US2179823A - Production of alkaline earth metals - Google Patents
Production of alkaline earth metals Download PDFInfo
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- US2179823A US2179823A US248521A US24852138A US2179823A US 2179823 A US2179823 A US 2179823A US 248521 A US248521 A US 248521A US 24852138 A US24852138 A US 24852138A US 2179823 A US2179823 A US 2179823A
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- United States
- Prior art keywords
- alkaline earth
- mixture
- aluminum
- magnesium
- earth metal
- 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
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- 229910052784 alkaline earth metal Inorganic materials 0.000 title description 35
- 150000001342 alkaline earth metals Chemical class 0.000 title description 35
- 238000004519 manufacturing process Methods 0.000 title description 8
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 51
- 229910052782 aluminium Inorganic materials 0.000 description 47
- 239000000463 material Substances 0.000 description 32
- 239000000203 mixture Substances 0.000 description 32
- FYYHWMGAXLPEAU-UHFFFAOYSA-N Magnesium Chemical compound [Mg] FYYHWMGAXLPEAU-UHFFFAOYSA-N 0.000 description 24
- 229910052749 magnesium Inorganic materials 0.000 description 24
- 239000011777 magnesium Substances 0.000 description 24
- 239000011888 foil Substances 0.000 description 22
- 238000010438 heat treatment Methods 0.000 description 21
- 238000000034 method Methods 0.000 description 21
- CPLXHLVBOLITMK-UHFFFAOYSA-N magnesium oxide Inorganic materials [Mg]=O CPLXHLVBOLITMK-UHFFFAOYSA-N 0.000 description 18
- 239000000395 magnesium oxide Substances 0.000 description 17
- 230000008569 process Effects 0.000 description 17
- AXZKOIWUVFPNLO-UHFFFAOYSA-N magnesium;oxygen(2-) Chemical compound [O-2].[Mg+2] AXZKOIWUVFPNLO-UHFFFAOYSA-N 0.000 description 16
- 229910052751 metal Inorganic materials 0.000 description 14
- 239000002184 metal Substances 0.000 description 14
- 238000009835 boiling Methods 0.000 description 11
- 238000002844 melting Methods 0.000 description 7
- 230000008018 melting Effects 0.000 description 7
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 5
- 238000003723 Smelting Methods 0.000 description 5
- 229910052799 carbon Inorganic materials 0.000 description 5
- 239000007789 gas Substances 0.000 description 5
- 239000011261 inert gas Substances 0.000 description 5
- 239000011872 intimate mixture Substances 0.000 description 5
- 239000003638 chemical reducing agent Substances 0.000 description 4
- 239000000843 powder Substances 0.000 description 4
- 239000011874 heated mixture Substances 0.000 description 3
- 229910000287 alkaline earth metal oxide Inorganic materials 0.000 description 2
- QVQLCTNNEUAWMS-UHFFFAOYSA-N barium oxide Chemical compound [Ba]=O QVQLCTNNEUAWMS-UHFFFAOYSA-N 0.000 description 2
- 230000008901 benefit Effects 0.000 description 2
- 238000006243 chemical reaction Methods 0.000 description 2
- 238000009833 condensation Methods 0.000 description 2
- 230000005494 condensation Effects 0.000 description 2
- 238000011109 contamination Methods 0.000 description 2
- 239000000428 dust Substances 0.000 description 2
- 238000010410 dusting Methods 0.000 description 2
- 239000001257 hydrogen Substances 0.000 description 2
- 229910052739 hydrogen Inorganic materials 0.000 description 2
- 239000007788 liquid Substances 0.000 description 2
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 2
- 239000002245 particle Substances 0.000 description 2
- 230000009467 reduction Effects 0.000 description 2
- IATRAKWUXMZMIY-UHFFFAOYSA-N strontium oxide Chemical compound [O-2].[Sr+2] IATRAKWUXMZMIY-UHFFFAOYSA-N 0.000 description 2
- 238000009736 wetting Methods 0.000 description 2
- OYPRJOBELJOOCE-UHFFFAOYSA-N Calcium Chemical compound [Ca] OYPRJOBELJOOCE-UHFFFAOYSA-N 0.000 description 1
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 description 1
- 229920000742 Cotton Polymers 0.000 description 1
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 1
- 229910052788 barium Inorganic materials 0.000 description 1
