US2355130A - Separation of molten magnesium from molten salt baths - Google Patents

Separation of molten magnesium from molten salt baths Download PDF

Info

Publication number
US2355130A
US2355130A US469391A US46939142A US2355130A US 2355130 A US2355130 A US 2355130A US 469391 A US469391 A US 469391A US 46939142 A US46939142 A US 46939142A US 2355130 A US2355130 A US 2355130A
Authority
US
United States
Prior art keywords
molten
magnesium
molten salt
ladle
separation
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
US469391A
Inventor
Leland A Yerkes
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
Priority to US469391A priority Critical patent/US2355130A/en
Application granted granted Critical
Publication of US2355130A publication Critical patent/US2355130A/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

  • My invention relates to the separation of molten magnesium from molten salt baths and to apparatus for use therewith.
  • magnesium metal commercially is to electrolyze it from a salt bath comprising essentially magnesium chloride.
  • the magnesium compound is reduced at the cathode, producing metallic magnesium, and, the metallic magnesium being lighter than the bath from which it is electrolyzed, floats to the top of the cell near the cathodes thereof, usually in a cathode compartment provided in the cell., It is essential that this magnesium be removed for subsequent use as the metal and it should be free of substantially .all traces of electrolyte.
  • Various methods and equipment have been used for removing the magnesium metal but so far as I know neither the method nor equipment has been satisfactory in that the magnesium was either not suitably or rapidly removed or undesirably large proportions of the molten electrolyte were also removed.
  • Fig. 1 is a perspective view of apparatus constructed in accordance with my invention, a portion of the handle being broken away,
  • Fig. 2 is a transverse sectional view taken on the line 2-2 of Fig. 1, and
  • Fig. 3 isan enlarged fragmentary section.
  • I provide a dish shaped body III with a plurality of openings II running entirely therethrough and having a handle l2 suitably secured thereon.
  • the dish shaped body In is formed of ferrous metal such as ordinary ingot iron or low carbon steel, although other ferrous metals may be used.
  • the openings I I are of relatively fine size but the size may vary, depending in part upon the thickness 01' the material comprising the dish shaped body of the ladle and partly because some'latitude in cross sectional area is permitted from a functional standpoint. In general, I prefer to have the openings about .090" when material .25" to .125" thick is used although the openings may run between about .050" and .125" and satisfactory results obtained.
  • the ladle may be cast' and they holes formed therein by means of a drill.
  • the openings II are shown round but they may have other shapes. While size and shape may vary, the ladle may be 12" to 18" in diameter and 12" deep when an open type of cell is used.
  • the formed ladle is treated to produce a continuous coating l3 of an iron compound on the surface thereof.
  • the iron compound may be formed in various ways, such as by heating a mild steel ladle under controlled oxidizing conditions to form an oxide coating, immersing such It will be understood that the exact method of formationof the oxidized iron film is not critical to my invention, it only being necessary that an adherent film or layer of an iron compound be produced upon the entire surface.
  • the dish shaped body comprising the ladle when prepared as. described, is'then employed to dip the molten magnesium metal from the surface of the electrolyte and the entrained molten salt comprising the electrolyte is allowed to drain by holding the ladle above the cell. This period of draining is only relatively short and, of course, the ladle may be handled manually or mechanically as'determined by the type of mechanical installation comprising the electrolytic plant.
