US2429668A - Metallurgical furnace and condenser - Google Patents
Metallurgical furnace and condenser Download PDFInfo
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- US2429668A US2429668A US453984A US45398442A US2429668A US 2429668 A US2429668 A US 2429668A US 453984 A US453984 A US 453984A US 45398442 A US45398442 A US 45398442A US 2429668 A US2429668 A US 2429668A
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- 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
- C22B5/00—General methods of reducing to metals
- C22B5/02—Dry methods smelting of sulfides or formation of mattes
- C22B5/16—Dry methods smelting of sulfides or formation of mattes with volatilisation or condensation of the metal being produced
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- 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 metallurgical furnaces and more particularly to apparatus ⁇ adapted for the reduction of metal' oxides at reduced pressures and for the vacuum distillation and condensation of the metal constituent of said oxides.
- One of the objects of the present invention is to provide an improved apparatus' for the reduction of metal oxides under reduced pressures.
- Another object is to provide an improved apparatus'ior the reduction of metal oxides under reduced pressures and for the distillation and condensation of the metal constitutent of the said oxides,
- Another object isvto provide an improved ap paratus in which to practice the reduction of magnesium oxide by a high boiling point reducing agent, at reduced pressures at temperatures above the vaporization temperature of magnesium. with resultant vaporization and condensation of the magnesium at a point removed from the temperature zone of reduction.
- Still another object is to provide anv improved apparatus for the production of metallic magnesium.
- Fig. 1 is a sectionalside elevational view of th apparatus of the present invention
- Fig. 2 is a sectional view taken along plane 2-'2 of Fig. l;
- Fig. 3 is a sectional view taken yalong plane 3 3 of Fig. 1;
- Fig. 4 is a bottom view along plane 4 4 of Fig.1:'
- Fig, 5 is a side elevational view partly in section illustrating one practical mode of-applying the apparatus of Fig. 1 commercially;
- Fig. 6 illustrates one feature of the present invention
- Y z Fig. 7v illustrates a second feature of the present invention.
- Another. essential difficulty is to effect the condensation of the magnesium vapors in such a manner as to promote the formation of large grains or masses of sufficient size as to resist spontaneous combustion when the exposed surfaces thereof are subjected to oxidation.
- Serial No. 435,678 led nesium which is featured by the use of a depending water-cooled condenser disposed interiorly the apparatus in relatively close spaced relation to the point of origin of the magnesium vapors which provides for the condensation.
- the present apparatus combines this feature of i my said co-pending application Serial No. 435,678
- the oper- Vwith other features in the design of a vacuum reduction .and distillation and condensing furnace, that is adapted for'wide utility in the art in the reduction of substantially all metal oxides whose metallic constituent may be vaporized at low pressures at temperatures up toabout 1500 C., but which in the specific embodiment shown, is specifically designed for the reduction of magnesium oxide by calcium silicide at temperatures within the range o-1150 C.
- the vacuum reduction-distilling-and condensation apparatus ofthe present invention comprises an elongated vertically sustained chamber A, preferably circular in cross-section, having a portion of its length intermediate the ends thereof enclosed by a means M to heat the same to any desired temperature.
- means M comprises a tubular refractory member I sustained within refractory enclosure ilV in spaced relation to the outery surface of tubular chamber B and electrical resistance heating element l2 disposed adjacent the surface of tubular refractory member I0 opposite to the face lying in spaced relation to the outer surface of tubular chamber A.
- Any alternative means for heating chamber A in substantially the same manner may be substituted for the means shown, without departure from the present invention, but the means shown is preferred as will be morefully hereinafter disclosed.
- the upper endvof chamber A is provided with a removable condensing chamber B and the bottom end of the chamber A is provided with a detachable closure means C.
- Means D which is essentially a platform also is provided to sustain a refractory container or crucible E fllled with a charge consisting of a briquetted mixture of MgO and CaSiz in approximately equivalent molecular weight proportions, in heating position Within the heated portion of chamber A and means, such as-conduit G communicating to the interior of chamber A, is provided through valve V1, to lower. the pressure within chamber A or through valve V2, to introduce any desired gas within the chamber A.