- DSAJWYNOEDNPEQ-UHFFFAOYSA-N barium atom Chemical compound [Ba] DSAJWYNOEDNPEQ-UHFFFAOYSA-N 0.000 description 1
- 229910052599 brucite Inorganic materials 0.000 description 1
- 229910052791 calcium Inorganic materials 0.000 description 1
- 239000011575 calcium Substances 0.000 description 1
- BRPQOXSCLDDYGP-UHFFFAOYSA-N calcium oxide Chemical compound [O-2].[Ca+2] BRPQOXSCLDDYGP-UHFFFAOYSA-N 0.000 description 1
- ODINCKMPIJJUCX-UHFFFAOYSA-N calcium oxide Inorganic materials [Ca]=O ODINCKMPIJJUCX-UHFFFAOYSA-N 0.000 description 1
- 239000000292 calcium oxide Substances 0.000 description 1
- 229910002091 carbon monoxide Inorganic materials 0.000 description 1
- 150000004649 carbonic acid derivatives Chemical class 0.000 description 1
- 235000015218 chewing gum Nutrition 0.000 description 1
- 229940112822 chewing gum Drugs 0.000 description 1
- 235000019506 cigar Nutrition 0.000 description 1
- 235000019504 cigarettes Nutrition 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 235000009508 confectionery Nutrition 0.000 description 1
- 238000004821 distillation Methods 0.000 description 1
- 238000004880 explosion Methods 0.000 description 1
- 239000004744 fabric Substances 0.000 description 1
- 235000013305 food Nutrition 0.000 description 1
- 239000008187 granular material Substances 0.000 description 1
- 231100001261 hazardous Toxicity 0.000 description 1
- 229910052734 helium Inorganic materials 0.000 description 1
- 239000001307 helium Substances 0.000 description 1
- SWQJXJOGLNCZEY-UHFFFAOYSA-N helium atom Chemical compound [He] SWQJXJOGLNCZEY-UHFFFAOYSA-N 0.000 description 1
- 150000002431 hydrogen Chemical class 0.000 description 1
- 230000006872 improvement Effects 0.000 description 1
- 239000004615 ingredient Substances 0.000 description 1
- 239000001095 magnesium carbonate Substances 0.000 description 1
- ZLNQQNXFFQJAID-UHFFFAOYSA-L magnesium carbonate Chemical compound [Mg+2].[O-]C([O-])=O ZLNQQNXFFQJAID-UHFFFAOYSA-L 0.000 description 1
- 235000014380 magnesium carbonate Nutrition 0.000 description 1
- 229910000021 magnesium carbonate Inorganic materials 0.000 description 1
- 150000002681 magnesium compounds Chemical class 0.000 description 1
- 229910044991 metal oxide Inorganic materials 0.000 description 1
- 150000004706 metal oxides Chemical class 0.000 description 1
- 239000003595 mist Substances 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 239000011148 porous material Substances 0.000 description 1
- 230000035939 shock Effects 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 229910052712 strontium Inorganic materials 0.000 description 1
- CIOAGBVUUVVLOB-UHFFFAOYSA-N strontium atom Chemical compound [Sr] CIOAGBVUUVVLOB-UHFFFAOYSA-N 0.000 description 1
- 238000006467 substitution reaction Methods 0.000 description 1
- 239000002699 waste material Substances 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
Definitions
- This invention relates to a method and com position for use in the production of alkaline earth metals.
- Alkaline earth metals may be produced-conventionally by electric furnace heating of a reducing agent with a material bearing the oxide of the metal, carbon being an example of the reducing agent.
- Aluminum powder also may be used as the reducing agent. Its use, however, introduces a difficulty. Being combustible, and in extremely finely divided form; the powder is hazardous from the explosion standpoint. Being dusty, it is entrained with the alkaline earth metal vapor, so as to contaminate the metal produced. In addition, there is also waste of the aluminum powder; the loss of powder carried with the vapor makes impossible accurate calculation of amounts of the ingredients to be used in a charge, particularly since the amount of powder lost varies with the rate of release of the alkaline earth metal vapor, which, due to irregularities in furnace operation, cannot always be maintained at a uniform rate.
- the invention comprises the production of an alkaline earth metal by heating a material bearing its oxide with aluminum foil.
- the invention comprises also special means of obtaining very intimate association of the said material with aluminum supplied in the form of foil.
