US1951494A - Electrolysis of anhydrous fused metal chlorides - Google Patents
Electrolysis of anhydrous fused metal chlorides Download PDFInfo
- Publication number
- US1951494A US1951494A US528452A US52845231A US1951494A US 1951494 A US1951494 A US 1951494A US 528452 A US528452 A US 528452A US 52845231 A US52845231 A US 52845231A US 1951494 A US1951494 A US 1951494A
- Authority
- US
- United States
- Prior art keywords
- electrolysis
- chlorine
- anhydrous
- chlorides
- metal chlorides
- 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
- 238000005868 electrolysis reaction Methods 0.000 title description 15
- 229910001510 metal chloride Inorganic materials 0.000 title description 7
- TWRXJAOTZQYOKJ-UHFFFAOYSA-L Magnesium chloride Chemical compound [Mg+2].[Cl-].[Cl-] TWRXJAOTZQYOKJ-UHFFFAOYSA-L 0.000 description 14
- KZBUYRJDOAKODT-UHFFFAOYSA-N Chlorine Chemical compound ClCl KZBUYRJDOAKODT-UHFFFAOYSA-N 0.000 description 11
- ZAMOUSCENKQFHK-UHFFFAOYSA-N Chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 description 11
- 229910052801 chlorine Inorganic materials 0.000 description 11
- 239000000460 chlorine Substances 0.000 description 11
- FYYHWMGAXLPEAU-UHFFFAOYSA-N Magnesium Chemical compound [Mg] FYYHWMGAXLPEAU-UHFFFAOYSA-N 0.000 description 7
- 150000001805 chlorine compounds Chemical class 0.000 description 7
- 239000003792 electrolyte Substances 0.000 description 6
- 229910052749 magnesium Inorganic materials 0.000 description 4
- 239000011777 magnesium Substances 0.000 description 4
- 229910001629 magnesium chloride Inorganic materials 0.000 description 4
- 238000004519 manufacturing process Methods 0.000 description 4
- 238000000034 method Methods 0.000 description 4
- 238000006243 chemical reaction Methods 0.000 description 3
- 239000012535 impurity Substances 0.000 description 3
- 229910052751 metal Inorganic materials 0.000 description 3
- 239000002184 metal Substances 0.000 description 3
- 239000002245 particle Substances 0.000 description 3
- 238000002360 preparation method Methods 0.000 description 3
- VEXZGXHMUGYJMC-UHFFFAOYSA-M Chloride anion Chemical compound [Cl-] VEXZGXHMUGYJMC-UHFFFAOYSA-M 0.000 description 2
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 2
- FPIPGXGPPPQFEQ-OVSJKPMPSA-N all-trans-retinol Chemical compound OC\C=C(/C)\C=C\C=C(/C)\C=C\C1=C(C)CCCC1(C)C FPIPGXGPPPQFEQ-OVSJKPMPSA-N 0.000 description 2
- 239000004411 aluminium Substances 0.000 description 2
- 229910052782 aluminium Inorganic materials 0.000 description 2
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 2
- VSCWAEJMTAWNJL-UHFFFAOYSA-K aluminium trichloride Chemical compound Cl[Al](Cl)Cl VSCWAEJMTAWNJL-UHFFFAOYSA-K 0.000 description 2
- 239000000428 dust Substances 0.000 description 2
- 239000007789 gas Substances 0.000 description 2
- 239000000395 magnesium oxide Substances 0.000 description 2
- CPLXHLVBOLITMK-UHFFFAOYSA-N magnesium oxide Inorganic materials [Mg]=O CPLXHLVBOLITMK-UHFFFAOYSA-N 0.000 description 2
- AXZKOIWUVFPNLO-UHFFFAOYSA-N magnesium;oxygen(2-) Chemical compound [O-2].[Mg+2] AXZKOIWUVFPNLO-UHFFFAOYSA-N 0.000 description 2
- 229910044991 metal oxide Inorganic materials 0.000 description 2
- 150000004706 metal oxides Chemical class 0.000 description 2
- 150000002739 metals Chemical class 0.000 description 2
- 238000000746 purification Methods 0.000 description 2
- 239000002994 raw material Substances 0.000 description 2
- XPYQFIISZQCINN-QVXDJYSKSA-N 4-amino-1-[(2r,3e,4s,5r)-3-(fluoromethylidene)-4-hydroxy-5-(hydroxymethyl)oxolan-2-yl]pyrimidin-2-one;hydrate Chemical compound O.O=C1N=C(N)C=CN1[C@H]1C(=C/F)/[C@H](O)[C@@H](CO)O1 XPYQFIISZQCINN-QVXDJYSKSA-N 0.000 description 1
- OYPRJOBELJOOCE-UHFFFAOYSA-N Calcium Chemical compound [Ca] OYPRJOBELJOOCE-UHFFFAOYSA-N 0.000 description 1
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- 239000011717 all-trans-retinol Substances 0.000 description 1
- 235000019169 all-trans-retinol Nutrition 0.000 description 1
- 239000010425 asbestos Substances 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 229910052791 calcium Inorganic materials 0.000 description 1
- 239000011575 calcium Substances 0.000 description 1
- -1 calcium and the like Chemical class 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 238000011109 contamination Methods 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 125000004122 cyclic group Chemical group 0.000 description 1
- 238000000354 decomposition reaction Methods 0.000 description 1
- 230000001627 detrimental effect Effects 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- 230000008020 evaporation Effects 0.000 description 1