- the specic size, shape and configuration of condensing chamber B and closure means C may be varied Widely without essential departure from and nitrogen or helium, to a pressure approximating atmospheric pressure which releases vacuum seal Hz on closure member C permitting the removal of the member and the removal of crucible E- from chamber A and the insertion of a second crucible E lled with fresh charge F in heating position within the chamber A and a reseating of closure member C in closure position on the end of chamber A without subjecting the condensed metal l5 to oxidation and Without interrupting the heating of the heated portion of chamber A.
- the means provided is adapted to accomplish the desired result, namely, the heating of charge F contained within crucible E to a temperature, at the low pressure provided,- at which the reduction reaction, resulting in the formation of a vaporizable metal (Mg), proceeds with simultaneous vaporization of the metal and condensation of the metal vapors upon the surface I4 of vwater-cooled condenser i3 which is dependingly sustained interiorly within condenser chamber B with its condensingv surface Il disposed in spaced and covering position over crucible E, so as to provide a relativelyv short path of travel of the metal vapors from the crucible to the condensing metal I5 collecting thereon at a. temperature at which the deposited metal vapors undergo grain growth 'into relatively large sized masses,
- the major advantage of the arrangement shown is that a plurality of crucibles E may be heated successively 'within chamber A without removing condenser chamber B from closure position on theupper end of chamber A. This is obtained byl closing valve V1 and opening valve V: lling the. chamber A with a. relatively light inert gas, such as non-explosive'mixture o! hydrogen se, form no part of the present invention, being adapted to perform substantially the same functional result in the present apparatus as described and claimed therefor in my said co-pending application.
- a. relatively light inert gas such as non-explosive'mixture o! hydrogen se
- vacuum seals H1 and H2 each consist of annular resilient members and annular extensions disposed in engaging position oppositely to each other on the opposite parts which it is desired t0 vacuum seal together.
- One marked advantage of the arrangement shown for heating chamber A lies in the feature of providing tubular refractory member I0 adjacent the outer surface of the chamber A, but
- the exterior surface of the heated portion of chamber A is protected from oxidation, by means of a protective reducing gas, such as Hz, cracked-am conduct the gases flowing through' the space gap to a point remote from the apparatus lfor burning or for reclaiming, as may be desired.
- a protective reducing gas such as Hz
- the protective gas is introduced, within the refractory enclosure Il, which is sealed from the atmosphere in any convenient manner wel1 known in the art, by means of pipe I1, filling the enclosure and surrounding heating element I2'protecting the same fromoxidation and passing through openings I8 in the bottom of tubular refractory member I0 into the space gap between this member I0 and the wall of chamber A enclosed thereby, and thence out through conduit I6 to the Vdischarge point.
- Another advantage of the present invention resides in the production possibilities obtained through the use of a battery of such reduction, distillation and condensing furnaces, illustrated in Fig. l in combination with a melting furnace.
- a second chamber B may be immediately disposed in closure position on the end of chamber A, and chamber A may be recharged as hereinabove described following a short heated cycle in the presence of an inert gas to remove water vapor and air from chamber B.
- a metallurgical furnace for the vacuum production of readily vaporized metals such as magnesium comprising an elongated vertically sustained metallic container open at member being provided with an interiorly depending water cooled condenser chamber, means to sustain a crucible within the heated portion of said container, and means to obtain and maintain a desired low pressure of an atmosphere within'the interior of the container.
- a plurality of. furnaces of the type described and Aclaimed in claim 1 sustained vertically in spaced relation and at least one melting furnace, saidmelting furnace containing a bath of molten fiuxheated to a tem,- perature approximating the melting point of the vaporizable metal produced in the said metal- :lurgical furnaces and condensed upon the inabove the melting point of the condensed metal plication Serial No. 453,051.
- an elongated vertically sustained tubular metallic container open at both ends and provided at each said end with water cooling means to maintain the temperatures of said open ends at approximately atmospheric temperatures, the upper said end being provided with an upwardly facing area having an annular recess therein with an annular gasket of resilient material seated therein and the said bottom end being provided with a depending annular extension, a vaulted closure member for the upper said end, said member having an interior depending Water cooled condenser and being provided with an annular extension on the bottom thereof to engage and seat upon the said annular gasket, a closure member for the bottom end of said container, said member being provided with an annular recess in the face thereof containing an annular gasket of resilient material to engage and seat upon said annular extension on the said bottom end of the container, means removably securing the said bottom closure member in closure position upon the bottom end of said container, means to heat a portion of the length of said container intermediate the
- Metallurgical apparatus for the production under reduced pressures of' vaporizable metals such as magnesium, said apparatus comprising in combination an elongated vertically sustained .tubular metal container, means to heat an ex- A heated surface of said container and means to flow a reducing and non-oxidizing gas under pressure through the space gap therebetween, means to water-cool the opposite open ends of said bottom closure member in closure position on the open end of saidvcontainer, said means providing substantially free vertical movement of the closure member upwardly from its secured position, means to sustain a crucible in position within said heated portion of said container,
- At least one melting furnace provided with an open end adapted to receive in closureposition the said vaulted condenser chambers with the said interiorly depending water cooled condenser thereof disposed within the melting furnace and substantially immersed in a bath of molten ux move the said vaulted condenser chambers from closure position on the said vacuum furnace to l closure position on the said melting furnace and 'Vice Versa.
