US2101904A - Recovery of compact metallic magnesium from magnesium in finely divided form - Google Patents
Recovery of compact metallic magnesium from magnesium in finely divided form Download PDFInfo
- Publication number
- US2101904A US2101904A US753892A US75389234A US2101904A US 2101904 A US2101904 A US 2101904A US 753892 A US753892 A US 753892A US 75389234 A US75389234 A US 75389234A US 2101904 A US2101904 A US 2101904A
- Authority
- US
- United States
- Prior art keywords
- magnesium
- dust
- recovery
- finely divided
- divided form
- 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
Links
- 229910052749 magnesium Inorganic materials 0.000 title description 30
- 239000011777 magnesium Substances 0.000 title description 30
- FYYHWMGAXLPEAU-UHFFFAOYSA-N Magnesium Chemical compound [Mg] FYYHWMGAXLPEAU-UHFFFAOYSA-N 0.000 title description 29
- 238000011084 recovery Methods 0.000 title description 5
- 239000000428 dust Substances 0.000 description 16
- 238000000034 method Methods 0.000 description 7
- 238000000859 sublimation Methods 0.000 description 7
- 230000008022 sublimation Effects 0.000 description 7
- 229910052751 metal Inorganic materials 0.000 description 5
- 239000002184 metal Substances 0.000 description 5
- 238000009835 boiling Methods 0.000 description 4
- 239000003795 chemical substances by application Substances 0.000 description 4
- 238000010438 heat treatment Methods 0.000 description 4
- 238000007670 refining Methods 0.000 description 4
- 238000006243 chemical reaction Methods 0.000 description 3
- 239000007787 solid Substances 0.000 description 3
- 238000005336 cracking Methods 0.000 description 2
- 238000000354 decomposition reaction Methods 0.000 description 2
- 238000004821 distillation Methods 0.000 description 2
- 239000012535 impurity Substances 0.000 description 2
- 239000007788 liquid Substances 0.000 description 2
- 238000009834 vaporization Methods 0.000 description 2
- 230000008016 vaporization Effects 0.000 description 2
- -1 Magnesium Metals Chemical class 0.000 description 1
- HCHKCACWOHOZIP-UHFFFAOYSA-N Zinc Chemical compound [Zn] HCHKCACWOHOZIP-UHFFFAOYSA-N 0.000 description 1
- 239000000571 coke Substances 0.000 description 1
- 238000007906 compression Methods 0.000 description 1
- 230000006835 compression Effects 0.000 description 1
- 238000009833 condensation Methods 0.000 description 1
- 230000005494 condensation Effects 0.000 description 1
- 238000001125 extrusion Methods 0.000 description 1
- 229930195733 hydrocarbon Natural products 0.000 description 1
- 150000002430 hydrocarbons Chemical class 0.000 description 1
- 229910001338 liquidmetal Inorganic materials 0.000 description 1
- 150000002681 magnesium compounds Chemical class 0.000 description 1
- 238000010297 mechanical methods and process Methods 0.000 description 1
- 230000008018 melting Effects 0.000 description 1
- 238000002844 melting Methods 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 230000001590 oxidative effect Effects 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 239000012071 phase Substances 0.000 description 1
- 238000002203 pretreatment Methods 0.000 description 1
- 239000007790 solid phase Substances 0.000 description 1
- 230000008023 solidification Effects 0.000 description 1
- 238000007711 solidification Methods 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C22—METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
- C22B—PRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
- C22B26/00—Obtaining alkali, alkaline earth metals or magnesium
- C22B26/20—Obtaining alkaline earth metals or magnesium
- C22B26/22—Obtaining magnesium
Definitions
- This invention relates to the recovery of substantially pure metallic magnesium from finely divided magnesium, ,and more particularly from magnesium dust by sublimation.
- sub- 5 limation is used in the following description and claims to mean vaporization of the magnesium content from the solid phase or from the fused state, in both cases with the direct recovery of a solid condensate from the vaporous phase (that is to say sublimation in the narrower and wider sense, respectively).