  • the iron compound coating causes the molten magnesium to be retained in the ladle, but allows the molten salt comprising the electrolyte to pass through. I explain this as being due to an interfacial surface tension phenomenon but do not wish to be limited to this explanation. It is my concept that magnesium metal will form a thi. coating over a surface of metal, and the metal surface having been coated with magnesium in.
  • the iron oxide coating is not wetted by the magnesium metal, but is wetted or has some affinity for the molten electrolyte, with the result that the latter is fluid at the openings provided in the ladle and passes therethrough, while the molten magnesium tends to present a small surface, is less fiuid at the openings and is retained in the ladle.
  • the ladle may be formed of any material so long as the surface thereof is an iron compound and the ladle has adequate strength.
  • There is a definite advantags in having the material of the ladle formed of a ferrous metal however, both from the standpoint of strength and from the standpoint of the simplicity of production of the oxidized surface.
  • the method of separatingmolten magnesium from a molten salt bath which comprises providing a dish shaped body of ferrous metal having a plurality of fine openings therethrough, treating the said ferrous metal to produce an oxide coating thereon, dipping the resulting coated dish shaped'body into the molten magnesiumin the salt bath, and allowing the same to remain above the said bath to drain the molten salt through the said fine openings, the molten ma nesium remaining within the said dish shaped body.
  • a method of separating metallic magnesium from salts thereof which comprises passing a mixture of molten metallic magnesium with a molten salt thereof over a perforated support.
  • a method of separating metallic magnesium from a molten salt bath which comprises passing a mixture of molten metallic magnesium and a molten salt over a' perforated support provided with anadherent coating of an iron compound .125 inch in diameter, whereby the molten salt passes through the perforated support while the molten metallic magnesium is retained thereby.
  • a method of separating metallic magnesium from a molten salt bath which comprises passing a mixture of molten metallic magnesium and a unwettable by molten metallic magnesium, the perforations being from about .050 inch to about 5.
  • a method of separating a mixture of metal- 110 magnesium and salts thereof which comprises passing such a mixture over a perforated ferrous support provided with an iron oxide coating thereon, the perforations being sufficiently large to permit free passage of molten salt while being too small to overcome the surface tension of molten metallic magnesium, whereby metallic magnesium is retained on the ferrous support while the molten salt passes through the perforations and is separated from the metallic magprovided with an oxide coating thereon, the perforations being about .090 inch in diameter, whereby the molten salt passes through the perforated support while the molten metallic magnesium is retained thereby.
  • the method of separating molten magnesium from a molten salt bath which comprises providing a ferrousmetal support having a pinrality of fine openings therethrough, treating the ferrous metal to produce an oxide coating thereon, passing a molten magnesium metal-salt bath mixture over said coated support, and allowing the molten salt to'drain through the said fine openings, whereby molten magnesium is recovered'from' said ferrous metal support free from molten salt.
  • the method of separating molten magnesium from a molten salt bath which comprises providing a dish-shaped body of ferrous metal having therein a plurality of fine openings of about .050 inch to about .125 inch in diameter, treating the said dish-shaped body with an oxiinto the molten magnesium in the salt bath, and
  • the method of separating molten magnesium from a molten salt bath which comprises providing a dish-shaped body of ferrous metal having therein a plurality of fine openings of "d dishshaped body with an oxidizing agen an adherent oxidized coating tl'i'ereo to metallic magnesium, dipping th" ;;resulting coated dish-shaped body into the molten magnesium in the salt bath, and allowing the same to remain above the said bath to drain the molten salt through the said-fine openings, the molten

