US880489A - Process of producing magnesium. - Google Patents

Process of producing magnesium. Download PDF

Info

Publication number
US880489A
US880489A US26450505A US1905264505A US880489A US 880489 A US880489 A US 880489A US 26450505 A US26450505 A US 26450505A US 1905264505 A US1905264505 A US 1905264505A US 880489 A US880489 A US 880489A
Authority
US
United States
Prior art keywords
magnesium
oxid
fluorid
electrolysis
bath
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
US26450505A
Inventor
Franz Von Kuegelgen
George O Seward
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.)
VIRGINIA LABORATORY Co
VIRGINIA LAB Co
Original Assignee
VIRGINIA LAB Co
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 VIRGINIA LAB Co filed Critical VIRGINIA LAB Co
Priority to US26450505A priority Critical patent/US880489A/en
Application granted granted Critical
Publication of US880489A publication Critical patent/US880489A/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

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

  • This'invention relates to the production of magnesium and magnesium alloys by electrolysis.
  • the present commercial process for the production of metallic magnesium consists in the electrolysis of the double chlorid of magnesium and sodium (or potassium). It is i very difficult to obtain the electrolyte free from water. The best results are obtained by mixing chlorid of magnesium with chlorid of sodium or of potassium, and carefully drying this mixture-and melting it. After certain other treatments the molten salt is poured into iron crucibles and subjected to an electrolyzing current while applying'heat externally. To get good results, the temperature has to be kept low and watched very carefully. If it rises too high, the magnesium is redissolved in the electrolyte; and furthermore the magnesium rises to the top where it is partly burned by exposure to the air, and partly recombines with the chlorin.
  • Our invention is based upon the discovery that magnesium oxid or analogous magnesium compound is soluble in certain flworids of higher decomposition voltage, so t'l iat when such fused bath is subjected to electrolysis the magnesium compound alzone is decomposed and magnesium is separated-at the cathode.
  • Wehave found that-a continuous electrolytic production of magnesium is ossible by the use as an-eleetrolyte of a used mixture of magnesium oxidr and magnesium fluorid, rendered fusibleby the.
  • the process may e carried on continuously.
  • some magnesium fluori d is also decomposed, but this is easily replaced by the addition of magnesium'fiuorid during the electrolysis.
  • the solvent bath may be consi erably varied.
  • the mixture is chosen with a view of getting as low a melting point as o ssible consistent with the property of disso vlng magnesium oxid.
  • mag'nesiumfluorid w th one or more alkaline fluorids is suitable.
  • ma nesiumfiuorid, one or more alkaline fluori and one or more alkahne earth fiuorlds may be used.
  • a nnxture of two parts magnesium .fluorid, one part lithium fluorid and one part calcium fluorid gives good results;
  • magnesium oxid instead of magnesium oxid, we may use magnesium oxy-chlorid or other oxy-comound which will dissolve in the solvent baths already described. In case the oxychlorid is used, both oxygen and chlorm are separated at the anode.
  • oxychlorid both oxygen and chlorm are separated at the anode.
  • we designate magnesium oxid it is understood that we include the ox -chlorid of ma nesium or any other suitab e oxycompoun
  • An example of an application of our invention is as follows :-A mixture of O aF 'ium fluorid. The combine 'ected to electrolysis in. any suitable and and MgF in any suitable proportions is melted in a suitable vessel, and when sufii- .ciently molten, MgO is dissolved therein. Or
  • the solvent bath may be made of any of the fluorids referred to, and may or may not include a lithium compound, referably lithd bath is subown manner.
  • Carbon anodes may be used and an iron cathode, but other mate- 7 rials may be used for the anode and cathode.

