US931092A - Electrolytic production of magnesium. - Google Patents

Electrolytic production of magnesium. Download PDF

Info

Publication number
US931092A
US931092A US30845406A US1906308454A US931092A US 931092 A US931092 A US 931092A US 30845406 A US30845406 A US 30845406A US 1906308454 A US1906308454 A US 1906308454A US 931092 A US931092 A US 931092A
Authority
US
United States
Prior art keywords
magnesium
chlorid
electrolytic production
specific gravity
fused
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
US30845406A
Inventor
George O Seward
Franz Von Kuegelgen
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 US30845406A priority Critical patent/US931092A/en
Application granted granted Critical
Publication of US931092A publication Critical patent/US931092A/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

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

  • This invention relates to the roduction of magnesium by electrol sis 0 its fused salts.
  • electrolysis a ords serious difficulty, because the difference in the specific gravity of the liberated metal difi'ers so slightly from that of its fused salt, that the metal does not readily separate. It is practically necessary for good results to use an electrol te whose specific gravity is so different rom that of magnesium, that the-latter will either sink readily to the bottom or rise freely to the to of the bath, where it canbe collected.
  • Kbr a metal as light as magnesium it is extremely diflicult to find electrolytes which have so .low a specific gravity that the separated metal will readily sink tothe bottom, and insuch cases it is A trolytically from an electro preferable to add to the electrolyte a component' which will make it materially heavier than the metal, so that the latter will rise to the top of the bath.
  • Such added component should be a flux which is eflicient when used in comparatively small quantities, and should not be decomposed by the current.
  • the present invention is characterized by the use for this purpose of the salts of the alkali-earth metals, which are peculiarly suited to this use because (1) they have a high specific gravity, and (2) they are difficult .to decom ose electrolyt1cally.' I
  • magnesium chlorid with potassium chlorid added as a flux, the separated magnesium being collected at the bottom of the vesse1 It is only under certain conditions of temthan the separated magnesium, and it is difficult to so manage the process that these temperature conditions are maintained so that a good separation of the magnesium re-' sults.

