US3837843A - Process for thermal production of magnesium - Google Patents

Process for thermal production of magnesium Download PDF

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Publication number
US3837843A
US3837843A US00410965A US41096573A US3837843A US 3837843 A US3837843 A US 3837843A US 00410965 A US00410965 A US 00410965A US 41096573 A US41096573 A US 41096573A US 3837843 A US3837843 A US 3837843A
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US
United States
Prior art keywords
slag
magnesium
agglomerates
reducing agent
calcined
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
US00410965A
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English (en)
Inventor
R Pons
A Mena
M Poyet
J Desbert
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.)
FR D ELECTROMETALLURGIE SOC
SOC FR D ELECTROMETALLURGIE FR
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FR D ELECTROMETALLURGIE SOC
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Application granted granted Critical
Publication of US3837843A publication Critical patent/US3837843A/en
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Expired - Lifetime legal-status Critical Current

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Classifications

    • CCHEMISTRY; METALLURGY
    • C22METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
    • C22BPRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
    • C22B26/00Obtaining alkali, alkaline earth metals or magnesium
    • C22B26/20Obtaining alkaline earth metals or magnesium
    • C22B26/22Obtaining magnesium

Definitions

  • magnesium can be produced by reacting reducing agents, such as silicon, with a substance containing magnesium oxide in the presence of a slag, whereby lumps of reducing agent, for instance iron and silicon, and lumps of calcined dolomite, are introduced above a molten slag.
  • reducing agents such as silicon
  • lumps of reducing agent for instance iron and silicon
  • lumps of calcined dolomite are introduced above a molten slag.
  • the magnesium oxide dissolves in the slag, enters into contact with the lumps of reducing agent and reacts therewith, causing a strong evolution of magnesium in the vapor state.
  • the binders normally used to bring about agglomeration also have the effect of introducing impurities into the furnace and hence into the metal and of modifying the composition of the slag, which may affect the process.
  • the method of production of magnesium by reaction of silicon with calcined dolomite exhibits another feature, i.e. the slag obtained, consisting of a calcium silico-aluminate plus a little magnesia, has little market value.
  • the slag is nevertheless used by the cement industry in combination with other materials to make up cements, but, in order to render it marketable, the slag has to be quenched rapidly by pouring the molten material into cold water. This obviates setting during transportation. A substantial fraction of the slag escapes this treatment and solidifies naturally in air, particularly at the bottom of the receptacle from which the molten slag is poured into the water.
  • the non-quenched fraction disintegrates during the cooling stage of between 400 and 600 C, forming a finely divided dust for which no use has yet been discovered and which gives rise to fairly difficult problems of storage.
  • the reducing agent is introduced in the form of uniform size granules which exhibit little tendency to sink into the slag.
  • the reducing agent is diluted by mixing with part of the slag formed as a by-product of the reaction. Additionally, the process permits the use of a large proportion, if not all, of the non-quenched slag, which has hitherto been unusable and which has constituted a nuisance factor.
  • composition is typical of the slag obtained from the furnace:
  • This apparatus consisted essentially of a flanged disc inclined at an angle of 3045 to the horizontal, and rotated at a speed of 18 to 24 rpm.
  • the mixture of ferro-silicon and slag is poured evenly onto the: disc, accompanied by a spray of water.
  • the paste so formed is gradually converted into spherical granules by the rotation of the disc which gradually overflow the rim.
  • speed and inclination of the disc it was found possible to obtain spherical granules to 20 mm in diameter, all of which gave good results when subsequently used in the process.
  • the balls were calcined for 50 minutes at 700 C in a rotary furnace.
  • the silicon content of the balls was determined as follows: The material was finely ground, treated with concentrated caustic soda. The hydrogen evolved was passed over a drying agent and determined by measuring the quantity of water fonned by reaction with copper oxide heated to 400 C. The results of the analysis showed that oxidation of silicon during calcination was negligible.
  • a reducing agent is reacted with a substance containing magnesium oxide in the presence of molten slag
  • the reducing agent is introduced in the form of agglomerates produced by mixing the finely divided reducing agent with a binder consisting of water and slag, drying the agglomerates, and then calcining the dried agglomerates at a temperature not less than 700 C.
  • a process as claimed in claim 1 in which the slag used in the binder is of a composition corresponding to the composition of the slag resulting from the production of magnesium.

Landscapes

  • Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Geology (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • General Life Sciences & Earth Sciences (AREA)
  • Manufacturing & Machinery (AREA)
  • Environmental & Geological Engineering (AREA)
  • Materials Engineering (AREA)
  • Mechanical Engineering (AREA)
  • Metallurgy (AREA)
  • Organic Chemistry (AREA)
  • Manufacture And Refinement Of Metals (AREA)
  • Silicon Compounds (AREA)
  • Compounds Of Alkaline-Earth Elements, Aluminum Or Rare-Earth Metals (AREA)
US00410965A 1972-10-30 1973-10-29 Process for thermal production of magnesium Expired - Lifetime US3837843A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
FR7238394A FR2204697B1 (ja) 1972-10-30 1972-10-30

Publications (1)

Publication Number Publication Date
US3837843A true US3837843A (en) 1974-09-24

Family

ID=9106405

Family Applications (1)

Application Number Title Priority Date Filing Date
US00410965A Expired - Lifetime US3837843A (en) 1972-10-30 1973-10-29 Process for thermal production of magnesium

Country Status (6)

Country Link
US (1) US3837843A (ja)
JP (1) JPS5348166B2 (ja)
BR (1) BR7308513D0 (ja)
CA (1) CA1001421A (ja)
FR (1) FR2204697B1 (ja)
NO (1) NO133843C (ja)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3918959A (en) * 1973-12-28 1975-11-11 Showa Denko Kk Process for production of magnesium
US4400207A (en) * 1981-05-13 1983-08-23 Continental Alloys S.A. Method of producing metal alloys
US4648900A (en) * 1980-12-08 1987-03-10 Bostroem Olle Suction sintering method and apparatus therefor
ES2125829A1 (es) * 1997-03-04 1999-03-01 Univ Salamanca Procedimiento para la obtencion de magnesio.