- the invention will be illustrated more particularly by reference 'to the manufacture of magnesium.
- magnesium oxide or a source thereof and admixed aluminum are heated in the absence of air, to avoid oxidation of the metal produced, in a usual type of furnace including electrical heating elements, an
- the vapors are passed through an outlet from the furnace for the magnesium vapor outlet and delivery pipe, advantageously resembling somewhat a tuyere in the side of the furnace, at a position above the level of the charge therein, and thus delivered to a condenser of typecominonly used in the manufacture of mag- I nesium.
- the condensed magnesium may be obtained in finely divided or compact or'masslve form, say, as a powder, liquid or solid, the condensation and coilection of the magnesium being made in an atmosphere of hydrogen or other suitable .inert or reducing gas.
- the aluminum for reducing the magnesium oxide containing compound to the metallic or elemental condition, is foil.
- the aluminum foil used is thin, say, about 0.0025 to 0.0002 inch in thickness. Scrap material from the wrapping of confectionery, food products, cigars, cigarettes, or chewing gum, is satisfactory. 20
- the heat-insulating grade of aluminum foil, either by itself or backed with paper may be used.
- magnesium oxide there is preferred a relatively high grade magnesium oxide, such as that now being manufactured by the wet process and utilized in the commercial production of magnesium compounds. Also there may be used calcined magnesite, (1010- 30 mite or brucite.
- the aluminum foil and the selected source of magnesia are mixed intimately, as in a wheel or pan mill or in other suitable manner.
- the magnesium oxide bearing material in amount somewhat in excess of the aluminum foil as. calculated from the equivalent weights of the two materials.
- the foil may also be shredded preparatory to making up the charge 40 of magnesium oxide and aluminum foil.
- the charge in unbriquetted condition is heated, as, for instance, in a furnace of the kind described, to a temperature at or above the melting point of aluminum.
- the foil softens, it tends, 5 under the large force of its surface tension, to contract into spheres. But it is restrained from doing so by the presence of contacting particles of magnesium oxide. As a result, the foil is drawn into or it surface-wets. the said particles. 5
- the temperature of the mixture is then raised to that of volatilizat-ion of the resulting magnesium, so that magnesium in the form of vapor passes from the furnace to the condensing system.
- the temperature of heating is preferably at least 1,110 C. or somewhat higher. It
- the charge to be used in the production of magnesium may be evacuated, to withdraw a large part or practically all of the gas therefrom. This evacuation may be made if desired in a suitable pretreating vessel that is practically air tight. Evacuation may be made either before, during or after the heating of the charge, but the charge in any case should be above the melting point of aluminum when the vacuum is .0 broken.
- the vacuum is broken by the admission of 'inert (nonoxidizing) gas such as hydrogen, helium or methane.
- 'inert gas such as hydrogen, helium or methane.
- the resulting increase of pressure forces molten aluminum into the evacuated pores or spaces within the finely divided magnesium oxide bearing material, with resultant and very satisfactory association of the components of the mixture.
- the aluminum and the go magnesium oxide bearing material are brought into intimate contact by a process of surface wetting of the oxide by molten aluminum, under the influence of vacuum and pressure successively applied. As a result there is impregna- 'tion of the molten aluminum into the magnesium oxide bearing material.
- An advantage of this wetting and impregnating is that the method can be applied to relatively coarse or granular material, which can be fed into a smelting furnace and reduced so as greatly to minimize the phenomenon of dusting and permit greater speed of reaction and ease of escape of the metallic vapor from the charge. when the evacuation process is used even aluminumpowder may be used without excessive dusting.
- the production of magnesium as described avoids the difliculty of excessive contamination of the distillate by aluminum carried over in finely divided condition. Also, the process is one that may be performed simply and economically, and with an improvement in the quality of the condensed product.
- magnesium oxide bearing material used in the examples above, there may be substituted an equivalent amount of a material containing barium oxide, strontium oxide, or calcium oxide.
- a material containing barium oxide, strontium oxide, or calcium oxide When such substitution is made, the process used to produce the alkaline earth metal is the same as described, final heating in all cases being effected at a temperature somewhat above the boiling point of the metal whose oxidic material has been selected.
- the materials that may be substituted for the magnesium oxide or the like are the carbonates of barium, strontium and calcium, preferably in calcined condition, or any materials that give under smelting conditions the oxide of the alkaline earth metal that is to be produced.