Description

Aug; 8, 1944. A. YERKES 2,355,130
SEPARATION OF MOLTEN MAGNESIUM FROM MOLTEN SALT BATHS I Filed Dec. 18, 1942 A INVENTOR.
Patented Aug. 8, 1944 UNITED STATES PATENT OFFICE SEPARATION OF MOLTEN MAGNESIUM FROM MOLTEN SALT BATHS (Granted under the act of March 3, 1883, as
amended April 30, 1928; 370 0. G. 757), l
Claim.
This invention described herein may be manufactured and used by or for the Government for governmental purposes, without the payment to me of any royalty thereon.
My invention relates to the separation of molten magnesium from molten salt baths and to apparatus for use therewith.
One usual method of producing magnesium metal commercially is to electrolyze it from a salt bath comprising essentially magnesium chloride. In a usual type of cell employed for the purpose, the magnesium compoundis reduced at the cathode, producing metallic magnesium, and, the metallic magnesium being lighter than the bath from which it is electrolyzed, floats to the top of the cell near the cathodes thereof, usually in a cathode compartment provided in the cell., It is essential that this magnesium be removed for subsequent use as the metal and it should be free of substantially .all traces of electrolyte. Various methods and equipment have been used for removing the magnesium metal but so far as I know neither the method nor equipment has been satisfactory in that the magnesium was either not suitably or rapidly removed or undesirably large proportions of the molten electrolyte were also removed.
I have discovered that if a ladle or ladle-like object be provided having a large number of relatively fine holes therethrough, and the surface be covered with an iron compound such as iron oxide, the molten magnesium can be dipped from.
the surface, all or substantially all of the molten magnesium being retained in the ladle and 'the molten electrolyte being quickly drained through the openings. Following this discovery, I have produced improved apparatus and provided an improved method as will be brought out in connection with the following description taken with the accompanying drawing wherein .5
Fig. 1 is a perspective view of apparatus constructed in accordance with my invention, a portion of the handle being broken away,
Fig. 2 is a transverse sectional view taken on the line 2-2 of Fig. 1, and
Fig. 3 isan enlarged fragmentary section.
In accordance'with my invention, I provide a dish shaped body III with a plurality of openings II running entirely therethrough and having a handle l2 suitably secured thereon. The dish shaped body In is formed of ferrous metal such as ordinary ingot iron or low carbon steel, although other ferrous metals may be used. The openings I I are of relatively fine size but the size may vary, depending in part upon the thickness 01' the material comprising the dish shaped body of the ladle and partly because some'latitude in cross sectional area is permitted from a functional standpoint. In general, I prefer to have the openings about .090" when material .25" to .125" thick is used although the openings may run between about .050" and .125" and satisfactory results obtained. The ladle may be cast' and they holes formed therein by means of a drill. The openings II are shown round but they may have other shapes. While size and shape may vary, the ladle may be 12" to 18" in diameter and 12" deep when an open type of cell is used.
The formed ladle is treated to produce a continuous coating l3 of an iron compound on the surface thereof. The iron compound may be formed in various ways, such as by heating a mild steel ladle under controlled oxidizing conditions to form an oxide coating, immersing such It will be understood that the exact method of formationof the oxidized iron film is not critical to my invention, it only being necessary that an adherent film or layer of an iron compound be produced upon the entire surface.
' The dish shaped body comprising the ladle, when prepared as. described, is'then employed to dip the molten magnesium metal from the surface of the electrolyte and the entrained molten salt comprising the electrolyte is allowed to drain by holding the ladle above the cell. This period of draining is only relatively short and, of course, the ladle may be handled manually or mechanically as'determined by the type of mechanical installation comprising the electrolytic plant.
The iron compound coating causes the molten magnesium to be retained in the ladle, but allows the molten salt comprising the electrolyte to pass through. I explain this as being due to an interfacial surface tension phenomenon but do not wish to be limited to this explanation. It is my concept that magnesium metal will form a thi. coating over a surface of metal, and the metal surface having been coated with magnesium in.