Families Citing this family (21)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR2395319A1 (fr) * 1977-06-24 1979-01-19 Sofrem Perfectionnements aux procedes de production de magnesium par voie thermique
CA1149092A (en) * 1979-01-11 1983-06-28 William E. Horn, Jr. Phosphite heat stabilized graft diene copolymers
JPS56104622U (ja) * 1980-01-14 1981-08-15
JPS57161319A (en) * 1981-03-27 1982-10-04 Citizen Watch Co Ltd Forming method of bearing in plastic ground plate
US7011600B2 (en) 2003-02-28 2006-03-14 Fallbrook Technologies Inc. Continuously variable transmission
CN101166922B (zh) 2004-10-05 2011-02-09 瀑溪技术公司 无级变速器
KR101641317B1 (ko) 2005-10-28 2016-07-20 폴브룩 인텔렉츄얼 프로퍼티 컴퍼니 엘엘씨 전동 드라이브
WO2007061993A2 (en) 2005-11-22 2007-05-31 Fallbrook Technologies Inc Continuously variable transmission
WO2007067249A1 (en) 2005-12-09 2007-06-14 Fallbrook Technologies Inc. Continuously variable transmission
EP1811202A1 (en) 2005-12-30 2007-07-25 Fallbrook Technologies, Inc. A continuously variable gear transmission
US8376903B2 (en) 2006-11-08 2013-02-19 Fallbrook Intellectual Property Company Llc Clamping force generator
EP2573424A3 (en) 2007-04-24 2017-07-26 Fallbrook Intellectual Property Company LLC Electric traction drives
CN101796327B (zh) 2007-07-05 2014-01-29 福博科技术公司 无级变速器
CN101861482B (zh) 2007-11-16 2014-05-07 福博科知识产权有限责任公司 用于变速传动装置的控制器
US8398518B2 (en) 2008-06-23 2013-03-19 Fallbrook Intellectual Property Company Llc Continuously variable transmission
US8469856B2 (en) 2008-08-26 2013-06-25 Fallbrook Intellectual Property Company Llc Continuously variable transmission
US8888643B2 (en) 2010-11-10 2014-11-18 Fallbrook Intellectual Property Company Llc Continuously variable transmission
WO2012138610A1 (en) 2011-04-04 2012-10-11 Fallbrook Intellectual Property Company Llc Auxiliary power unit having a continuously variable transmission
US10047861B2 (en) 2016-01-15 2018-08-14 Fallbrook Intellectual Property Company Llc Systems and methods for controlling rollback in continuously variable transmissions
US11215268B2 (en) 2018-11-06 2022-01-04 Fallbrook Intellectual Property Company Llc Continuously variable transmissions, synchronous shifting, twin countershafts and methods for control of same
US11174922B2 (en) 2019-02-26 2021-11-16 Fallbrook Intellectual Property Company Llc Reversible variable drives and systems and methods for control in forward and reverse directions

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB569744A (en) * 1943-11-10 1945-06-06 Int Alloys Ltd Improvements relating to the production of magnesium
US2390016A (en) * 1944-03-10 1945-11-27 New Jersey Zinc Co Charge preparation
US3114627A (en) * 1963-12-17 Producing metallic magnesium from a
US3441402A (en) * 1965-12-15 1969-04-29 Exxon Research Engineering Co Continuous process for the production of magnesium

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3114627A (en) * 1963-12-17 Producing metallic magnesium from a
GB569744A (en) * 1943-11-10 1945-06-06 Int Alloys Ltd Improvements relating to the production of magnesium
US2390016A (en) * 1944-03-10 1945-11-27 New Jersey Zinc Co Charge preparation
US3441402A (en) * 1965-12-15 1969-04-29 Exxon Research Engineering Co Continuous process for the production of magnesium

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3918959A (en) * 1973-12-28 1975-11-11 Showa Denko Kk Process for production of magnesium
US4648900A (en) * 1980-12-08 1987-03-10 Bostroem Olle Suction sintering method and apparatus therefor
US4400207A (en) * 1981-05-13 1983-08-23 Continental Alloys S.A. Method of producing metal alloys
ES2125829A1 (es) * 1997-03-04 1999-03-01 Univ Salamanca Procedimiento para la obtencion de magnesio.

Also Published As

Publication number Publication date
AU6192173A (en) 1975-05-01
JPS5348166B2 (ja) 1978-12-27
CA1001421A (en) 1976-12-14
NO133843B (ja) 1976-03-29
FR2204697B1 (ja) 1975-01-03
NO133843C (ja) 1976-07-07
BR7308513D0 (pt) 1974-08-15
JPS505211A (ja) 1975-01-20
FR2204697A1 (ja) 1974-05-24

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