- Aluminum foil backed with paper, cotton fabric or other cellulosic material may be substituted
- the temperature of smelting is raised to that at which the carbon becomes effective.
- the distilled metal vapor is subjected to shock condensation in well known manner, to prevent a reverse reaction between the liberated metal and the carbon monoxide produced from the carbon as reducing agent for the metal oxide.
- bearing or containing
- oxide providing or supplying, under the smelting conditions and at the furnace temperatures recited.
- the process of producing magnesium which comprises forming an intimate mixture of aluminum foil and a finely divided magnesium oxide bearing material, heating the mixture in unbriquetted condition in a furnace in the absence of air to a temperature at least as high as that of volatilization of magnesium and below the boiling point of aluminum, passing the volatilized magnesium from the furnace and then condensing the vapors.
- the process of producing an alkaline earth metal which comprises forming a mixture of aluminum and a finely divided material bearing an oxide of the alkaline earth metal, heating the mixture to a temperature above the melting point of the aluminum and below the boiling point of the alkaline earth metal, evacuating the heated mixture, admitting an inert gas to the evacuated mixture, so as to force molten aluminum into intimate association with the said material, and then heating the mixture to the temperature of volatilization of the alkaline earth metal and distilling the said metal.
- the process of producing magnesium which comprises forming an intimate mixture of aluminum foil and a finely divided magnesium oxide bearing material, evacuating the mixture, heating the evacuated mixture to a temperature above the melting point of the aluminum foil and below the boiling point of the magnesium, admitting an inert gas to the evacuated and heated mixture, so as to force molten aluminum into intimate association with the said material, and then heating the mixture to the temperature of volatilization of magnesium and distilling the resulting magnesium.
- the process of producing magnesium which comprises forming an intimate mixture of finely divided aluminum with a finely divided magnesium oxide bearing material, heating the mixture in an inert atmosphere to a temperature above the melting point of the aluminum and below the boiling point of magnesium, evacuating o the heated mixture, admitting an inert gas to the evacuated mixture so as to force molten aluminum into intimate association with thesaid material, and then heating the mixture to the temperature of volatilization of magnesium and distilling the resulting magnesium.
- the process of producing an alkaline earth metal which comprises forming a mixture of aluminum foil having a cellulosic backing and a material bearing an oxide of the alkaline earth metal, heating the mixture in a furnace in the absence of air to a temperature at least as high as that of volatilization of the alkaline earth metal and below the temperature of reduction of the alkaline earth metal oxide by carbon, passing the volatilized metal from the furnace, and then condensing the vapor.
- the process of producing an alkaline earth metal which comprises forming a mixture of amminum foil having a charred cellulosic backing and a material bearing an oxide of the alkaline earth metal, heating the mixture in a furnace in the absence of air to a temperatureat least as high as that of volatilization of the alkaline earth metal and below the temperature oi reduction of the alkaline earth metal oxide by carbon, passing the volatilized metal from the furnace, and then condensing the vapor.
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)
- Compounds Of Alkaline-Earth Elements, Aluminum Or Rare-Earth Metals (AREA)
Description
Patented Nov. 14, 1939 UNITED STATES PATENT OFFICE No Drawing. Application December 30; 1938, Serial No. 248,521
11 Claims.
This invention relates to a method and com position for use in the production of alkaline earth metals.
Alkaline earth metals may be produced-conventionally by electric furnace heating of a reducing agent with a material bearing the oxide of the metal, carbon being an example of the reducing agent.
Aluminum powder also may be used as the reducing agent. Its use, however, introduces a difficulty. Being combustible, and in extremely finely divided form; the powder is hazardous from the explosion standpoint. Being dusty, it is entrained with the alkaline earth metal vapor, so as to contaminate the metal produced. In addition, there is also waste of the aluminum powder; the loss of powder carried with the vapor makes impossible accurate calculation of amounts of the ingredients to be used in a charge, particularly since the amount of powder lost varies with the rate of release of the alkaline earth metal vapor, which, due to irregularities in furnace operation, cannot always be maintained at a uniform rate.
It is an object of the invention to provide a method in which desired intimacy of contact of aluminum with the selected oxide bearing material may be obtained, without the need of using aluminum powder. Another object is to avoid dust contamination of the distilled alkaline earth metal. Other objects and advantages of the invention will appear from the description which follows.