- Metallurgical apparatus for the production of vaporizable metals, such as magnesium, said apparatus comprising in combination a plurality of metallurgical furnaces each consisting of an elongated tubular ⁇ metal container each of subvtemperatures and with top and bottom closure members detachably secured in vacuum tight relation to the upper and lower open ends thereof with the top said closure member beingr vaulted 15 and provided with an interiorly depending water cooled condenser, means vto sustain a crucible ⁇ interiorly of each lsaid container within the heated portion thereof and means to maintain a desired lreduced pressure within said container, and at least one melting furnace, said melting furnace consisting of a container having at the top thereof an outside diameter approximating the inside diameter of the vaulted top closure members of the said metallurgical furnaces and' 25 an outer annular support means in a position to sustain the said closure member in closure position over the said melting furnace with the depending condenser thereof substantially immersed in a bath of molten flux contained in the melting furnace, and
Description
Oct. 28, '1947. H. s. COOPER A METALLURGICAL FURNACB AND CONDENSER Filed Aug. 7. 1942.
3 Sheets-Sheet 1' [yl/f l INVENTOR. flug/1.1000510* Imm *Oct 28, 1947. H. s. COOPER METADLURGICAL FURNACE AND CONDENSER 3 Sheeis-Sheet 2 Filed Aug. 7, 1942 Patented Oct. 1947 METLLURGICAL FURNACE AND CONDENSER Hugh S. Cooper,'Cleveland, Ohio, assignor, by direct and mesne assignments, to Acme Aluminum Alloys, Inc.,Da'yton, Ohio, a corporation of Ohio Application August '1, 1942, serial` No. 453,984
This invention relates to metallurgical furnaces and more particularly to apparatus `adapted for the reduction of metal' oxides at reduced pressures and for the vacuum distillation and condensation of the metal constituent of said oxides.
One of the objects of the present invention is to provide an improved apparatus' for the reduction of metal oxides under reduced pressures.
Another object is to provide an improved apparatus'ior the reduction of metal oxides under reduced pressures and for the distillation and condensation of the metal constitutent of the said oxides,
Another object isvto provide an improved ap paratus in which to practice the reduction of magnesium oxide by a high boiling point reducing agent, at reduced pressures at temperatures above the vaporization temperature of magnesium. with resultant vaporization and condensation of the magnesium at a point removed from the temperature zone of reduction.
Still another object is to provide anv improved apparatus for the production of metallic magnesium. Y
Other objects will be apparent as the invention is more fully hereinafter disclosed;
In accordance with these objects, I have devised the metallurgical apparatus illustrated in the accompanying drawings, of which the following is av full and complete description:
In the drawings:
Fig. 1 is a sectionalside elevational view of th apparatus of the present invention;
Fig. 2 is a sectional view taken along plane 2-'2 of Fig. l;
Fig. 3 is a sectional view taken yalong plane 3 3 of Fig. 1;
Fig. 4 is a bottom view along plane 4 4 of Fig.1:'
Fig, 5 is a side elevational view partly in section illustrating one practical mode of-applying the apparatus of Fig. 1 commercially;
Fig. 6 illustrates one feature of the present invention, and Y z Fig. 7v illustrates a second feature of the present invention.
In the production of magnesium by a process involving the reduction of its oxide by a metallic reducing agent at reduced pressures and at temperatures above the vaporization temperature of the magnesium, but below'the vaporization tems claims, (ci. ess-17) I and condensation of magnesium must be performed in a closed and evacuated container.