- Magnesium results in the form of dust in the refining of crude metallic magnesium or magnesium scrap, and also in the course of the recovery of metallic magnesium from oxidic magnesium compounds by reduction carried out at temperatures above the boiling point of metallic magnesium, provided the vapors be suddenly cooled down, for the purpose .of condensation, to a temperature below. the solidification point of magnesium.
- the dust evolved in refining distillation has been regarded n as hardly capable of being fused together, and
- the volume of the paste obtained by the sprinkling of the dust with agglomerating agents can be still further reduced by compressing the mass While in the moist state.
- bodies of a nature to increase the heat conductivity for example pieces of .metal in the shape of rods, sheets, or wire, are embedded in the moistened magnesium dust.
- the described method can also be employed to. very great advantage for the pre-treatment of magnesium dust intended for refinement by sublimation in the strict sense of the term, that is 40 to say by the immediate conversion of the metal from the solid into the vaporous state.
- the sublimation is preferably effected in a current of a non-oxidizing gas.
- the magnesium obtained as a crystalline sublimate is then, if desired, converted into compact metal by various further operations. It can be freely melted together or directly shaped by extrusion or compression.
- What I claim is: a 1. The method of producing substantially pure magnesium from magnesium in a finely divided state, which comprises making the finely divided magnesium into a paste with a liquid hydrocarbonaceous impasting agent, heating the said This procedure yields 15 paste up to a temperature at which partial decomposition, by cracking, of the hydrocarbonaceous impasting' agent occurs while agitating the mass under treatment to form solid granular aggregates therefrom, and recovering the magnesium from the said aggregates by sublimation.
Landscapes
- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Life Sciences & Earth Sciences (AREA)
- Environmental & Geological Engineering (AREA)
- General Life Sciences & Earth Sciences (AREA)
- Geology (AREA)
- Manufacturing & Machinery (AREA)
- Materials Engineering (AREA)
- Mechanical Engineering (AREA)
- Metallurgy (AREA)
- Organic Chemistry (AREA)
- Manufacture And Refinement Of Metals (AREA)
Description
Patented Dec. 14, 1937 UNITED STATES RECOVERY OF COMPACT METALLIC MAG- -NE SIUNI DIVIDED FORM FROM MAGNESIUM IN FINELY Fritz Hansgirg, Radenthein, Austria, assignor to American Magnesium Metals Corporation,
Pittsburgh, Pa., a corporation of Delaware No Drawing. Application November 20, 1934, Serial No. 753,892. In Austria May 4, 1934 3 Claims. (on. 75-67) This invention relates to the recovery of substantially pure metallic magnesium from finely divided magnesium, ,and more particularly from magnesium dust by sublimation. The term sub- 5 limation is used in the following description and claims to mean vaporization of the magnesium content from the solid phase or from the fused state, in both cases with the direct recovery of a solid condensate from the vaporous phase (that is to say sublimation in the narrower and wider sense, respectively).
It is amongst the objects of this invention to provide a process of refining finely divided magnesium yielding a refinedproduct which lends 5 itself to easy conversion into compact metal,
which process is readily practicable and effective, and afiords also other advantages which will be understood by those skilled in the art.
Magnesium results in the form of dust in the refining of crude metallic magnesium or magnesium scrap, and also in the course of the recovery of metallic magnesium from oxidic magnesium compounds by reduction carried out at temperatures above the boiling point of metallic magnesium, provided the vapors be suddenly cooled down, for the purpose .of condensation, to a temperature below. the solidification point of magnesium. For a long time the dust evolved in refining distillation has been regarded n as hardly capable of being fused together, and
nesium oxide as absolutely incapable of being fused together It is only recently that such dust has been successfully converted into compact metallic magnesium, and that either by maintaining the dust at a temperature in the vicinity of the boiling pointof metallic magnesium until such time as the particles unite to liquid metal, or by redistilling the dust.
