US984503A - Producing calcium. - Google Patents

Producing calcium. Download PDF

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Publication number
US984503A
US984503A US51340609A US1909513406A US984503A US 984503 A US984503 A US 984503A US 51340609 A US51340609 A US 51340609A US 1909513406 A US1909513406 A US 1909513406A US 984503 A US984503 A US 984503A
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Prior art keywords
calcium
furnace
graphite
producing calcium
carbid
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US51340609A
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William C Arsem
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General Electric Co
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General Electric Co
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    • CCHEMISTRY; METALLURGY
    • C22METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
    • C22BPRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
    • C22B26/00Obtaining alkali, alkaline earth metals or magnesium
    • C22B26/20Obtaining alkaline earth metals or magnesium

Definitions

  • WITNESSES %/KM 26% f4 r STATES PATENT orrion.
  • My present invention comprises the production or recovery of metallic calcium by direct decomposition of calcium carbid in 'a suitable furnace in which the gaseous pres sure is materially less than one atmosphere.
  • suitable for carrying out this operation has an air-tight envelop in which a good vacu um can be produced and maintained and has a hot zone in which the calcium carbid can be heated and decomposed and from which thevaporized calcium can, be conducted to a cooling zone for condensation and recovery as substantially pure metal.
  • Figure 1 is a sectional elevation of the furnace with the crucible removed from the heating chamber so that the heating elements may be clearly seen;
  • Fig. 2 is a sectional plan of-the same; and
  • Fig. 3 is an end elevation with certain parts cut away.
  • the main envelop of the furnace consists metal with a coating of tin, provided with a cover 2 bolted securely in place.
  • the cover 2 has mau -holes 3 and 4 located respectively above the cold and hot zones of the furnace.
  • Lead gaskets 5 can'be used under the covers to make'air-tight joints.
  • the heating element of the furnace consists of four graphite grids 6, 7, 8. and 9 sawed transversely and with their corners rounded off, as shown in the drawing, so that when current is passed through them they will'attain a. uniform incandescence throughout substantially their entire length. Current is supplied tothese graphite resistance elements by way of water cooled copper tubes 10 and 11 passing through insulating -.bushings in the end of envelop 1.
  • the above described heating elemeng consisti'ng of the four grids 6, 7-, 8 an 9 is inclosed in a rectangular heat insulating screen, the graphite walls of which are made double throughout with an intervening packing of graphite powder.
  • the bottom member 19 of the screen rests. on insulating buttons 20 of lava and supports the end walls 21 and 22 and also the side walls 23 and 24.
  • the top member 25 rests on the tops of the four side walls.
  • This heat insulating screen serves to limit the radiation of heat outward and serves to reflect and concentrate the heat on the rectangular space inclosed by the heater grids.
  • a rectangularcrucible 26 of graphite containing the charge of calcium carbid' geously consist of an earthenware pot of suffici ent size to insure complete condensation of the calcium distilling over from the hot zone of the furnace.
  • the condensing chamber may be provided witha cover 32 preferably having an outlet 33 for the ready removal of air when the entire furnace is pumped out by way of pipe 3 1 which leads to a vacuum pump.
  • the material under treatment of carbon can be obtained and constantly maintained for any length of time at a pressure of a fraction" of. a millimeter of rrfleroes not come in contact with the heating elements and chemical action therebetween is avoided.
  • the main envelop of the furnace is' maintained cool by the circulation of water below and on all sides up to a level I just below the man-hole covers 3 and 4. These are preferably leftu nsubmerged for the more ready introduction and removal of the calcium carbid and its decomposition products. In charging and discharging the furnace it is only necessary. to remove the covers 3 and 4, whereupon after removal of the upper screen 25, the crucible 26 can be filled with a newcharge and the condens-,.
  • the method which consists in decomcalcium carbid to a temperature in the neighborhood of 1500 C. while under a pressureless than atmospheric, conductin away the resultant calcium vapor, and col ecting and condensing said vapor.

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  • 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