One of the essentialdiiliculties in this general method of reducing magnesium and other metal oxides is to nd and employ ametallic reducing agent which will effect the reduction of the magnesium oxide at a commercially practical temperature within the range of temperatures easily obtained and maintained by known heat generating equipment Without the use' of special heat-resistant materials.` In co-pending application Serial No. 453,051 filed July 31, 1942, lnow Patent 2,387,979 issued Oct. 30, 1945. I have disclosed such a metallic reducingagent, namely, calcium sillcide (CaSizlwhich is eiective as a reducing-agent for magnesium oxide at temperatures within the range 900-1150 C. at reduced pressures below about 1 millimeter of mercury,
Another. essential difficulty is to effect the condensation of the magnesium vapors in such a manner as to promote the formation of large grains or masses of sufficient size as to resist spontaneous combustion when the exposed surfaces thereof are subjected to oxidation. In co- 'pending application Serial No. 435,678 led nesium which is featured by the use of a depending water-cooled condenser disposed interiorly the apparatus in relatively close spaced relation to the point of origin of the magnesium vapors which provides for the condensation. of the magnesium vapors on a'water-cooled surface thereof at a temperature approximating but below the freezing or solidiilcation temperature thereby obtaining grain growth o f the deposited magnesium vapors into crystalline structures having a large mass relative to its surface' area, which protects the deposited magnesium from being heated up on surface oxidation to a temperature at which it will vaporine and spontaneously combust.
The present apparatus combines this feature of i my said co-pending application Serial No. 435,678
perature o'f the metallic reducing agent, the oper- Vwith other features, in the design of a vacuum reduction .and distillation and condensing furnace, that is adapted for'wide utility in the art in the reduction of substantially all metal oxides whose metallic constituent may be vaporized at low pressures at temperatures up toabout 1500 C., but which in the specific embodiment shown, is specifically designed for the reduction of magnesium oxide by calcium silicide at temperatures within the range o-1150 C.
ations of reduction, volatilization of magnesium 5| lReferring to the drawings, the vacuum reduction-distilling-and condensation apparatus ofthe present invention comprises an elongated vertically sustained chamber A, preferably circular in cross-section, having a portion of its length intermediate the ends thereof enclosed by a means M to heat the same to any desired temperature. In the specic embodiment shown in Fig. 1, means M comprises a tubular refractory member I sustained within refractory enclosure ilV in spaced relation to the outery surface of tubular chamber B and electrical resistance heating element l2 disposed adjacent the surface of tubular refractory member I0 opposite to the face lying in spaced relation to the outer surface of tubular chamber A. Any alternative means for heating chamber A in substantially the same manner may be substituted for the means shown, without departure from the present invention, but the means shown is preferred as will be morefully hereinafter disclosed. y Y
The upper endvof chamber A is provided with a removable condensing chamber B and the bottom end of the chamber A is provided with a detachable closure means C. Means D which is essentially a platform also is provided to sustain a refractory container or crucible E fllled with a charge consisting of a briquetted mixture of MgO and CaSiz in approximately equivalent molecular weight proportions, in heating position Within the heated portion of chamber A and means, such as-conduit G communicating to the interior of chamber A, is provided through valve V1, to lower. the pressure within chamber A or through valve V2, to introduce any desired gas within the chamber A.
It is preferable to provide means, suchA as water-cooled vacuum seals Hi-Hz to removably and to detachably secure condensing chamber B and closure means C, respectively, in position on the opposite ends of chamber A.
The specic size, shape and configuration of condensing chamber B and closure means C may be varied Widely without essential departure from and nitrogen or helium, to a pressure approximating atmospheric pressure which releases vacuum seal Hz on closure member C permitting the removal of the member and the removal of crucible E- from chamber A and the insertion of a second crucible E lled with fresh charge F in heating position within the chamber A and a reseating of closure member C in closure position on the end of chamber A without subjecting the condensed metal l5 to oxidation and Without interrupting the heating of the heated portion of chamber A.
While the second crucible and its contents are heating up to the reaction temperature the gas pressure contained therein may be reduced to the desired pressure byfclosing .valve V2 and re` tion Serial No. 435,678, above identified, and, per
the present invention, as one skilled in the art may readily perceive; as may also the specific arrangement provided by means D to sustain crucible E within the heated portion of chamber A.
