electrolysis at a voltage of a few volts causes the calcium of the heavy alloy at the anode to pass into the light alloy at the cathode, with a current yield ofapproximately 100 percent. In the foregoing description and in the claims, there should be understood by the term alkaline earth metals calcium, barium and strontium, to the exclusion of magnesium, the properties of the last differing entirely, from the point of view of electrolysis and the point of view of chemistry from those of calcium, barium and strontium.
What I claim is:
l. A-method of manufacturing an alloy of an alkaline earth metal of the group consisting of calcium, barium and strontium with a heavy metal of the group consisting of lead, zinc and copper, by electrolysis with a carbon anode and a cathode consisting of said fused heavy metal, which comprises dissolving an oxide of said alkaline earth metal in a fused chloro-fluoride of said alkaline earth metal, and electrolyzing the fused bath thus obtained.
2. A method of manufacturing an alloy of an alkaline earth metal of the group consisting of calcium, barium and strontium with a heavy metal of the group consisting of lead, zinc and copper, by electrolysis with a carbon anode and a cathode consisting of said heavy metal in the fused state, which comprises dissolving a carbonate of said alkaline earth metal in a fused chloro-fiuoride of said alkaline earth metal, to give off by the heat of said chloro-fiuorlde the oxide of said alkaline earth metal, and electrolyzing the fused bath thus obtained.
3. A method of manufacturing an alloy of an alkaline earth metal of the group consisting of calcium, barium and strontium with a heavy metal of the group consisting of zinc, lead and copper, by electrolysis with a carbon anode and a cathode consisting of said heavy metal in the fused state, which comprises dissolving lime in a mixture of from 90 to 40 per cent in weight of fused calcium chloride and from 10 to 60 per cent in weight of fused calcium fluoride, and electrolyzing the fused bath thus obtained.
ROBERT ANDRE GADEAU.
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| DE2111470X | 1935-05-27 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US2111470A true US2111470A (en) | 1938-03-15 |
Family
ID=7985454
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US75240A Expired - Lifetime US2111470A (en) | 1935-05-27 | 1936-04-18 | Process for electrolytic preparation of alkaline-earth alloys |
Country Status (1)
| Country | Link |
|---|---|
| US (1) | US2111470A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2913382A (en) * | 1957-01-28 | 1959-11-17 | Union Carbide Corp | Method for producing metals electrolytically |
-
1936
- 1936-04-18 US US75240A patent/US2111470A/en not_active Expired - Lifetime
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2913382A (en) * | 1957-01-28 | 1959-11-17 | Union Carbide Corp | Method for producing metals electrolytically |
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