40 Alternatively it has been proposed to proceed for this purpose in view, by mechanical methods (for example agitating or shaking at temperatures above the melting point but below the boiling temperature of metallic magnesium), such as were previously usual for the conversion of zinc dust into .the molten state. In whatever manner this further treatment may be carried out, it is attended by the difficulty that the dust,
I more particularly when in a state of extremely 50 fine subdivision, is spontaneously inflammable. Further, for the fusing together by heating at temperatures in the neighbourhood of the boiling point of magnesium and for distillation, very spacious plant is required, on account of the low 55 volumetric weight of the dust; moreover, the heat the dust resulting from the reduction of mag conductivity of the 'dust is slight, to the detri- 7 is subsequently freed of the agglomerating agent by heating, which is preferably carried out in an 10 inert or reducing gaseous atmosphere. When hydrocarbons are used for the purpose they are preferably driven ofi while raising the temperature to a point at which partial decomposition by cracking takes place. a crumbly residual mass in which themagnesium dust is held together by a coke framework. Refining by sublimation of the dust solidified in this manner, can be carried out more conveniently and with better utilization of the heat 20 applied. When the further treatment of the dust is efiected by vaporization of the magnesium content from the fused state, there is obtained the further particular advantage that the disengaged magnesium vapors are free of pulverulent impurities, or at least carry over such impurities with them in but very slight quantities.
The volume of the paste obtained by the sprinkling of the dust with agglomerating agents can be still further reduced by compressing the mass While in the moist state.
In accordance with a particular mode of carrying out the invention, bodies of a nature to increase the heat conductivity, for example pieces of .metal in the shape of rods, sheets, or wire, are embedded in the moistened magnesium dust.
.The described method can also be employed to. very great advantage for the pre-treatment of magnesium dust intended for refinement by sublimation in the strict sense of the term, that is 40 to say by the immediate conversion of the metal from the solid into the vaporous state.
The sublimation is preferably effected in a current of a non-oxidizing gas.
The magnesium obtained as a crystalline sublimate is then, if desired, converted into compact metal by various further operations. It can be freely melted together or directly shaped by extrusion or compression.
What I claim is: a 1. The method of producing substantially pure magnesium from magnesium in a finely divided state, which comprises making the finely divided magnesium into a paste with a liquid hydrocarbonaceous impasting agent, heating the said This procedure yields 15 paste up to a temperature at which partial decomposition, by cracking, of the hydrocarbonaceous impasting' agent occurs while agitating the mass under treatment to form solid granular aggregates therefrom, and recovering the magnesium from the said aggregates by sublimation.
2. A method according to claim 1, said sublimation being conducted under reduced pressure. 3. The method of purifying magnesium in a 10 finely divided impure form, which comprises ad mixing the divided magnesium with a liquid hydrocarbonaceous impasting medium to make a paste therefrom, heating said paste, while
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| AT2101904X | 1934-05-04 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US2101904A true US2101904A (en) | 1937-12-14 |
Family
ID=3689846
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US753892A Expired - Lifetime US2101904A (en) | 1934-05-04 | 1934-11-20 | Recovery of compact metallic magnesium from magnesium in finely divided form |
Country Status (1)
| Country | Link |
|---|---|
| US (1) | US2101904A (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2448993A (en) * | 1944-08-26 | 1948-09-07 | Reconstruction Finance Corp | Grain refining magnesium alloys |
| US2477549A (en) * | 1947-01-22 | 1949-07-26 | Permanente Metals Corp | Explosive composition |
| US2509710A (en) * | 1943-07-01 | 1950-05-30 | Kaiser Aluminium Chem Corp | Incendiary |
-
1934
- 1934-11-20 US US753892A patent/US2101904A/en not_active Expired - Lifetime
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2509710A (en) * | 1943-07-01 | 1950-05-30 | Kaiser Aluminium Chem Corp | Incendiary |
| US2448993A (en) * | 1944-08-26 | 1948-09-07 | Reconstruction Finance Corp | Grain refining magnesium alloys |
| US2477549A (en) * | 1947-01-22 | 1949-07-26 | Permanente Metals Corp | Explosive composition |
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