With the arrangement shown in Fig. 1, however, the means provided is adapted to accomplish the desired result, namely, the heating of charge F contained within crucible E to a temperature, at the low pressure provided,- at which the reduction reaction, resulting in the formation of a vaporizable metal (Mg), proceeds with simultaneous vaporization of the metal and condensation of the metal vapors upon the surface I4 of vwater-cooled condenser i3 which is dependingly sustained interiorly within condenser chamber B with its condensingv surface Il disposed in spaced and covering position over crucible E, so as to provide a relativelyv short path of travel of the metal vapors from the crucible to the condensing metal I5 collecting thereon at a. temperature at which the deposited metal vapors undergo grain growth 'into relatively large sized masses,
\ by the heat energy radiated thereto from the heated crucible.
The major advantage of the arrangement shown is that a plurality of crucibles E may be heated successively 'within chamber A without removing condenser chamber B from closure position on theupper end of chamber A. This is obtained byl closing valve V1 and opening valve V: lling the. chamber A with a. relatively light inert gas, such as non-explosive'mixture o! hydrogen se, form no part of the present invention, being adapted to perform substantially the same functional result in the present apparatus as described and claimed therefor in my said co-pending application. It is believed unnecessary to specilically describe the same in view of the clear illustration thereof in the drawings.` However, attention is directed to the fact that vacuum seals H1 and H2 each consist of annular resilient members and annular extensions disposed in engaging position oppositely to each other on the opposite parts which it is desired t0 vacuum seal together. The mechanical engagement of the two annular members, either by the force of gravity as in the case of the joint between' the condensing chamberv B and chamber A or mechanically as indicated in the case of closure member C o`n the bottom end of chamber A, operates to form an hermetic seal therebetween, which seal becomes a vacuum tight seal with decrease in pressure in the interior of chamber A as a result of the movement of the two closures B and C against the upper and lower ends of chamber A, incident to the gas and air pressure differential between the inside and outside of chamber A.
One marked advantage of the arrangement shown for heating chamber A lies in the feature of providing tubular refractory member I0 adjacent the outer surface of the chamber A, but
- in spaced relation thereto. IThe problem solved However, there are many other steels which,
while lacking in high temperature oxidation resistance, nevertheless when protected from oxidation possess the requisite high temperature strength to4 withstand continued or repeated heating to relatively high temperatures underthe stress conditions imposed by the pressure differentials existing in the present apparatus, y v
In the heating arrangement shown, the exterior surface of the heated portion of chamber A is protected from oxidation, by means of a protective reducing gas, such as Hz, cracked-am conduct the gases flowing through' the space gap to a point remote from the apparatus lfor burning or for reclaiming, as may be desired.
Where the means for heating tubular refracscribed in connection with the recharging operation. The introduction of an inert gas in chamber A normally doesnot break the hermetic seal connection between the engaging annular parts of seal Hi, however, as the pressure within container A becomes equal to atmospheric pressure container B may be readily removed from its closure position on the end of chamber "A, as by the vertical displacement 'of condenser tory member I0 and the enclosed length of cham- 'r ber A. to the desired temperature comprises the it is preferable to utilize this protective gasV to protect the incandescent metalof the heating coil from oxidation also. In the arrangement shown in Fig. 1, the protective gas is introduced, within the refractory enclosure Il, which is sealed from the atmosphere in any convenient manner wel1 known in the art, by means of pipe I1, filling the enclosure and surrounding heating element I2'protecting the same fromoxidation and passing through openings I8 in the bottom of tubular refractory member I0 into the space gap between this member I0 and the wall of chamber A enclosed thereby, and thence out through conduit I6 to the Vdischarge point. By tightly sealing the jointbetween chamber A andthe top and bottom Walls of refractory enclosure Il, the entire enclosed length of chamber A thus is protected from oxidation.
When electrical resistance heating is dispensed with and means, such as gas or oil fired burners I, are employed, as is also common in the art, it is preferable to omit holes I8 in the bottom of refractory member I0 and to introduce the protective gas directly into the space gap through tubes I1', as indicated in Fig. 5. l v
Another advantage of the present invention, resides in the production possibilities obtained through the use of a battery of such reduction, distillation and condensing furnaces, illustrated in Fig. l in combination with a melting furnace.
Referring to Fig. 5, these advantages will be ap` parent.
. electrical resistance heating coil or element I 2,
chamber B upwardly by the means T. Any convenient means may be employed for this purpose, the means, per se, forming no part of the present invention. l
Where continuous operation of the apparatus is desired, a second chamber B may be immediately disposed in closure position on the end of chamber A, and chamber A may be recharged as hereinabove described following a short heated cycle in the presence of an inert gas to remove water vapor and air from chamber B.
