US1816972A - Manufacture and purification of magnesium - Google Patents

Manufacture and purification of magnesium Download PDF

Info

Publication number
US1816972A
US1816972A US99411A US9941126A US1816972A US 1816972 A US1816972 A US 1816972A US 99411 A US99411 A US 99411A US 9941126 A US9941126 A US 9941126A US 1816972 A US1816972 A US 1816972A
Authority
US
United States
Prior art keywords
magnesium
metal
cell
layer
purification
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
Application number
US99411A
Inventor
Jessup Alfred
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Individual
Original Assignee
Individual
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Individual filed Critical Individual
Application granted granted Critical
Publication of US1816972A publication Critical patent/US1816972A/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Images

Classifications

    • CCHEMISTRY; METALLURGY
    • C25ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25CPROCESSES FOR THE ELECTROLYTIC PRODUCTION, RECOVERY OR REFINING OF METALS; APPARATUS THEREFOR
    • C25C3/00Electrolytic production, recovery or refining of metals by electrolysis of melts
    • C25C3/04Electrolytic production, recovery or refining of metals by electrolysis of melts of magnesium

Definitions

  • the present invention has for its object a process of secondary electrolysis, and a cell designed to realize the same, the process and cell beingboth specially applicable to the purification of magnesium by this method.
  • the process consists in superposing the following layers (in the order stated) in the secondary cell.
  • a protective covering for example of light fused chlorides which must be lighter at the Working temperature than the metal and may be liquid or solid at that temperature.
  • This top layer serves as a protective covering against oxidation for the pure metal layer, and the tvvo upper layers again serve as a protective covering for the electrolysis preventing the formation of oxychlorides in the electrolyte and their deposition on the anodic surface of the alloy which is highly deleterious.
  • the electrolysis should take place in a closed cell. and the possibility of keeping an atmosphere of some neutral gas inside the cell can also be envisaged.
  • the electrolytic bath may be constituted as follows.
  • a protective covering of light chlorides such for example as a mixture of potassium and magnesium chlorides have the composition KCLMgClg, or a mixture of potassium and sodium chlorides, say KClNaCl.
  • the proportions of barium and potassium or sodium chlorides are regulated according 4to the density of the lead-magnesium alloy and the Working temperature so that one may obtain a consecutive decrease in the specific gravities permitting the superposition and maintenance of the four layers as before described.
  • the cell in which this secondary electrolysis may be realized can be of any form, which permits of the superposition of the four above described layers. An example has been shown on the annexed figure.
  • This cell hasv a bottom of cast-iron f which conducts the current to the layer of leadvmagnesium alloy serving as the anode.
  • the sides of the cell are covered with a refractory lining g.
  • this piece of metal e On the inside of this refractory lining is placed a piece, of metal e, (for example in the form of a hollour cylinder) which may occupy roughly the height of the cathodic layer of pure metal, but which must on no account project below into the layer of the electrolyte.
  • This piece of metal is best formed of a metal or alloy which most advantageously can readily be wetted by molten ⁇ magnesium, With the result that the upper and lower layers of chlorides cannot diffuse along the cell Walls owing to the effects of i terial insoluble in magnesium and unattacked by it, project into the cathodic layer of pure magnesium c.
  • this metal Y band or cylinder e may be replaced by a piece yao of any other desired shape, such as a plate, grid etc., of a similar composition and placed always at the height of the layer of pure magnesium.
  • This metallic piece can also if convenient constitute the sole cathodic element, thus dispensing with the carbons lc. l
  • the cell is covered with a cover z, which may be air-tight so as to keep the surface of the bath protected from the air.
  • a space at s is left to constitute insulation from the cast iron receptacle A suitable insulating gasket canbe used to separate these, when the cover is to lit air-tight, as when an inert gas is to be used in the receptacle above the liquid level therein.
  • the various layers includingithat of magnesium are poured into the cell one after another in the order of their respective densities. After the addition of the top layerone can commence to pass the electric current.
  • a process of starting up the electro-v chemical purification of magnesium in a secondary cell which comprises first pouring only two heavy layers linto the cell, one of such layers consisting of magnesium alloy and the other consisting of a magnesium salt and a heavymetal compound readily miscible therewith when molten, the alloy being heavier than the salt, then starting the current vwhile using a metal piece destined to ⁇ separate the two chloride layers as the cathode in order to insure its thorough coating with magnesium, and when this object has been achieved, adding a layer of fused light magnesium metal, and a layer oflight protective salt, whereupon the cell will commence to function normally.
  • An electrolytic cell suitable for the electrolytic purification of magnesium havingl av bottom of conducting material for the anodic current, walls provided with a refractory lining, cathodic conductors extending downwardly into the cell only to the normal height of the refined metal layer therein and a metal piece ofsuch material that magnesium can electrodeposit upon it, said metal piece being positioned at about the normal height of the refined metal layer.
  • An electrolytic cell suitable for the electrolytic purification of magnesium in which a metallic piece located in between the two chloride layers, is located in the cathode portion of the cell, this piece being of such ma- -terial that magnesium can electrodeposit upon it.
  • the improvement consistin in collecting the metal formed in the secon ary vat as a homogeneous liquid layer above the electrolyte between parts of the vat provided with a covering of a material wetondary vat in a homogeneous liquid layer l above the electrolyte between the parts ofthe vat provided with a covering of material wettable by the said metal in a molten state and serving as a cathode, and in maintaining uponV the said layer of metal, a liquid layer of light salts inert to said metal, to Vavoid contact of the metal with the atmosphere.

