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US476256A - Method of and apparatus for extracting aluminium - Google Patents

Method of and apparatus for extracting aluminium Download PDF

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US476256A
US476256A US476256DA US476256A US 476256 A US476256 A US 476256A US 476256D A US476256D A US 476256DA US 476256 A US476256 A US 476256A
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aluminium
crucible
solvent
carbon
alumina
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    • CCHEMISTRY; METALLURGY
    • C25ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25CPROCESSES FOR THE ELECTROLYTIC PRODUCTION, RECOVERY OR REFINING OF METALS; APPARATUS THEREFOR
    • C25C3/00Electrolytic production, recovery or refining of metals by electrolysis of melts
    • C25C3/06Electrolytic production, recovery or refining of metals by electrolysis of melts of aluminium
    • C25C3/18Electrolytes

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  • My invention involves an improved method of and apparatus for producing aluminium.
  • the most economicalmethod of manufacturing aluminium now practiced involves the use of electricity for maintaining the salt or compound of aluminium in fusion while it is decomposed and the metal separated from the other elements of the compound.
  • My invention involves a combined chemical and electrical decomposition of the aluminium compound.
  • I preferably use a compound wound constant -potential generator of electricity of about eighty-one electrical horse-power, the generator being self-regulating and developing a current of two thousand four hundred amperes and twenty-five volts and a speed of three hundred and fifty revolutions per minute.
  • a current from this machine is caused to traverse a fused solvent in whichalumina is placed, this solvent reducing the conduct ivity and promoting the quality and quantity of aluminium produced.
  • the solvent I prefer to use is composed of fluoride of aluminium and chloride of aluminium mixed dry in.
  • Figure 1 represents aside elevation, partly in section, of such apparatus.
  • Fig. 2 is a plan view of one of the crucibles
  • Fig. 3 is a detail enlarged View of a portion of the pot or crucible where the aluminium is drawn offafter reduction.
  • Two crucibles are preferably used, (shown in the drawings at A and B and connected in series.) These crucibles are cylindrical castiron vessels having a wall I three-quarters of an inch thick and provided with a gas carbon lining K five inches thick, insulated from the iron by asbestus and bauxite paste L. (See Fig. 3.) The carbon lining constitutes the negative electrode.
  • Each crucible at or near the bottom is provided with a draw-off cock 0 of carbon mounted in the crucible and provided with an iron handle, so that melted aluminium may be readily withdrawn when occasion requires.
  • the positive electrodes are composed of a group of carbon cylinders 1D, suspended from the frame by a threaded support F, which may be raised or lowered vertically by the hand-wheel G.
  • Heavy copper bars H I are used forleading the current first to the carbon anode of the first crucible and then from the lining of the crucible to the carbon anode of the second crucible.
  • the positive electrodes or anodes are formed of cylindrical blocks of carbon and are held by screws in a cast-copper electrode-holder, so arranged that the cylinders may be given a different grouping or arrangement, so as to vary the electrical resistance of the crucible during the progress of the operation of reduction.
  • the distance from the cylinders to the wall of the crucible is greatest and the resistance at a maximum.
  • the ready-prepared and thoroughly-mixed dry solvent is introduced into the crucibles at the begin ning of the operation.
  • the chloride of aluminium adds to the fusibility of the fluoride and becomes a poor conductor.
  • the positive electrodes are adj usted into contact with the bottom of the crucible at starting and then raised so as to spring an are, which acts upon and fuses the compound solvent.
  • the apparatus might be used to decompose alumina alone without the use of the solvent if the interior resistance of the generator is as low as three thousandths of an ohm; but my experiments demonstrate that alumina becomes too good a conductor of electricity, so that its internal resistance becomes much lower than the generator and the economy of the process of reduction is lowered.
  • the resistance of the bath is continuously maintained in a good working condition.
  • the poor conductivity of the fused solvent prevents its rapid decomposition, so that only a small amount of the solvent is decomposed and but a slight addition is needed after several days work.
  • the dry solvent is introduced into the crucible by a small shovel, both crucibles being filled.
  • the resistance gradually decreasin
  • the positive electrodes are then gradually raised until the distance between the bottom of the crucibles and the bottom surface of the positive electrodes will be about the same or a little less than the distance between the electrodes and the side of the crucible. In less than ten hours fusion will be completed. Then about four pounds of calcined hot alumina is introduced into the crucibles and the process continued until the ampere-meter indicates about two amperes for each square centimeter of surface of the positive electrodes exposed to the cnrrentin the fused solvent.
  • the outer positive cylinders are then disconnected from the spider or holder and brought toward the central group, so as to arrange them together and maintain them at a maximum distance from thelining of the crucible, and in case of further increase of conductivity the positive electrode should be raised by its adjusting-screw until the distance to the bottom of the crucible is equal to the distance to the sidewall.
  • the operation should be continued as long as carbonic gas is given oit in any considerable quantity, after which a second portion of calcined alumina should be added and the same operation repeated.
  • the pure metal may be withdrawn from the draw-oft cock and run into molds and cast into bars or any form desired.
  • no deposition of carbon (black substance) or formation of the oxides of the alkalies or alkaline metals is formed, as in other electrical processes of aluminium reduction now practiced.
  • a generator of electricity combined with a cup-shaped negative electrode and a positive electrode provided with regulating devices for varying its distance from the bottom and sides of the cup-shaped cavity.