It is believed apparent from the above description and accompanying drawings thatthe present invention may be widely modified without essential departure therefrom and all such modifications and adaptations-are contemplated as may fall within the scope of the following claims.
What I claim is:
1. A metallurgical furnace for the vacuum production of readily vaporized metals such as magnesium, said furnace comprising an elongated vertically sustained metallic container open at member being provided with an interiorly depending water cooled condenser chamber, means to sustain a crucible within the heated portion of said container, and means to obtain and maintain a desired low pressure of an atmosphere within'the interior of the container.
2. The furnace of claim 1, wherein means is provided to prevent oxidation of the heated exv terior surface of said container, said means com- In the arrangement shown, a plurality of furmaintained, as by burner 2|, at a temperatureprising a tubular refractory body disposed in spaced relation to the said heated surface and means to flow a reducing and nonoxidizing gas under pressure through the space gap between said'refractory body and the exterior heated' surface of the said container.
3. In combination, a plurality of. furnaces of the type described and Aclaimed in claim 1, sustained vertically in spaced relation and at least one melting furnace, saidmelting furnace containing a bath of molten fiuxheated to a tem,- perature approximating the melting point of the vaporizable metal produced in the said metal- :lurgical furnaces and condensed upon the inabove the melting point of the condensed metal plication Serial No. 453,051.
- Before condenser chamber B is removed from closure position over chamber A, it is, of course, necessary to release the vacuum by filling the teriorly depending water cooled condenser of the top closure means thereof, the open end of said melting furnace being provided with means to `sustain the said top kclosure means of the said metallurgical furnaces in closure position thereon with the said interiorly depending condenser means thereof substantially immersed in the said molten flux, and transfer means to move the said top closure members from closure position on the chamber A with inert gas as hereinabove de 75 of an elongated vertically sustained tubular metal tainer from surface-oxidation, said means comprising a tubular refractory body .sustained in determined spaced relation to the heated surface of the container and means to flow a reducing and non-oxidizing gas under pressure through the space gap therebetween.
5. In a metallurgical furnace for the production of vaporizable metals under reduced pressure, an elongated vertically sustained tubular metallic container open at both ends and provided at each said end with water cooling means to maintain the temperatures of said open ends at approximately atmospheric temperatures, the upper said end being provided with an upwardly facing area having an annular recess therein with an annular gasket of resilient material seated therein and the said bottom end being provided with a depending annular extension, a vaulted closure member for the upper said end, said member having an interior depending Water cooled condenser and being provided with an annular extension on the bottom thereof to engage and seat upon the said annular gasket, a closure member for the bottom end of said container, said member being provided with an annular recess in the face thereof containing an annular gasket of resilient material to engage and seat upon said annular extension on the said bottom end of the container, means removably securing the said bottom closure member in closure position upon the bottom end of said container, means to heat a portion of the length of said container intermediate the ends thereof to elevated temperatures, means to sustain a crucible within said heated portion of said container, and means to provide a desired reduced pressure of a gas atmosphere within said container.
6. Metallurgical apparatus for the production under reduced pressures of' vaporizable metals such as magnesium, said apparatus comprising in combination an elongated vertically sustained .tubular metal container, means to heat an ex- A heated surface of said container and means to flow a reducing and non-oxidizing gas under pressure through the space gap therebetween, means to water-cool the opposite open ends of said bottom closure member in closure position on the open end of saidvcontainer, said means providing substantially free vertical movement of the closure member upwardly from its secured position, means to sustain a crucible in position within said heated portion of said container,
y and means to introduce a desired low pressure of an atmosphere within the container.
