US2097689A - Conversion of magnesium dust into compact metallic magnesium - Google Patents

Conversion of magnesium dust into compact metallic magnesium Download PDF

Info

Publication number
US2097689A
US2097689A US48435A US4843535A US2097689A US 2097689 A US2097689 A US 2097689A US 48435 A US48435 A US 48435A US 4843535 A US4843535 A US 4843535A US 2097689 A US2097689 A US 2097689A
Authority
US
United States
Prior art keywords
magnesium
dust
conversion
compact
compact metallic
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
US48435A
Inventor
Erdmann Konrad
Hansgirg Fritz
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.)
American Magnesium Metals Corp
Original Assignee
American Magnesium Metals Corp
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 American Magnesium Metals Corp filed Critical American Magnesium Metals Corp
Application granted granted Critical
Publication of US2097689A publication Critical patent/US2097689A/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Images

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

  • the result is 35 achieved that the process can be practised with the voltages of 50-300 volts usually employed in the art of electric heating, without appreciable amounts of magnesium being left behind in the residue of the charge.
  • the preparation of the charge in this manner offers the advantage that after the vaporization of the magnesium content the shaped pieces of the charge are still of such inherent strength that these granules. or the like. substantially retain 45 their shape, so that the material is not reduced to dust, and the disengaged metal vapors are consequently practically tree from dusty impurities. These vapors become readily condensed to a liquid deposit which sets to compact metal- 50 lic magnesium.
  • the spent residue can be comminuted and used asain as an addition to fresh magnesium dust.
  • the magnesium dust is commixed for example with carll bon in a powdered form and with pulverized magnesium oxide, the proportion of carbon to magnesium oxide being between 1:2 and 1:3, and the sum of these additions amounting to up to 50 parts by weight of the magnesium, dust to be dealt with.
  • the mixture is then worked up to a paste with the addition of hydrocarbon oils, after whichthis paste is heated to distil off the hydrocarbon oils. If this be eflected at higher temperatures (for example above 650 C.) a small proportion of the oils will be cracked with the result that the initially pasty mass assumes the form of solid granules.
  • parts of the line magnesium dust become agglomerated tolarger granules of a metallic nature; the fractured surface of the granulated material shows silky lustre and under the microscope minute metal droplets are detectable.
  • the magnesium dust is admixed with the selected additional substances in a mixing machine, for example in a kneading machine, and
  • the magnesium dust also loses its pyrophorous properties, so that the granulated charge can be exposed to the air without the slightest danger.
  • a process of converting magnesium dust into compact metallic magnesium which comprises mixingmagnesium dust with current conducting. substance indifierent to magnesium metal, which at temperatures at which lively vaporization of magnesium takes place is still unmelted and which has low vapor tension at such temperatures, while concurrently further adding magnesium oxide, impastingthe mixture thus obum oxide, impasting the mixture thus obtained with the addition of hydrocarbon oil, after which this paste is heated to distil off the hydrocarbon oil, and agglomerated to compacted bodies; then interposing the pieces thus obtained as resistor between the poles in an electric furnace to drive out the magnesium in the form of vapor, and
  • a process 01' converting magnesium dust into compact metallic magnesium which comprises mixing magnesium dust with comminuted iron, while concurrently further adding magnesium oxide, impasting the mixture thus obtained withthe addition of hydrocarbon oil, after which this paste is heated to distil off the hydrocarbon oil, and agglomerated to compacted bodies; then interposing the pieces thus obtained as resistor between the poles in an electric furnace to drive out the magnesium in the form of vapor, and condensing the vapor evolved to a liquid deposit.
  • a process of converting magnesium dust into compacted metallic magnesium which comprises mixing magnesium dust with a mixture of comminuted carbon and magnesium oxide, the proportion of carbon to magnesium oxide being between 1:2 and 1:3, and the sum of these additions amounting to up to 50 parts by weight of the magnesium dust, impasting the mixtuae thus obtained with the addition of hydrocarbon oil, after which this paste is heated to distil ofl the hydrocarbon oil, and agglomerated to compacted bodies; then interposing the pieces thus obtained as resistor between the poles in an electric furnace to drive out the magnesium in the form of vapor, and condensing the vapor evolved to a