the region of the holes, the flow of magnesium through the holes is promoted rat er than retarded. The iron oxide coating, according to my concept, is not wetted by the magnesium metal, but is wetted or has some affinity for the molten electrolyte, with the result that the latter is fluid at the openings provided in the ladle and passes therethrough, while the molten magnesium tends to present a small surface, is less fiuid at the openings and is retained in the ladle. For this reason, it is my concept that the ladle may be formed of any material so long as the surface thereof is an iron compound and the ladle has adequate strength. There is a definite advantags in having the material of the ladle formed of a ferrous metal, however, both from the standpoint of strength and from the standpoint of the simplicity of production of the oxidized surface.
It is clear that the invention may have somewhat broader aspects than indicated by the specific description. Molten salt baths are sometimes employed in connection with the purification of magnesium, for example, and the ladle of my invention will have advantage in connection therewith. The scope of the invention is defined by the claims.
What I claim as new and desire to protect by Letters Patent of the United States:
- 1. The method of separatingmolten magnesium from a molten salt bath, which comprises providing a dish shaped body of ferrous metal having a plurality of fine openings therethrough, treating the said ferrous metal to produce an oxide coating thereon, dipping the resulting coated dish shaped'body into the molten magnesiumin the salt bath, and allowing the same to remain above the said bath to drain the molten salt through the said fine openings, the molten ma nesium remaining within the said dish shaped body.
2. A method of separating metallic magnesium from salts thereof which comprises passing a mixture of molten metallic magnesium with a molten salt thereof over a perforated support.
provided with an adherent coating of an iron compound unwettable'by molten metallic magnesium, theperforations being sufficiently large to permit free passage of molten salt while being too small to. overcome the surface tension of molten metallic magnesium, whereby metallic magnesium is retained on the perforated support while the molten salt passes through the perforations and is separated from the metallic mag-.
nesium.
3. A method of separating metallic magnesium from a molten salt bath which comprises passing a mixture of molten metallic magnesium and a molten salt over a' perforated support provided with anadherent coating of an iron compound .125 inch in diameter, whereby the molten salt passes through the perforated support while the molten metallic magnesium is retained thereby.
4. A method of separating metallic magnesium from a molten salt bath which comprises passing a mixture of molten metallic magnesium and a unwettable by molten metallic magnesium, the perforations being from about .050 inch to about 5. A method of separating a mixture of metal- 110 magnesium and salts thereof which comprises passing such a mixture over a perforated ferrous support provided with an iron oxide coating thereon, the perforations being sufficiently large to permit free passage of molten salt while being too small to overcome the surface tension of molten metallic magnesium, whereby metallic magnesium is retained on the ferrous support while the molten salt passes through the perforations and is separated from the metallic magprovided with an oxide coating thereon, the perforations being about .090 inch in diameter, whereby the molten salt passes through the perforated support while the molten metallic magnesium is retained thereby.
8. The method of separating molten magnesium from a molten salt bath which comprises providing a ferrousmetal support having a pinrality of fine openings therethrough, treating the ferrous metal to produce an oxide coating thereon, passing a molten magnesium metal-salt bath mixture over said coated support, and allowing the molten salt to'drain through the said fine openings, whereby molten magnesium is recovered'from' said ferrous metal support free from molten salt.
9. The method of separating molten magnesium from a molten salt bath which comprises providing a dish-shaped body of ferrous metal having therein a plurality of fine openings of about .050 inch to about .125 inch in diameter, treating the said dish-shaped body with an oxiinto the molten magnesium in the salt bath, and
allowing the same to remain above the said bath to drain the molten salt through the said fine openings, the molten magnesium remaining within the said dish-shaped body.
10. The method of separating molten magnesium from a molten salt bath which comprises providing a dish-shaped body of ferrous metal having therein a plurality of fine openings of "d dishshaped body with an oxidizing agen an adherent oxidized coating tl'i'ereo to metallic magnesium, dipping th" ;;resulting coated dish-shaped body into the molten magnesium in the salt bath, and allowing the same to remain above the said bath to drain the molten salt through the said-fine openings, the molten
US469391A 1942-12-18 1942-12-18 Separation of molten magnesium from molten salt baths Expired - Lifetime US2355130A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
US469391A US2355130A (en) 1942-12-18 1942-12-18 Separation of molten magnesium from molten salt baths