'7. In a lmetallurgical furnace for the production of vaporizable metals under reduced pressures, the combination of an elongated vertically sustained metallic container open at both ends and provided at each said open end with Water cooling means to maintain the temperatures of said ends at approximately atmospheric temperatures, an annular gasket consisting of resilient material seated in an annular recess in the upper face of the upper water cooled end of said container, an annular rib extension depending from the bottom water cooled end of said container, lneans to heat an extended length of said container intermediate the said water cooled ends of the container, means to protect the exterior surface 'of said heated portion from oxidation, said means including a tubular refractory body located in spaced relation to the said exterior surface of said heated portion and means to flow a reducing and non-oxidizing gas under pressure through the space gap therebetween, a vaulted closure member for the upper water cooled end of said container, the open end of said closure being provided with an annular rib' extension adapted to engage and to seat upon the annular gasket in the upper face of the said upper water cooled end of the container and being provided with an interiorly depending water cooled condenser chamber, a closure member for the bottom water cooled end of said container, said closure member being provided with an annular gasket consisting of resilient material seated in be movable vertically upward in response to pressure differentials between the atmospheres interior and exterior the container, means to removably sustain a charge containing crucible within the said container Within the heated portion of the length thereof, and means to provide a desired reduced pressurey of an atmosphere within .said container when the said lend closure y members are located in closure position on each said container, an annular gasket consisting of resilient material disposed in an annular recess in an upwardly facing surface of the upper end of the container and a vaulted closure member for the said upper open end of the container, said member being provided with an annular rib extension on the bottom face thereof to engag and seat upon said annular gasket in the said upper end of the container and with an interiorly depending water cooled condenser surface,a depending annular rib extension on the bottom open end of the said container, a closure member for the said bottom end, said member being provided with an annular recess and with an annular gasket consisting of resilient material seated in said recess to engage and seat upon said annular rib extension depending from the said bottom end of the container, means to removably secure the v in said melting furnace, and transfer means to water cooled end of said container.
8. In apparatus for the production lof Vaporizable metals, such as magnesium,the combination of a plurality of vertically sustained vacuum furnaces, each provided with a vaulted condenser chamber seated in removable closure position upon the open upper ends of said vacuum furnaces, each said chamber being provided with an interiorly depending water cooled condenser, and
at least one melting furnace provided with an open end adapted to receive in closureposition the said vaulted condenser chambers with the said interiorly depending water cooled condenser thereof disposed within the melting furnace and substantially immersed in a bath of molten ux move the said vaulted condenser chambers from closure position on the said vacuum furnace to l closure position on the said melting furnace and 'Vice Versa.
9. Metallurgical apparatus for the production of vaporizable metals, such as magnesium, said apparatus comprising in combination a plurality of metallurgical furnaces each consisting of an elongated tubular` metal container each of subvtemperatures and with top and bottom closure members detachably secured in vacuum tight relation to the upper and lower open ends thereof with the top said closure member beingr vaulted 15 and provided with an interiorly depending water cooled condenser, means vto sustain a crucible` interiorly of each lsaid container within the heated portion thereof and means to maintain a desired lreduced pressure within said container, and at least one melting furnace, said melting furnace consisting of a container having at the top thereof an outside diameter approximating the inside diameter of the vaulted top closure members of the said metallurgical furnaces and' 25 an outer annular support means in a position to sustain the said closure member in closure position over the said melting furnace with the depending condenser thereof substantially immersed in a bath of molten flux contained in the melting furnace, and transfer means to remove the said top closure member from closure position on said metallurgical furnaces to closure position on said melting furnace and vice versa.