Description

Nov. 2,' 1937. K. ERDMANN ET AL CONVERSION OF MAGNESIUM DUST INTO COMPACT METALLIC MAGNESIUM Filed NOV. 5, 1935 W n x e M m a m an .s M 2 :4 n L i INVENTORS Zam free ,EesL'dae Mayne:
Patented Nov. 2, 1937 UNITED STATES CONVERSION OF MAGNESIUM DUST INTO COMPACT METALLIC MAGNESIUM Konrad Erdmann, Radenthein, Austria, and Fritz Hansglrg, Konan, Korea, assignors to American Magnesium Metals Corporation, Pittsburgh, Pa., a corporation oillelaware Application November 5,1935, Serial No. 48,435 r h In Austria November13, 1934 A 4 Claims. This invention relates to a process for the conversion oi' magnesium dust into compact magpieces or granules as resistor between the poles in an electric furnace, while regulating the conductivity of the charge made up into the form of pieces or granules in such a manner that it becomes possible to drive oil the magnesium completely. by vaporization, without wastage of electric energy. This is attained in accordance with the invention by working up the magnesium dust, into porous shaped pieces, with the admixture of suitably large quantities of current conducting additions which are inert to magnesium metal, which are still unmelted at temperatures at which magnesium vaporizes vigorously, and which have very low vapor tension at these temperatures. There are preferably employed concurrently further additions acting as carriers capable of preventing the pieces from crumbling during the distillation operation. Preferred examples of substances of the one type are carbon and iron, and a preferred example of a substance of the other kind is magnesium oxide.
By the use 01' such additions the result is 35 achieved that the process can be practised with the voltages of 50-300 volts usually employed in the art of electric heating, without appreciable amounts of magnesium being left behind in the residue of the charge. Furthermore, the preparation of the charge in this manner offers the advantage that after the vaporization of the magnesium content the shaped pieces of the charge are still of such inherent strength that these granules. or the like. substantially retain 45 their shape, so that the material is not reduced to dust, and the disengaged metal vapors are consequently practically tree from dusty impurities. These vapors become readily condensed to a liquid deposit which sets to compact metal- 50 lic magnesium.
The spent residue can be comminuted and used asain as an addition to fresh magnesium dust.
For the carrying out of the process the magnesium dust is commixed for example with carll bon in a powdered form and with pulverized magnesium oxide, the proportion of carbon to magnesium oxide being between 1:2 and 1:3, and the sum of these additions amounting to up to 50 parts by weight of the magnesium, dust to be dealt with. The mixture is then worked up to a paste with the addition of hydrocarbon oils, after whichthis paste is heated to distil off the hydrocarbon oils. If this be eflected at higher temperatures (for example above 650 C.) a small proportion of the oils will be cracked with the result that the initially pasty mass assumes the form of solid granules. At the same time parts of the line magnesium dust become agglomerated tolarger granules of a metallic nature; the fractured surface of the granulated material shows silky lustre and under the microscope minute metal droplets are detectable.
Apparatus well suited for the production of granular'material in accordance with the present invention is illustrated diagrammatically in the accompanying drawing. The casing l of a horizontally disposed conveyor helix 2 passes through a furnace 3 which is heated by an embedded resistance and works into a cooling shaft 5 equipped with a discharge device 6. About mid-way of the casing l of the helix there is branched off a pipe I for carrying 011 the vapors evolved, which pipe passes through a cooler 8 and discharges into a condensing trap 9 provided with overflow l and gas outlet pipe I I.
The magnesium dust is admixed with the selected additional substances in a mixing machine, for example in a kneading machine, and
kneaded with hydrocarbon oils until a doughypaste results. This paste is fed to the helix 2 through a hopper. In traversing the casing l, which is heated by radiation for example to 700 0., the hydrocarbon oils become volatilized. The vapors are condensed in the cooler 8 and flow into the receiver 9 where they are separated from the uncondensible gases which escape at H. The
charge passes in a granular state into the cooling shaft and is intermittently or continuously removed through the discharging device 8.
Through this treatment the magnesium dust also loses its pyrophorous properties, so that the granulated charge can be exposed to the air without the slightest danger.
According to the provisions of the patent statutes, we have explained the principle and construction of our invention and have illustrated and described what we now consider to represent its best embodiment. However. we desire t haveiit understood that, within the scope of the appended claims, the invention may be practised otherwise than as specifically illustrated and described.
We claim:
1. A process of converting magnesium dust into compact metallic magnesium, which comprises mixingmagnesium dust with current conducting. substance indifierent to magnesium metal, which at temperatures at which lively vaporization of magnesium takes place is still unmelted and which has low vapor tension at such temperatures, while concurrently further adding magnesium oxide, impastingthe mixture thus obum oxide, impasting the mixture thus obtained with the addition of hydrocarbon oil, after which this paste is heated to distil off the hydrocarbon oil, and agglomerated to compacted bodies; then interposing the pieces thus obtained as resistor between the poles in an electric furnace to drive out the magnesium in the form of vapor, and
condensing the vapor evolved to a liquid deposit.
3. A process 01' converting magnesium dust into compact metallic magnesium, which comprises mixing magnesium dust with comminuted iron, while concurrently further adding magnesium oxide, impasting the mixture thus obtained withthe addition of hydrocarbon oil, after which this paste is heated to distil off the hydrocarbon oil, and agglomerated to compacted bodies; then interposing the pieces thus obtained as resistor between the poles in an electric furnace to drive out the magnesium in the form of vapor, and condensing the vapor evolved to a liquid deposit.
4. A process of converting magnesium dust into compacted metallic magnesium, which comprises mixing magnesium dust with a mixture of comminuted carbon and magnesium oxide, the proportion of carbon to magnesium oxide being between 1:2 and 1:3, and the sum of these additions amounting to up to 50 parts by weight of the magnesium dust, impasting the mixtuae thus obtained with the addition of hydrocarbon oil, after which this paste is heated to distil ofl the hydrocarbon oil, and agglomerated to compacted bodies; then interposing the pieces thus obtained as resistor between the poles in an electric furnace to drive out the magnesium in the form of vapor, and condensing the vapor evolved to a
US48435A 1934-11-13 1935-11-05 Conversion of magnesium dust into compact metallic magnesium Expired - Lifetime US2097689A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
AT2097689X 1934-11-13