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

AAug. 4, 1931. A, JESSUP 1,816,972
MANUFACTURE AND PURIFICATION OF MAGNESIUM Filed April 2, 1926 Carbon rod L Cover' 1 @,MyczfKezy 12 .lr' space A ai n A, LA EUYZMQ e \;\/@Mgc22+cz2 P. Mg alloy Cas? von Patented Aug. 4, 1931 PATENT OFFICE,
ALFRED JESSUP, OF PARIS, FRANCE MANUFACTURE AND PURIFICATION OF MAGNESIUM Application led April 2, 1926, Serial No. 99,411, and in France October 9, 1925.
It has already been proposed to prepare certain light metals (by which term I refer to metals lighter than aluminum) by first producing an alloy or impure mixture containing the metal desired in .a primary electrolytic cell and then treating the metal so produced in the type of electrolytic cell generally known as a secondary and thus obtaining pure metal. In this secondary cell the metal Which it is desired to purify is electrolytically transferred from one elec trode to the other, the impure metal or alloy serving as the anode, the pure metal being deposited on the cathode.
The present invention has for its object a process of secondary electrolysis, and a cell designed to realize the same, the process and cell beingboth specially applicable to the purification of magnesium by this method.
The process consists in superposing the following layers (in the order stated) in the secondary cell.
(a) the alloy or impure metal serving as anode.
(b) above this, a layer containing the chloride of the metal to'be puried, to Which is added if necessary heavier chlorides of metals which are more electropositive, in such a manner that this layer is denserl at the working temperature than the molten metal Which one desires to obtain pure.
(c) above this again, a layer of pure metal serving as a-cathode, to which the electric current is led by any appropriate means.
(d) and lastly at the top, a protective covering for example of light fused chlorides, Which must be lighter at the Working temperature than the metal and may be liquid or solid at that temperature.
This top layer serves as a protective covering against oxidation for the pure metal layer, and the tvvo upper layers again serve as a protective covering for the electrolysis preventing the formation of oxychlorides in the electrolyte and their deposition on the anodic surface of the alloy which is highly deleterious.
Preferentially the electrolysis should take place in a closed cell. and the possibility of keeping an atmosphere of some neutral gas inside the cell can also be envisaged.
In the case of the purification of magnesium in this secondary cell, using as anode say for example an alloy of lead and magnesium previously obtained in a primary cell, the electrolytic bath may be constituted as follows.
(a) at the bottom an anode of lead magnesium alloy.
(b) a layer of magnesium chloride to which is added barium chloride, this layer serving as the electrolyte.
(c) a layer of molten magnesium serving as the cathode.
(0l) a protective covering of light chlorides, such for example as a mixture of potassium and magnesium chlorides have the composition KCLMgClg, or a mixture of potassium and sodium chlorides, say KClNaCl.
The proportions of barium and potassium or sodium chlorides are regulated according 4to the density of the lead-magnesium alloy and the Working temperature so that one may obtain a consecutive decrease in the specific gravities permitting the superposition and maintenance of the four layers as before described.
The cell in which this secondary electrolysis may be realized can be of any form, which permits of the superposition of the four above described layers. An example has been shown on the annexed figure.
This cell. hasv a bottom of cast-iron f which conducts the current to the layer of leadvmagnesium alloy serving as the anode.
The sides of the cell are covered With a refractory lining g.