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

Uurra suArEs ATENT Faro.
FRANZ VON KU'GELGEN AND GEORGE O. SEWARD, OF HOLCOM BS ROCK, VIRGINIA,
ASSIGNORS TO VIRGINIA'LABORATORY COMPANY, OF NEW YORK, N. Y., A. CORPO- RATION OF NEW YORK. F
rrcocnss or rnonucmc MAGNESIUM.
Specification of Letters Patent.
Patented Feb. 2a, 1908.
Application filed June 9. 1905. Serial-N0. 264.506.
This'invention relates to the production of magnesium and magnesium alloys by electrolysis.
The present commercial process for the production of metallic magnesium consists in the electrolysis of the double chlorid of magnesium and sodium (or potassium). It is i very difficult to obtain the electrolyte free from water. The best results are obtained by mixing chlorid of magnesium with chlorid of sodium or of potassium, and carefully drying this mixture-and melting it. After certain other treatments the molten salt is poured into iron crucibles and subjected to an electrolyzing current while applying'heat externally. To get good results, the temperature has to be kept low and watched very carefully. If it rises too high, the magnesium is redissolved in the electrolyte; and furthermore the magnesium rises to the top where it is partly burned by exposure to the air, and partly recombines with the chlorin. Even where the proper temperature is maintained, the difference in specific gravity is' so, slight that it is necessary to use diaphragms of porcelain, which are expensive and fragile. Another disadvantage is that after a certain amount of magnesium has been removed by electrolysis, the electrolyte contains too much sodium or potassium for continuing the process; it then becomes necessary to remove it and replace it by fresh electrolyte. Thus the preparation of the electrolyte re- (Spires a long and tedious treatment; and t e electrolytic process is not continuous,'re quires great care, and necessitates the use of expensive diaphragms. Under these conditions' it has been heretofore impossible to produce magnesium at a low price, although the raw material is cheap. The present invention'eliminates the disadvantages of the prior process, and renders it possib e to produce magnesium by a continuous process, and at a considerably lower cost than heretofore. g 1
Our invention is based upon the discoverythat magnesium oxid or analogous magnesium compound is soluble in certain flworids of higher decomposition voltage, so t'l iat when such fused bath is subjected to electrolysis the magnesium compound alzone is decomposed and magnesium is separated-at the cathode. Wehave found that-a continuous electrolytic production of magnesium is ossible by the use as an-eleetrolyte of a used mixture of magnesium oxidr and magnesium fluorid, rendered fusibleby the. addition of a fluorid or'fiuoridszof, metals more electro-positive than-magnesium.- Magnesium oxid has a lowendecompnsition voltagethan magnesium fluoridr and the other fluorid or' fluoride, and is: therefore'decomposed in preference" to the othercompounds, solong as the voltage iskept'within certain limits, and aproper concentrationv is maintained. -By feedlng magnesium oxid to the electrolyte. inpro ortionas itvis decomposed,
the process may e carried on continuously. In case the voltage is hi her than the normal, some magnesium fluori d is also decomposed, but this is easily replaced by the addition of magnesium'fiuorid during the electrolysis.
In practicin the process, the solvent bath may be consi erably varied. -The mixture is chosen with a view of getting as low a melting point as o ssible consistent with the property of disso vlng magnesium oxid. A
mixture of mag'nesiumfluorid w th one or more alkaline fluorids is suitable. Or ma nesiumfiuorid, one or more alkaline fluori and one or more alkahne earth fiuorlds may be used. A nnxture of two parts magnesium .fluorid, one part lithium fluorid and one part calcium fluorid gives good results;
Instead of magnesium oxid, we may use magnesium oxy-chlorid or other oxy-comound which will dissolve in the solvent baths already described. In case the oxychlorid is used, both oxygen and chlorm are separated at the anode. Hereinafter, whenever We designate magnesium oxid, it is understood that we include the ox -chlorid of ma nesium or any other suitab e oxycompoun An example of an application of our invention is as follows :-A mixture of O aF 'ium fluorid. The combine 'ected to electrolysis in. any suitable and and MgF in any suitable proportions is melted in a suitable vessel, and when sufii- .ciently molten, MgO is dissolved therein. Or
the solvent bath may be made of any of the fluorids referred to, and may or may not include a lithium compound, referably lithd bath is subown manner. Carbon anodes may be used and an iron cathode, but other mate- 7 rials may be used for the anode and cathode.
Asthe magnesium oxid is decomposed it is I 'to be re laced by feedinggn fresh magnesium oxid. I t is desirable to eep the bath nearly saturated with the magnesium oxid, and the latter should therefore be fed in at frequent intervals, and as much ornearly as much as will freely dissolve.
[If it is desired to produce an alloy of magnesium, We. may use the alloying metal as the cathode, with which the separatedrnagnesium alloys, using for example aluminium,
as set forth in our applicatlon Serial No.
257,618, filed April 27, 1905.
'We claim as our invention 1., The process of producing magnesium which consists in dissolvin magnesium oxid in a fused'bath of mixed uorids whose decomposition voltage is higher than that of magnesium oxid, subjectlng the same to electrolysis, and feeding magnesium oxi'd to 'replace that whichis decomposed.
2. The process of croducing magnesium which consists in disso ving magnesium oxid in a fused bath of magnesium fluorid and another fluorid whose decomposition voltage is higher than that of magnesium oirid, subjecting the same to electrolysis, and feeding magnesium oxid to replace that which is de composed.
3. The process of producing magnesium which consists in dissolving magnesium oxid in a fused bath of magnesium fluorid and one or more alkaline fiuorids', subjecting the same to electrolysis, and feeding magnesium oxid to replace that which is decomposed.
4. The process of producing magnesium by dissolving magnesium oxid in a fused bath of magnesium fluorid and one or more fluorids of metals more electro-positive than magnesium, and subjecting the same to elecsigned our names in the presence of two subscribing witnesses.
FRANZ VON KUGELGEN. GEORGE O. SEWARD.
' Witnesses:'
Gno. 'T. .LANc 'sTER, C. OFFERHAUS.
US26450505A 1905-06-09 1905-06-09 Process of producing magnesium. Expired - Lifetime US880489A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
US26450505A US880489A (en) 1905-06-09 1905-06-09 Process of producing magnesium.