HUGH S. COOPER.
REFERENCES CITED The following references are of record in the file of this patent:
UNITED STATES PATENTS Number Name Date 1,059,307 Lance .a--- Apr. 15, 1913 1,227,240 Bie May 22, 1917 1,594,348 Bakken Aug. 3, 1926 1,980,729 Loppacker Nov. 13, 1934 2,060,070 Hansgirg Nov. 1 0. 1936 20 2,111,661 Ebner Mar. 22, 1938 2,231,023 Nelson Feb. 1l, 1941 2,238,907 McConica et al' Apr. 22, 1941 2,252,052 Van Embden Aug. 12, 1941 2,258,374 Aurati Oct. 7, 1941 2,029,921 Hansgirg Feb. 4, 1936 2,255,549 Kruh Sept. 9, 1941 2,308 586 Kemmer July 23, 1940
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US453984A Expired - Lifetime US2429668A (en) | 1942-08-07 | 1942-08-07 | Metallurgical furnace and condenser |
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US (1) | US2429668A (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2629756A (en) * | 1949-06-28 | 1953-02-24 | Revere Copper & Brass Inc | Apparatus for smelting zinciferous material comprising an electric furnace |
US2709078A (en) * | 1952-07-23 | 1955-05-24 | Nat Lead Co | Apparatus for production of refractory metals |
DE1022747B (en) * | 1956-06-08 | 1958-01-16 | Jenaer Glaswerk Schott & Gen | Cooling device for vacuum systems |
Citations (13)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US1059307A (en) * | 1913-02-26 | 1913-04-15 | Pierre Ferrere | Apparatus for the manufacture of metallic zinc. |
US1227240A (en) * | 1915-02-02 | 1917-05-22 | Busch Sulzer Bros Diesel Engine Co | Engine-cylinder. |
US1594348A (en) * | 1925-02-10 | 1926-08-03 | American Magnesium Corp | Sublimation apparatus |
US1980729A (en) * | 1929-07-26 | 1934-11-13 | Loppacker Albert | Electric furnace |
US2029921A (en) * | 1933-02-03 | 1936-02-04 | American Magnesium Metals Corp | Apparatus for producing substantially pure magnesium |
US2060070A (en) * | 1933-12-28 | 1936-11-10 | American Magnesium Metals Corp | Apparatus for producing substantially pure magnesium |
US2111661A (en) * | 1936-03-11 | 1938-03-22 | American Lurgi Corp | Process for the production of metallic magnesium |
US2231023A (en) * | 1939-02-23 | 1941-02-11 | Dow Chemical Co | Method of treating magnesium |
US2238907A (en) * | 1940-01-31 | 1941-04-22 | Dow Chemical Co | Condensation of metal vapors |
US2252052A (en) * | 1938-10-17 | 1941-08-12 | Hartford Nat Bank & Trust Co | Sublimating apparatus |
US2255549A (en) * | 1938-10-06 | 1941-09-09 | Kruh Osias | Method for producing aluminum, beryllium, chromium, magnesium, and alloys of these metals |
US2258374A (en) * | 1939-07-01 | 1941-10-07 | Amati Luigi | Process for the production of magnesium by means of thermic reduction |
US2398586A (en) * | 1944-01-01 | 1946-04-16 | H M Hobson Aircraft & Motor Co | Power control for aircraft engines |
-
1942
- 1942-08-07 US US453984A patent/US2429668A/en not_active Expired - Lifetime
Patent Citations (13)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US1059307A (en) * | 1913-02-26 | 1913-04-15 | Pierre Ferrere | Apparatus for the manufacture of metallic zinc. |
US1227240A (en) * | 1915-02-02 | 1917-05-22 | Busch Sulzer Bros Diesel Engine Co | Engine-cylinder. |
US1594348A (en) * | 1925-02-10 | 1926-08-03 | American Magnesium Corp | Sublimation apparatus |
US1980729A (en) * | 1929-07-26 | 1934-11-13 | Loppacker Albert | Electric furnace |
US2029921A (en) * | 1933-02-03 | 1936-02-04 | American Magnesium Metals Corp | Apparatus for producing substantially pure magnesium |
US2060070A (en) * | 1933-12-28 | 1936-11-10 | American Magnesium Metals Corp | Apparatus for producing substantially pure magnesium |
US2111661A (en) * | 1936-03-11 | 1938-03-22 | American Lurgi Corp | Process for the production of metallic magnesium |
US2255549A (en) * | 1938-10-06 | 1941-09-09 | Kruh Osias | Method for producing aluminum, beryllium, chromium, magnesium, and alloys of these metals |
US2252052A (en) * | 1938-10-17 | 1941-08-12 | Hartford Nat Bank & Trust Co | Sublimating apparatus |
US2231023A (en) * | 1939-02-23 | 1941-02-11 | Dow Chemical Co | Method of treating magnesium |
US2258374A (en) * | 1939-07-01 | 1941-10-07 | Amati Luigi | Process for the production of magnesium by means of thermic reduction |
US2238907A (en) * | 1940-01-31 | 1941-04-22 | Dow Chemical Co | Condensation of metal vapors |
US2398586A (en) * | 1944-01-01 | 1946-04-16 | H M Hobson Aircraft & Motor Co | Power control for aircraft engines |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2629756A (en) * | 1949-06-28 | 1953-02-24 | Revere Copper & Brass Inc | Apparatus for smelting zinciferous material comprising an electric furnace |
US2709078A (en) * | 1952-07-23 | 1955-05-24 | Nat Lead Co | Apparatus for production of refractory metals |
DE1022747B (en) * | 1956-06-08 | 1958-01-16 | Jenaer Glaswerk Schott & Gen | Cooling device for vacuum systems |
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