Publications (1)

Publication Number Publication Date
US2097689A true US2097689A (en) 1937-11-02

Family

ID=3689838

Family Applications (1)

Application Number Title Priority Date Filing Date
US48435A Expired - Lifetime US2097689A (en) 1934-11-13 1935-11-05 Conversion of magnesium dust into compact metallic magnesium

Country Status (1)

Country Link
US (1) US2097689A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2634969A (en) * 1945-06-26 1953-04-14 North Carolina Magnesium Dev C Apparatus for continuous recovery of magnesium

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2634969A (en) * 1945-06-26 1953-04-14 North Carolina Magnesium Dev C Apparatus for continuous recovery of magnesium

Similar Documents

Publication Publication Date Title
US1179394A (en) METHOD AND MEANS FOR PRODUCING TITANIUM TETRACHLORID, (TiCl4.)
US2205386A (en) Production of metals and alloys
US2097689A (en) Conversion of magnesium dust into compact metallic magnesium
US1884993A (en) Production of metallic magnesium
US2789880A (en) Selective chlorination of beryl
US2442674A (en) Deleading zinc-lead fume
US2049633A (en) Reclamation of battery plate scrap
US679330A (en) Process of extracting arsenic, antimony, or tellurium from sulfurous ores.
US875381A (en) Process of treating complex ores containing zinc and other volatilizable metals.
US2429671A (en) Treatment of materials containing tantalum and niobium
US3918959A (en) Process for production of magnesium
US1311380A (en) warren f
US2043363A (en) Reduction of ores by metallic calcium
US2357614A (en) Treating finely divided magnesium
US2629650A (en) Method of purifying phosphate rock containing iron impurities
DE630710C (en) Process for converting magnesium dust into compact metallic magnesium
US2488398A (en) Basic lead sulfate
US1593022A (en) Process for volatilization of metals from their ores
US553115A (en) Reff galbraith
US1678607A (en) Metallurgy of zinc
US3104939A (en) Process for preventing short-circuiting by an electrode in an electric arc furnace having a liquid melt therein
US2344445A (en) Material for charging furnaces
US1778018A (en) Process for and relating to separating gold, silver, and lead from crude antimonial metal
US2168750A (en) Production of metallic magnesium
US2387206A (en) Method of making beryllium fluoride