On the inside of this refractory lining is placed a piece, of metal e, (for example in the form of a hollour cylinder) which may occupy roughly the height of the cathodic layer of pure metal, but which must on no account project below into the layer of the electrolyte. This piece of metal is best formed of a metal or alloy which most advantageously can readily be wetted by molten` magnesium, With the result that the upper and lower layers of chlorides cannot diffuse along the cell Walls owing to the effects of i terial insoluble in magnesium and unattacked by it, project into the cathodic layer of pure magnesium c. It is further to be noted that this metal Y band or cylinder e may be replaced by a piece yao of any other desired shape, such as a plate, grid etc., of a similar composition and placed always at the height of the layer of pure magnesium. This metallic piece can also if convenient constitute the sole cathodic element, thus dispensing with the carbons lc. l
The cell is covered with a cover z, which may be air-tight so as to keep the surface of the bath protected from the air. In the modification shown in the drawing, a space at s is left to constitute insulation from the cast iron receptacle A suitable insulating gasket canbe used to separate these, when the cover is to lit air-tight, as when an inert gas is to be used in the receptacle above the liquid level therein.
To start up the cell, the various layers includingithat of magnesium are poured into the cell one after another in the order of their respective densities. After the addition of the top layerone can commence to pass the electric current. y
l Or again one may commence by only adding the rst two layers and tin (or electrodeposit) the magnesium on to -the metallic piece e by using it first as the cathode. When -this piece is properly coated, one can then add the two upper layers, and continue passing the current.
I claim:
1. A process of starting up the electro-v chemical purification of magnesium in a secondary cell which comprises first pouring only two heavy layers linto the cell, one of such layers consisting of magnesium alloy and the other consisting of a magnesium salt and a heavymetal compound readily miscible therewith when molten, the alloy being heavier than the salt, then starting the current vwhile using a metal piece destined to `separate the two chloride layers as the cathode in order to insure its thorough coating with magnesium, and when this object has been achieved, adding a layer of fused light magnesium metal, and a layer oflight protective salt, whereupon the cell will commence to function normally.
2. An electrolytic cell suitable for the electrolytic purification of magnesium havingl av bottom of conducting material for the anodic current, walls provided with a refractory lining, cathodic conductors extending downwardly into the cell only to the normal height of the refined metal layer therein and a metal piece ofsuch material that magnesium can electrodeposit upon it, said metal piece being positioned at about the normal height of the refined metal layer.
3. An electrolytic cell suitable for the electrolytic purification of magnesium in which a metallic piece located in between the two chloride layers, is located in the cathode portion of the cell, this piece being of such ma- -terial that magnesium can electrodeposit upon it.
y 4. In the process of electrolytic manufacture of magnesium involving primary and secondary electrolysis, the improvement consistin in collecting the metal formed in the secon ary vat as a homogeneous liquid layer above the electrolyte between parts of the vat provided with a covering of a material wetondary vat in a homogeneous liquid layer l above the electrolyte between the parts ofthe vat provided with a covering of material wettable by the said metal in a molten state and serving as a cathode, and in maintaining uponV the said layer of metal, a liquid layer of light salts inert to said metal, to Vavoid contact of the metal with the atmosphere.
6. In conducting secondary electrolysis of magnesium from alloys of such metal with a heavy metal, supporting within the cell, a material wettable by the metal obtained, at the height predetermined for the formation of a liquid light metal layer.
In testimony-whereof Ihave afliXed my
US99411A 1925-10-09 1926-04-02 Manufacture and purification of magnesium Expired - Lifetime US1816972A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
FR1816972X 1925-10-09