Briefly stated, the invention comprises the production of an alkaline earth metal by heating a material bearing its oxide with aluminum foil. The invention comprises also special means of obtaining very intimate association of the said material with aluminum supplied in the form of foil.
The invention will be illustrated more particularly by reference 'to the manufacture of magnesium.
The process and equipment used are conventional, except as noted herein. Thus, magnesium oxide or a source thereof and admixed aluminum are heated in the absence of air, to avoid oxidation of the metal produced, in a usual type of furnace including electrical heating elements, an
5 or the like. The vapors are passed through an outlet from the furnace for the magnesium vapor outlet and delivery pipe, advantageously resembling somewhat a tuyere in the side of the furnace, at a position above the level of the charge therein, and thus delivered to a condenser of typecominonly used in the manufacture of mag- I nesium.
The condensed magnesium may be obtained in finely divided or compact or'masslve form, say, as a powder, liquid or solid, the condensation and coilection of the magnesium being made in an atmosphere of hydrogen or other suitable .inert or reducing gas.
A departure is made from the usual practice in that the aluminum, for reducing the magnesium oxide containing compound to the metallic or elemental condition, is foil. Preferably the aluminum foil used is thin, say, about 0.0025 to 0.0002 inch in thickness. Scrap material from the wrapping of confectionery, food products, cigars, cigarettes, or chewing gum, is satisfactory. 20 The heat-insulating grade of aluminum foil, either by itself or backed with paper may be used.
As the magnesium oxide bearing material,
there is preferred a relatively high grade magnesium oxide, such as that now being manufactured by the wet process and utilized in the commercial production of magnesium compounds. Also there may be used calcined magnesite, (1010- 30 mite or brucite.
The aluminum foil and the selected source of magnesia are mixed intimately, as in a wheel or pan mill or in other suitable manner. For the sake of economy in the use of the aluminum foil, I prefer to use the magnesium oxide bearing material in amount somewhat in excess of the aluminum foil as. calculated from the equivalent weights of the two materials. The foil may also be shredded preparatory to making up the charge 40 of magnesium oxide and aluminum foil.
The charge in unbriquetted condition is heated, as, for instance, in a furnace of the kind described, to a temperature at or above the melting point of aluminum. As the foil softens, it tends, 5 under the large force of its surface tension, to contract into spheres. But it is restrained from doing so by the presence of contacting particles of magnesium oxide. As a result, the foil is drawn into or it surface-wets. the said particles. 5
The temperature of the mixture is then raised to that of volatilizat-ion of the resulting magnesium, so that magnesium in the form of vapor passes from the furnace to the condensing system. There is practically no aluminum carried over as dust or as finely divided liquid mist in the distillation of the magnesium.
' Since the boiling point of magnesium is about 1,100 C., the temperature of heating is preferably at least 1,110 C. or somewhat higher. It
is kept well below the boiling point of aluminum but at a temperature sufiiciently high to cause volatilization of liberated magnesium.
To obtain a still more intimate association of 19 the aluminum with the magnesium oxide bearing material, the charge to be used in the production of magnesium may be evacuated, to withdraw a large part or practically all of the gas therefrom. This evacuation may be made if desired in a suitable pretreating vessel that is practically air tight. Evacuation may be made either before, during or after the heating of the charge, but the charge in any case should be above the melting point of aluminum when the vacuum is .0 broken. I
When the aluminum foil has melted, the vacuum is broken by the admission of 'inert (nonoxidizing) gas such as hydrogen, helium or methane. The resulting increase of pressure forces molten aluminum into the evacuated pores or spaces within the finely divided magnesium oxide bearing material, with resultant and very satisfactory association of the components of the mixture. In other words, the aluminum and the go magnesium oxide bearing material are brought into intimate contact by a process of surface wetting of the oxide by molten aluminum, under the influence of vacuum and pressure successively applied. As a result there is impregna- 'tion of the molten aluminum into the magnesium oxide bearing material. An advantage of this wetting and impregnating is that the method can be applied to relatively coarse or granular material, which can be fed into a smelting furnace and reduced so as greatly to minimize the phenomenon of dusting and permit greater speed of reaction and ease of escape of the metallic vapor from the charge. when the evacuation process is used even aluminumpowder may be used without excessive dusting.