- 239000003500 flue dust Substances 0.000 description 1
- 230000001771 impaired effect Effects 0.000 description 1
- 229910052742 iron Inorganic materials 0.000 description 1
- FBAFATDZDUQKNH-UHFFFAOYSA-M iron chloride Chemical compound [Cl-].[Fe] FBAFATDZDUQKNH-UHFFFAOYSA-M 0.000 description 1
- 150000002506 iron compounds Chemical class 0.000 description 1
- 239000000155 melt Substances 0.000 description 1
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 1
- 238000011084 recovery Methods 0.000 description 1
- 229910052895 riebeckite Inorganic materials 0.000 description 1
- 239000010802 sludge Substances 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 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
- C25C3/04—Electrolytic production, recovery or refining of metals by electrolysis of melts of magnesium
Definitions
- the present invention relates to improvements in the electrolysis of anhyd ous fused metal chlorides.
- the invention ismore particularly concerned with processes in which chlorine, re-
- Processes are known for obtaining fused metal In chlorides, for instance, magnesium chloride, in an anhydrous state and in a form suitable for electrolysis, by causing thecorresponding metal oxides to react with chlorine in presence of carbon or by dehydrating the water-containing 1.; chlorides by treatment with chlorine. It has also been proposed to employ the chlorine produced at-the anode in the electrolysis of such molten chlorides for the conversion of the raw materials into anhydrous chlorides.
- the latter may already be present in the electrolyte from the very beginning in small amounts as impurities or they may be produced during electrolysis by the action of the chlorine on the ash-particles of the carbon electrodes or also on the refractory walls of the anode chamber.
- the said impurities are removed from the chlorine liber- 60 ated at the anode before such chlorine is reutilized for the preparation of anhydrous magnesium chloride.
- This may be accomplished by causing the chlorine gas to pass, after the con version of the volatile chloride vapours into the 55 form of dust which occurs in the course of the cooling of the chlorine, through a mechanical dust filter, for instance, of asbestos bags, or through an electric filter of the type usually employed in the purification of gases, if neces- 7o sary after having passed the gas through a flue dust canal.
- the chlorine gas is employed in the conversion of magnesium oxide or similar compounds into anhydrous magnesium chloride, or in thedehydration of hydrated magnesium chloride in the manner known per 'se and outlined above, whereupon the resulting pure anhydrous magnesium chloride is, introduced into the electrolytic bath and subjected to electrolysis.
- a continuous cyclic process for the electrolytic production of metals from metal oxides involving the electrolysis of the corresponding anhydrous metal chlorides which comprises recovering the chlorine gas evolved at the anode during such electrolysis, freeing said chlorine gas chlorine gas evolved at the anode during such electrolysis, freeing said chlorine gas from foreign metal chlorides contained therein, reacting the purified chlorine gas with fresh amounts of magnesium oxide so as to form anhydrous magnesium chloride, and subjecting such chloride to electrolysis to produce further amounts of magnesium metal and chlorine gas.
Landscapes
- 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. 20, 1934 PATENT OFFICE ELECTROLYSIS OF ANHYDROUS FUSED METAL CHLORIDES Karl Staib and Wilhelm Moschel, Bitter-felt], Germany, assignors,
by mesne assignments, to
Magnesium Development Corporation, a corporation of Delaware No Drawing. Application April 7. 1931, Serial No. 528,452. In Germany November 12, 1930 2 Claims.
The present invention relates to improvements in the electrolysis of anhyd ous fused metal chlorides. The invention ismore particularly concerned with processes in which chlorine, re-
sulting from the electrolytic decomposition of anhydrous fused metal chlorides, is utilized in the preparation of further quantities of electrolyte from suitable raw materials.
Processes are known for obtaining fused metal In chlorides, for instance, magnesium chloride, in an anhydrous state and in a form suitable for electrolysis, by causing thecorresponding metal oxides to react with chlorine in presence of carbon or by dehydrating the water-containing 1.; chlorides by treatment with chlorine. It has also been proposed to employ the chlorine produced at-the anode in the electrolysis of such molten chlorides for the conversion of the raw materials into anhydrous chlorides.