Publications (1)

Publication Number Publication Date
US1816972A true US1816972A (en) 1931-08-04

Family

ID=9681333

Family Applications (1)

Application Number Title Priority Date Filing Date
US99411A Expired - Lifetime US1816972A (en) 1925-10-09 1926-04-02 Manufacture and purification of magnesium

Country Status (1)

Country Link
US (1) US1816972A (en)

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2880151A (en) * 1957-02-11 1959-03-31 Dow Chemical Co Electrolytic production of magnesium metal
US2888389A (en) * 1956-09-06 1959-05-26 Dow Chemical Co Electrolytic production of magnesium metal
US2950236A (en) * 1957-06-24 1960-08-23 Dow Chemical Co Electrolytic production of magnesium metal
US3245836A (en) * 1960-02-23 1966-04-12 Gen Motors Corp Regenerative battery
US20150225864A1 (en) * 2014-02-13 2015-08-13 Phinix, LLC Electrorefining of magnesium from scrap metal aluminum or magnesium alloys

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2888389A (en) * 1956-09-06 1959-05-26 Dow Chemical Co Electrolytic production of magnesium metal
US2880151A (en) * 1957-02-11 1959-03-31 Dow Chemical Co Electrolytic production of magnesium metal
US2950236A (en) * 1957-06-24 1960-08-23 Dow Chemical Co Electrolytic production of magnesium metal
US3245836A (en) * 1960-02-23 1966-04-12 Gen Motors Corp Regenerative battery
US20150225864A1 (en) * 2014-02-13 2015-08-13 Phinix, LLC Electrorefining of magnesium from scrap metal aluminum or magnesium alloys
US10017867B2 (en) * 2014-02-13 2018-07-10 Phinix, LLC Electrorefining of magnesium from scrap metal aluminum or magnesium alloys
US10557207B2 (en) 2014-02-13 2020-02-11 Phinix, LLC Electrorefining of magnesium from scrap metal aluminum or magnesium alloys

Similar Documents

Publication Publication Date Title
US3028324A (en) Producing or refining aluminum
KR100227921B1 (en) Electrolytic production process for magnesium and its alloy
US2919234A (en) Electrolytic production of aluminum
US1816972A (en) Manufacture and purification of magnesium
US2302604A (en) Fused bath electrolytic production of ferrochromium
US4430174A (en) Method for refinement of impure aluminum
US4882017A (en) Method and apparatus for making light metal-alkali metal master alloy using alkali metal-containing scrap
US2034339A (en) Refining of aluminum
US3202600A (en) Current conducting element for aluminum reduction cells
US1534317A (en) Electrolytic production of aluminum
US1782616A (en) Electrolytic apparatus for refining aluminum and for like processes
US3787300A (en) Method for reduction of aluminum with improved reduction cell and anodes
US2959533A (en) Production of aluminium by fused salt electrolysis with vertical or inclined cathodes of carbon and aluminium
US2742418A (en) Electrolytic cell for alkali-lead alloy manufacture
US3464900A (en) Production of aluminum and aluminum alloys from aluminum chloride
US2033172A (en) Process for the manufacture of alloys containing boron
US1534319A (en) Refining aluminum electrolytically with fused electrolytes
US2552423A (en) Process for the direct production of refined aluminum
US3787310A (en) Reduction of aluminum with improved reduction cell and anodes
US1567318A (en) Method of making metallic magnesium
US20030209426A1 (en) Insulating lid for aluminum production cells
US1384499A (en) Method of and apparatus for refining metals
US1882525A (en) Process for the electrolytic production of metals of the alkalis or alkaline earths
US2950236A (en) Electrolytic production of magnesium metal
US4165263A (en) Method of preparing an electrolytic cell for operation