Whether the evacuation and subsequent admission of the inert'gas has been efiected in an outside vessel or in the smelting furnace itself, the mixture is now heated in the furnace to distil magnesium therefrom.
The production of magnesium as described avoids the difliculty of excessive contamination of the distillate by aluminum carried over in finely divided condition. Also, the process is one that may be performed simply and economically, and with an improvement in the quality of the condensed product.
In place of the magnesium oxide bearing material used in the examples above, there may be substituted an equivalent amount of a material containing barium oxide, strontium oxide, or calcium oxide. When such substitution is made, the process used to produce the alkaline earth metal is the same as described, final heating in all cases being effected at a temperature somewhat above the boiling point of the metal whose oxidic material has been selected.
Among the materials that may be substituted for the magnesium oxide or the like are the carbonates of barium, strontium and calcium, preferably in calcined condition, or any materials that give under smelting conditions the oxide of the alkaline earth metal that is to be produced. Aluminum foil backed with paper, cotton fabric or other cellulosic material may be substituted In a modification of the method using the toil with cellulosic backing, the temperature of smelting is raised to that at which the carbon becomes effective.
In that case, the distilled metal vapor is subjected to shock condensation in well known manner, to prevent a reverse reaction between the liberated metal and the carbon monoxide produced from the carbon as reducing agent for the metal oxide.
It will be understood that the term bearing" or containing" as applied to the oxide is used herein to include oxide providing or supplying, under the smelting conditions and at the furnace temperatures recited.
It will be understood, also, that the details given are for the purpose of illustration, not restriction, and that variations within the spirlt of the invention are intended to be included in the scope of the appended claims.
I claim:
1. The process of producing an alkaline earth metal which comprises forming a mixture of aluminum foil and a material bearing an oxide of the alkaline earth metal, heating the mixture in unbriquetted condition in a furnace in the absence of air to a temperature at least as high as that of volatilization of the alkaline earth metal and below the boiling point of aluminum, passing the volatilized metal from the furnace, and then condensing the vapor.
2. The process of producing an alkaline earth metal which comprises forming a mixture of aluminum foil and a finely divided oxide of an alkaline earth metal, heating the mixture in unbriquetted condition in a furnace in the absence of air to a temperature at least as high as that of volatilization of the alkaline earth metal and below the boiling point of aluminum, passing the volatilized metal from the furnace, and then condensing the vapors.
3. The process of producing magnesium which comprises forming an intimate mixture of aluminum foil and a finely divided magnesium oxide bearing material, heating the mixture in unbriquetted condition in a furnace in the absence of air to a temperature at least as high as that of volatilization of magnesium and below the boiling point of aluminum, passing the volatilized magnesium from the furnace and then condensing the vapors.
4. The process of producing an alkaline earth metal which comprises forming a mixture or aluminum foil of thickness of the order of 0.0025 to6.0002 inch and a finely divided material bearing an oxide of the alkaline earth metal, heating the mixture in unbriquetted condition in a furnace in the absence of air to a temperature at least as high as that of volatilization of the alkaline earth metal, passing the volatilized metal from the furnace, and then condensing the vapors.
5. The process of producing an alkaline earth metal which comprises forming a mixture of aluminum and a finely divided material bearing an oxide of the alkaline earth metal, heating the mixture to a temperature above the melting point of the aluminum and below the boiling point of the alkaline earth metal, evacuating the heated mixture, admitting an inert gas to the evacuated mixture, so as to force molten aluminum into intimate association with the said material, and then heating the mixture to the temperature of volatilization of the alkaline earth metal and distilling the said metal.
6. The process of producing an alkaline earth metal which comprises forming an intimate mixture of aluminum and a material bearing an oxide of the alkaline earth metal, heating the mixture in an inert atmosphere to a temperature above the melting point of the aluminum and below the boiling point of the alkaline earth metal, evacuating the mixture, admitting an inert gas to the evacuated mixture subsequent to the melting of the aluminum, so as to force molten aluminum into intimate association with the said material, and then heating the mixture to the temperature of volatilization of the said metal and distilling the metal.