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

UNI D STATES PATENT onnron.
GEORGE O. SEWARD AND FRANZ VON KI IGELGEN, OF HOLCOMBS ROCK, VIRGINIA, ASSIGNORS TO VIRGINIALABORATORY COMPANY, OF NEW YORK, N. Y., A CORPORATION OF NEW YORK.
ELECTROLYTIC PRODUCTION OF MAGNEsIUM.
To all whom it may concern:
Be it known that we, GEORGE O. SEWARD, a citizen of the United States, and FRANZ you KIB'GELGEN, a subject of the German Emperor, both residing at Holcombs Rock, in the county of Bedford and State of Virginia, have jointly invented certain new and useful Improvements in the Electrolytic Pro- I duction of Magnesium, of which the 'following is a specification.
This invention relates to the roduction of magnesium by electrol sis 0 its fused salts. Such electrolysis a ords serious difficulty, because the difference in the specific gravity of the liberated metal difi'ers so slightly from that of its fused salt, that the metal does not readily separate. It is practically necessary for good results to use an electrol te whose specific gravity is so different rom that of magnesium, that the-latter will either sink readily to the bottom or rise freely to the to of the bath, where it canbe collected. Kbr a metal as light as magnesium it is extremely diflicult to find electrolytes which have so .low a specific gravity that the separated metal will readily sink tothe bottom, and insuch cases it is A trolytically from an electro preferable to add to the electrolyte a component' which will make it materially heavier than the metal, so that the latter will rise to the top of the bath. Such added component should be a flux which is eflicient when used in comparatively small quantities, and should not be decomposed by the current.
The present invention is characterized by the use for this purpose of the salts of the alkali-earth metals, which are peculiarly suited to this use because (1) they have a high specific gravity, and (2) they are difficult .to decom ose electrolyt1cally.' I
As an examp e of the practical application of our invention, we will describe the production of magnesium b electrol sis of magnesium chlorid, using arium c orid to increase the specific gravity of the electrolyte. m r
At present magnesium -is produced elecyte of fused Specification of LettersPatent. Application filed larch 28, 1906. Serial No. 308,454.
'perature that such an electrolyte is lighter Patented Aug. 17, 1909.
magnesium chlorid, with potassium chlorid added as a flux, the separated magnesium being collected at the bottom of the vesse1 It is only under certain conditions of temthan the separated magnesium, and it is difficult to so manage the process that these temperature conditions are maintained so that a good separation of the magnesium re-' sults.
In producing magnesium according to the present invention, we replacethe potassium chlorid partly by barium chlorid, so that we obtain an electrolyte which is so much heavier than the magnesium, that the latter rises readily to the top, where 1t ma be collected. Although the' roportion. 0 barium chlorid may be great y varied, we have found an electrolyte of the followin composition to give suitable results gOl, 5 parts, KGl 5 parts, BaCl 3.5 parts.
Instead of barium chlorid we may use the chlorid or other suitable salt of calcium or strontium.
We are aware that alkali-earth salts have been used before as fluxes," but not for the purpose of regulating the specific gravity of the electroyl What we claim is v 1. The electrolytic production of magnesium by electrolyzing fused magnesium chlorid to which is added enough of a denser alkali-earth chlorid to ren er the bath heavier than the separated ma esium.
2. The electrolytic production of magnesium by electrolyzing a fused bath of magnesium chlorid and barium chlorid.
3. The electrolytic production of magnesium by electrolyzing a fused bath of mag;
nesium chlorid, potassium chlorid, an barium chlorid.
In witness whereof, we have hereunto scribing witnesses.
- GEORGE O. SEWARD.
FRANZ VON -KUGELGEN. Witnesses:
J. H. WEBB,
F. V. Bmnnn.
US30845406A 1906-03-28 1906-03-28 Electrolytic production of magnesium. Expired - Lifetime US931092A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
US30845406A US931092A (en) 1906-03-28 1906-03-28 Electrolytic production of magnesium.

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US30845406A US931092A (en) 1906-03-28 1906-03-28 Electrolytic production of magnesium.

Publications (1)

Publication Number Publication Date
US931092A true US931092A (en) 1909-08-17

Family

ID=2999515

Family Applications (1)

Application Number Title Priority Date Filing Date
US30845406A Expired - Lifetime US931092A (en) 1906-03-28 1906-03-28 Electrolytic production of magnesium.

Country Status (1)

Country Link
US (1) US931092A (en)

Cited By (3)

* 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

Cited By (3)

* 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

Similar Documents

Publication Publication Date Title
US2757135A (en) Electrolytic manufacture of titanium
US1511829A (en) Method of making metallic beryllium
US2783196A (en) Method for producing titanium and zirconium
US2715093A (en) Electrolytic production of molybdenum powder and coherent deposits
US3791945A (en) Method of production of alkali metals and their alloys
US900962A (en) Production of barium and barium alloys.
US1878918A (en) Manufacture of chromic acid
US868226A (en) Production of magnesium.
US788315A (en) Method of electrolytic separation.
US464097A (en) Ludwig grabaij
US778270A (en) Production of metallic magnesium.
US2774729A (en) Recovery of uranium by electrolysis of a fused bath
US771646A (en) Process of obtaining metals.
US947983A (en) Purifying tantalum.
US1092178A (en) Cathode for electrolytic furnaces.
US3407127A (en) Method of recovering rhenium values from rhenium-containing scrap material
US1258261A (en) Production of magnesium.
US2092451A (en) Electrolytic production of lead
US2742414A (en) Electrolytic method of producing aluminum
US808066A (en) Process for the production of metallic calcium.
US2813069A (en) Porous anode
US1116865A (en) Process of producing alkali and alkaline-earth metals.
US2840519A (en) Peroxidation process
US2158269A (en) Electrolytic process for the manufacture of litharge
US631253A (en) Process of reducing aluminium.