We have observed, for example, in the electrolytic production of magnesium metal, that the chlorine gas produced in the anode chamber of the bath by the electrolysis of a melt containing magnesium chloride always carries along a. certain amount of chlorides, especially when the anode chamber is constructed so as to be suited for the recovery of concentrated chlorine. The presence of these chlorides in the chlorine gas is partly due to the evaporation and splashing of the electrolyte. Besides, the chlorine also contains variable amounts of evaporated aluminium chloride and iron chloride. The latter may already be present in the electrolyte from the very beginning in small amounts as impurities or they may be produced during electrolysis by the action of the chlorine on the ash-particles of the carbon electrodes or also on the refractory walls of the anode chamber.
When using chlorine gas contaminated by such foreign metal chlorides in the preparation of anhydrous magnesium chloride for purposes of electrolysis by the methods mentioned above, we have observed that these contaminations are again incorporated in said magnesium chloride and thus, upon introduction of the latter into the electrolytic bath, caused to accumulate in the electrolyte to a continually increasing extent. Under thesecircumstances, they produce a detrimental action, since they are, when present 30 in sufficient amount, reduced by the magnesium liberated at the cathode with the formation of particles of aluminium and iron which particles,
in their turn, sink to the bottom of the bath, causing part of the'molten magnesium produced by the electrolysis to adhere to them and pass with them into the electrolyte sludge, so that ultimately the yield of magnesium is noticeably impaired.
According to our present invention, the said impurities are removed from the chlorine liber- 60 ated at the anode before such chlorine is reutilized for the preparation of anhydrous magnesium chloride. This may be accomplished by causing the chlorine gas to pass, after the con version of the volatile chloride vapours into the 55 form of dust which occurs in the course of the cooling of the chlorine, through a mechanical dust filter, for instance, of asbestos bags, or through an electric filter of the type usually employed in the purification of gases, if neces- 7o sary after having passed the gas through a flue dust canal. After having undergone such purification, the chlorine gas is employed in the conversion of magnesium oxide or similar compounds into anhydrous magnesium chloride, or in thedehydration of hydrated magnesium chloride in the manner known per 'se and outlined above, whereupon the resulting pure anhydrous magnesium chloride is, introduced into the electrolytic bath and subjected to electrolysis.
In the foregoing, the present invention has been described as applied to the manufacture of magnesium metal from a bath containing anhydrous magnesium chloride, but we wish it to be understood that we do not limit the scope of, 35 our invention to such application as the invention will prove advantageous in the production of allother metals, such as calcium and the like, which are obtained by electrolysis of their anhy drous fused chlorides. provided a similar acon cumulation of undesirable impurities such as aluminium and iron compounds is caused in the electrolyte by the circulation of the chlorine.-
We claim:
1. A continuous cyclic process for the electrolytic production of metals from metal oxides involving the electrolysis of the corresponding anhydrous metal chlorides, which comprises recovering the chlorine gas evolved at the anode during such electrolysis, freeing said chlorine gas chlorine gas evolved at the anode during such electrolysis, freeing said chlorine gas from foreign metal chlorides contained therein, reacting the purified chlorine gas with fresh amounts of magnesium oxide so as to form anhydrous magnesium chloride, and subjecting such chloride to electrolysis to produce further amounts of magnesium metal and chlorine gas.
KARL STAIB. WILHELM MOSCHEL.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE1951494X | 1930-11-12 |
Publications (1)
Publication Number | Publication Date |
---|---|
US1951494A true US1951494A (en) | 1934-03-20 |
Family
ID=7760183
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
US528452A Expired - Lifetime US1951494A (en) | 1930-11-12 | 1931-04-07 | Electrolysis of anhydrous fused metal chlorides |
Country Status (1)
Country | Link |
---|---|
US (1) | US1951494A (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2974093A (en) * | 1958-10-27 | 1961-03-07 | Knapsack Ag | Process for the manufacture of salt mixtures for the electrolytic production of magnesium |
US3418223A (en) * | 1966-06-08 | 1968-12-24 | Nat Lead Co | Continuous process for producing magnesium metal from magnesium chloride including fused bath electrolysis |
-
1931
- 1931-04-07 US US528452A patent/US1951494A/en not_active Expired - Lifetime
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2974093A (en) * | 1958-10-27 | 1961-03-07 | Knapsack Ag | Process for the manufacture of salt mixtures for the electrolytic production of magnesium |
US3418223A (en) * | 1966-06-08 | 1968-12-24 | Nat Lead Co | Continuous process for producing magnesium metal from magnesium chloride including fused bath electrolysis |
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