7. The process of producing magnesium which comprises forming an intimate mixture of aluminum foil and a finely divided magnesium oxide bearing material, evacuating the mixture, heating the evacuated mixture to a temperature above the melting point of the aluminum foil and below the boiling point of the magnesium, admitting an inert gas to the evacuated and heated mixture, so as to force molten aluminum into intimate association with the said material, and then heating the mixture to the temperature of volatilization of magnesium and distilling the resulting magnesium.
8. The process of producing magnesium which comprises forming an intimate mixture of finely divided aluminum with a finely divided magnesium oxide bearing material, heating the mixture in an inert atmosphere to a temperature above the melting point of the aluminum and below the boiling point of magnesium, evacuating o the heated mixture, admitting an inert gas to the evacuated mixture so as to force molten aluminum into intimate association with thesaid material, and then heating the mixture to the temperature of volatilization of magnesium and distilling the resulting magnesium.
9. The process of producing an alkaline earth metal which comprises forming a mixture of aluminum foil having a cellulosic backing and a material bearing an oxide of the alkaline earth metal, heating the mixture in a furnace in the absence of air to a temperature at least as high as that of volatilization of the alkaline earth metal and below the temperature of reduction of the alkaline earth metal oxide by carbon, passing the volatilized metal from the furnace, and then condensing the vapor.
10. The process of producing an alkaline earth metal which comprises forming an intimate mixture of aluminum and a material bearing an oxide of the alkaline earth metal, evacuating the mixture, admitting to the evacuated mixture 9. gas that is inert to aluminum and magnesium, heating the mixture in an atmosphere of the inert gas to the temperature of volatilization of the alkaline earth metal but below the boiling point of aluminum, separating the resulting vapor 'of the alkaline earth metal from the said mixture, and then condensing the vapor.
11. The process of producing an alkaline earth metal which comprises forming a mixture of amminum foil having a charred cellulosic backing and a material bearing an oxide of the alkaline earth metal, heating the mixture in a furnace in the absence of air to a temperatureat least as high as that of volatilization of the alkaline earth metal and below the temperature oi reduction of the alkaline earth metal oxide by carbon, passing the volatilized metal from the furnace, and then condensing the vapor.
FRANK R. KEMMER.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US248521A US2179823A (en) | 1938-12-30 | 1938-12-30 | Production of alkaline earth metals |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US248521A US2179823A (en) | 1938-12-30 | 1938-12-30 | Production of alkaline earth metals |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US2179823A true US2179823A (en) | 1939-11-14 |
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ID=22939515
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US248521A Expired - Lifetime US2179823A (en) | 1938-12-30 | 1938-12-30 | Production of alkaline earth metals |
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| Country | Link |
|---|---|
| US (1) | US2179823A (en) |
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2461697A (en) * | 1947-09-23 | 1949-02-15 | Augustin L J Queneau | Recovery of zinc from its ores |
| US2464767A (en) * | 1945-09-06 | 1949-03-15 | Dominion Magnesium Ltd | Production of calcium |
| US2527722A (en) * | 1946-05-27 | 1950-10-31 | North Carolina Magnesium Dev C | Production of magnesium |
| US2527724A (en) * | 1946-05-27 | 1950-10-31 | North Carolina Magnesium Dev C | Production of magnesium |
| US2527723A (en) * | 1946-05-28 | 1950-10-31 | North Carolina Magnesium Dev C | Recovery of values from aluminum scrap |
| US2988444A (en) * | 1952-05-29 | 1961-06-13 | Hurum Fredrik Jorgen Ording | Method and apparatus for treating molten metal |
-
1938
- 1938-12-30 US US248521A patent/US2179823A/en not_active Expired - Lifetime
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2464767A (en) * | 1945-09-06 | 1949-03-15 | Dominion Magnesium Ltd | Production of calcium |
| US2527722A (en) * | 1946-05-27 | 1950-10-31 | North Carolina Magnesium Dev C | Production of magnesium |
| US2527724A (en) * | 1946-05-27 | 1950-10-31 | North Carolina Magnesium Dev C | Production of magnesium |
| US2527723A (en) * | 1946-05-28 | 1950-10-31 | North Carolina Magnesium Dev C | Recovery of values from aluminum scrap |
| US2461697A (en) * | 1947-09-23 | 1949-02-15 | Augustin L J Queneau | Recovery of zinc from its ores |
| US2988444A (en) * | 1952-05-29 | 1961-06-13 | Hurum Fredrik Jorgen Ording | Method and apparatus for treating molten metal |
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