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US26450505A US880489A (en) 1905-06-09 1905-06-09 Process of producing magnesium.

Publications (1)

Publication Number Publication Date
US880489A true US880489A (en) 1908-02-25

Family

ID=2948929

Family Applications (1)

Application Number Title Priority Date Filing Date
US26450505A Expired - Lifetime US880489A (en) 1905-06-09 1905-06-09 Process of producing magnesium.

Country Status (1)

Country Link
US (1) US880489A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2431723A (en) * 1942-01-17 1947-12-02 Leland A Yerkes Electrolytic method for producing magnesium alloys
US3503857A (en) * 1967-04-24 1970-03-31 Union Carbide Corp Method for producing magnesium ferrosilicon

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2431723A (en) * 1942-01-17 1947-12-02 Leland A Yerkes Electrolytic method for producing magnesium alloys
US3503857A (en) * 1967-04-24 1970-03-31 Union Carbide Corp Method for producing magnesium ferrosilicon

Similar Documents

Publication Publication Date Title
US2722509A (en) Production of titanium
US880489A (en) Process of producing magnesium.
US3226311A (en) Process of producing calcium by electrolysis
RU2692759C1 (en) Lead-carbon metal composite material for electrodes of lead-acid batteries and a method for synthesis thereof
Ono et al. Design, test and theoretical assessments for reduction of titanium oxide to produce titanium in molten salt
CN104357880A (en) Method for preparing copper-lithium mother alloy by self-consuming cathode fused salt electrolysis
US996094A (en) Method of making fusible compounds of aluminium and recovering aluminium therefrom.
US1077894A (en) Electrode.
US2623848A (en) Process for producing modified electronickel
US2876180A (en) Fused salt bath for the electrodeposition of transition metals
US1066787A (en) Process of producing zinc from blue powder.
US881934A (en) Process of producing aluminum-magnesium alloys.
US1888118A (en) Production of fluorine
US589415A (en) Guillaume de chalmot
US1882525A (en) Process for the electrolytic production of metals of the alkalis or alkaline earths
SU47448A1 (en) Electrolytic production method of magnesium alloys
US602873A (en) Process of electrolytically manufacturing metallic sulfids
US2899369A (en) Special electrolytic processing
US1447892A (en) Smelting and electrolytic process
US578633A (en) Process of reducing aluminium
US875668A (en) Process of producing an alloy for use in steel-casting.
US1869493A (en) Lithium alloys and process of producing the same
US881527A (en) Process for treating complex cobalt ores and for refining cobalt from nickel, arsenical, and silver-bearing ores.
US2974092A (en) Production of titanium
US631253A (en) Process of reducing aluminium.