W. O. ARSEM. PRODUCING CALCIUM. APPLICATION FILED AUG. 18, 1909.
Patented Feb. 14, 1911.
Ill/I111];
II VI INVENTEIFL:
EEM
ATTX
WITNESSES: %/KM 26% f4 r STATES PATENT orrion.
WILLIAM G. ARSEM,
OF SCHENECTADY, NEW YORK, ASSIGNOR TO GENERAL ELECTRIC COMPANY, CORPORATION OF NEW YORK.
PRODUCING CALCIUM.
Specification of Letters .Patent.
Patented Feb. 14, 1911.
Application filed August 18, 1909. Serial No. 513,406.
To all whom it may concern:
Be it known that 1, WILLIAM C. ARsEM, a citizen of the United States, residing at Schenectady, county of Schenectady, State of New York, have invented certain new and useful Improvements in Producing Calcium, of which the following is a specification.
My present invention comprises the production or recovery of metallic calcium by direct decomposition of calcium carbid in 'a suitable furnace in which the gaseous pres sure is materially less than one atmosphere.
I The electric furnace devised by me and of a rectangular box 1, preferably of. gun
suitable for carrying out this operation, has an air-tight envelop in which a good vacu um can be produced and maintained and has a hot zone in which the calcium carbid can be heated and decomposed and from which thevaporized calcium can, be conducted to a cooling zone for condensation and recovery as substantially pure metal.
In order that my improved process may .be available to those skilled .in the art, I deem it advisable to describe in detail the furnace in which it can be carried out.
In the accompanying drawing, Figure 1 .is a sectional elevation of the furnace with the crucible removed from the heating chamber so that the heating elements may be clearly seen; Fig. 2 is a sectional plan of-the same; and Fig. 3 is an end elevation with certain parts cut away.
The main envelop of the furnace consists metal with a coating of tin, provided with a cover 2 bolted securely in place. The cover 2 has mau -holes 3 and 4 located respectively above the cold and hot zones of the furnace. Lead gaskets 5 can'be used under the covers to make'air-tight joints. The heating element of the furnace consists of four graphite grids 6, 7, 8. and 9 sawed transversely and with their corners rounded off, as shown in the drawing, so that when current is passed through them they will'attain a. uniform incandescence throughout substantially their entire length. Current is supplied tothese graphite resistance elements by way of water cooled copper tubes 10 and 11 passing through insulating -.bushings in the end of envelop 1. The tubes-rare. clamped, respectively, in copper blocks. 12 and 13, which in turn are bolted to the graphite grids 6 and 9. The other ends of these' grids may contact respectively with the graphite blocks 14.- and 15 which make electrical connection with the lower pair of grids. A cross connection 16 of graphite at the extreme end of the furnace completes the electrical circuit.
For the sake of avoiding .confusion on the drawing, the current supply cables for the tubes 10 and 11 have been omitted but the rubber hose for conducting water to these terminals for cooling purposes is shown at 17 and 18.. O
The above described heating elemeng consisti'ng of the four grids 6, 7-, 8 an 9 is inclosed in a rectangular heat insulating screen, the graphite walls of which are made double throughout with an intervening packing of graphite powder. The bottom member 19 of the screen rests. on insulating buttons 20 of lava and supports the end walls 21 and 22 and also the side walls 23 and 24. The top member 25 rests on the tops of the four side walls. This heat insulating screen serves to limit the radiation of heat outward and serves to reflect and concentrate the heat on the rectangular space inclosed by the heater grids. Within this space may be introduced a rectangularcrucible 26 of graphite containing the charge of calcium carbid' geously consist of an earthenware pot of suffici ent size to insure complete condensation of the calcium distilling over from the hot zone of the furnace. The condensing chamber may be provided witha cover 32 preferably having an outlet 33 for the ready removal of air when the entire furnace is pumped out by way of pipe 3 1 which leads to a vacuum pump.
Inasmuch as the direct decomposition of calcium carbid into calcium and carbon does not result in the liberation or production of any great quantity of gaseous material, the continuous maintenance of a substantial vacuum in the furnace is easily possible even at the high temperature at which the operation must b,e carried out. By working in a vacuum, 'the temperature of decomposition is much reduced and the calcium comes off in pure and unoxidized condition. Theoperating temperature varies somewhat with the degree of vacuum and seems to be in the neighborhood of 15002000, the calcium distilling off at this temperature and leaving behind a pseudomorph of soft unctuous graphite. Alternating current may advantageously be used in the heater grids, and
If any temperature up to the vaporizing point cury. The material under treatment of carbon can be obtained and constantly maintained for any length of time at a pressure of a fraction" of. a millimeter of rrfleroes not come in contact with the heating elements and chemical action therebetween is avoided. The main envelop of the furnace .is' maintained cool by the circulation of water below and on all sides up to a level I just below the man-hole covers 3 and 4. These are preferably leftu nsubmerged for the more ready introduction and removal of the calcium carbid and its decomposition products. In charging and discharging the furnace it is only necessary. to remove the covers 3 and 4, whereupon after removal of the upper screen 25, the crucible 26 can be filled with a newcharge and the condens-,.
ing chamber 31 relieved of the condensed material and even lifted bodily out and replaced by another similar earthen pot.
What I claim as new and desire to secure by Letters Patent of the United States is:
1. The method of producing calcium, which consists in decomposing calcium carbid at less, than atmospheric pressure, and condensing the resultant calcium vapors.
2. The method which consists in decomcalcium carbid to a temperature in the neighborhood of 1500 C. while under a pressureless than atmospheric, conductin away the resultant calcium vapor, and col ecting and condensing said vapor.
calcium carbid in a substantial vacuum to a temperature at which it decomposes, conducting "away the resultant calcium vapor, and collecting and cooling said vapor In witness whereof, I have hereunto set my hand this 17th day of Au st, 1909.
WILLIAM ARSEM. Witnesses:
BENJAMIN B; HULL,
MARGARET E. WOOLLEY.
4. The method which consists in heating '5. The method which consists in heating posing calcium carbid by heating in a
US51340609A 1909-08-18 1909-08-18 Producing calcium. Expired - Lifetime US984503A (en)

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Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2839380A (en) * 1955-06-13 1958-06-17 Air Reduction Production of calcium metal
US2931719A (en) * 1956-09-28 1960-04-05 Pechiney Prod Chimiques Sa Process and apparatus for the production of metals by dissociation of their carbides
DE1191112B (en) * 1962-02-28 1965-04-15 Vaw Ver Aluminium Werke Ag Process and device for the thermal extraction of magnesium

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2839380A (en) * 1955-06-13 1958-06-17 Air Reduction Production of calcium metal
US2931719A (en) * 1956-09-28 1960-04-05 Pechiney Prod Chimiques Sa Process and apparatus for the production of metals by dissociation of their carbides
DE1191112B (en) * 1962-02-28 1965-04-15 Vaw Ver Aluminium Werke Ag Process and device for the thermal extraction of magnesium

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