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US469391A US2355130A (en) 1942-12-18 1942-12-18 Separation of molten magnesium from molten salt baths

Publications (1)

Publication Number Publication Date
US2355130A true US2355130A (en) 1944-08-08

Family

ID=23863602

Family Applications (1)

Application Number Title Priority Date Filing Date
US469391A Expired - Lifetime US2355130A (en) 1942-12-18 1942-12-18 Separation of molten magnesium from molten salt baths

Country Status (1)

Country Link
US (1) US2355130A (en)

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2787592A (en) * 1948-10-01 1957-04-02 Ver Deutsche Metallwerke Ag Method for the treatment of metal
US3289850A (en) * 1964-02-07 1966-12-06 Peter J Gubash Ice skimmer
US3403098A (en) * 1966-06-30 1968-09-24 Hydromation Engineering Compan Oil skimmers
EP0089009A1 (en) * 1982-03-11 1983-09-21 HELIOTRONIC Forschungs- und Entwicklungsgesellschaft für Solarzellen-Grundstoffe mbH Process for the removal of the slag from molten mixtures of slag and silicon
US8418369B1 (en) * 2003-10-07 2013-04-16 Kim Laube Clipper lever support insert
US9009980B2 (en) 2010-07-06 2015-04-21 Melvin M. Dunbar, Jr. Perforated food ladle
US20170156526A1 (en) * 2015-12-06 2017-06-08 Dorothy Swanson Disposable Relish Spoon

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2787592A (en) * 1948-10-01 1957-04-02 Ver Deutsche Metallwerke Ag Method for the treatment of metal
US3289850A (en) * 1964-02-07 1966-12-06 Peter J Gubash Ice skimmer
US3403098A (en) * 1966-06-30 1968-09-24 Hydromation Engineering Compan Oil skimmers
EP0089009A1 (en) * 1982-03-11 1983-09-21 HELIOTRONIC Forschungs- und Entwicklungsgesellschaft für Solarzellen-Grundstoffe mbH Process for the removal of the slag from molten mixtures of slag and silicon
US8418369B1 (en) * 2003-10-07 2013-04-16 Kim Laube Clipper lever support insert
US9009980B2 (en) 2010-07-06 2015-04-21 Melvin M. Dunbar, Jr. Perforated food ladle
US20170156526A1 (en) * 2015-12-06 2017-06-08 Dorothy Swanson Disposable Relish Spoon

Similar Documents

Publication Publication Date Title
DE3172036D1 (en) A process of electrolytically manufacturing perforated material and perforated material so obtained
ATE140172T1 (en) METHOD AND DEVICE FOR PRODUCING METAL STRIPS
US2355130A (en) Separation of molten magnesium from molten salt baths
US2620296A (en) Method of electrolytically coating and etching bearing surfaces
US2276232A (en) Metal coating process
RU2725524C1 (en) Method of producing carbon-graphite composite material
US2431947A (en) Formation of a strong bond between a ferrous metal surface and an electrodeposit of silver
US2513859A (en) Method of electroplating of tin on ferrous strip
US3054737A (en) Process and bath for electrosmoothing ferrous metals
ES419556A2 (en) Method of increasing the hardness of a film formed on the surface of an alloy. (Machine-translation by Google Translate, not legally binding)
US1511967A (en) Treatment of tin-plate scrap
JPS57156130A (en) Wire cut electric discharge machining electrode wire
US2971898A (en) Electroplating ferrous-base molded bodies
JPS55131165A (en) Galvanizing method for silicon-containing steel sheet
US2107318A (en) White coating on aluminum
RU2725526C1 (en) Method of producing carbon-graphite composite material
RU2725518C1 (en) Method of producing carbon-graphite composite material
RU2725522C1 (en) Method of producing carbon graphite composite material
US1276977A (en) Method of coating metal articles.
DE2412912A1 (en) METHOD FOR ELECTROPLATING SILICON CARBIDE BODIES
DE624723C (en) Device for the electrolytic separation of copper-silver alloys
JPS57114695A (en) Production of zinc plated steeel plate of superior blackening resistance and intergranular corrosion resistance
DE702147C (en) Process for electrolytic demassing and copper removal
SU127537A1 (en) High-speed electrolytic deposition of metals with electrolyte flow
JPS5534607A (en) Recovering and removing method for useless metals from chromate solution by diaphragm electrolysis