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  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Electrochemistry (AREA)
  • Materials Engineering (AREA)
  • Metallurgy (AREA)
  • Organic Chemistry (AREA)
  • Electrolytic Production Of Metals (AREA)

Description

(No Model.)
M. EMME. METHOD OF AND APPARATUS FOREXTRAGTING ALUMINIUM.
No. 476.256. Patented June 7,1892.
I: s 'I 1| 11- a I I Luz THE NORRIS V'EYERS C QYON D O NITED STATES ATET Futon.
MICHAEL EMME, OF ATLANTA, GEORGIA.
METHOD OF AND APPARATUS FOR EXTRACTING ALUMINIUM.
SPECIFICATION forming part of Letters Patent No. 476,256, dated June '7, 1892.
Application filed September 28, 1891- Serial No. 407,001- (No model.)
To all whom it may concern:
Be it known that I, MICHAEL EMME, a citizen of the United States, residing at Atlanta, in the county of Fulton and State of Georgia, have invented certain new and useful Improvementsin Methods of and Apparatus for Extracting Aluminium; and I do hereby declare the following to be a full, clear, and exact description of the invention, such as will enable others skilled in the art to which it appertains to make and use the same.
My invention involves an improved method of and apparatus for producing aluminium. The most economicalmethod of manufacturing aluminium now practiced involves the use of electricity for maintaining the salt or compound of aluminium in fusion while it is decomposed and the metal separated from the other elements of the compound.
My invention involves a combined chemical and electrical decomposition of the aluminium compound. In carrying it into practice I preferably use a compound wound constant -potential generator of electricity of about eighty-one electrical horse-power, the generator being self-regulating and developing a current of two thousand four hundred amperes and twenty-five volts and a speed of three hundred and fifty revolutions per minute. A current from this machine is caused to traverse a fused solvent in whichalumina is placed, this solvent reducing the conduct ivity and promoting the quality and quantity of aluminium produced. The solvent I prefer to use is composed of fluoride of aluminium and chloride of aluminium mixed dry in.
the proportion of ten parts of the former to one part of the latter (lOAl,F -]-Al,Ol This material is inserted between carbon electrodes and an arc sprung, which fuses it, after which alumina is introduced, when the process can be carried forward continuously.
In the accompanying drawings I have shown a form of apparatus well adapted for carrying out my process.
Figure 1 represents aside elevation, partly in section, of such apparatus. Fig. 2 is a plan view of one of the crucibles, and Fig. 3 is a detail enlarged View of a portion of the pot or crucible where the aluminium is drawn offafter reduction.
Two crucibles are preferably used, (shown in the drawings at A and B and connected in series.) These crucibles are cylindrical castiron vessels having a wall I three-quarters of an inch thick and provided with a gas carbon lining K five inches thick, insulated from the iron by asbestus and bauxite paste L. (See Fig. 3.) The carbon lining constitutes the negative electrode. Each crucible at or near the bottom is provided with a draw-off cock 0 of carbon mounted in the crucible and provided with an iron handle, so that melted aluminium may be readily withdrawn when occasion requires.
M indicates a pivotal point of support for the cook. The positive electrodes are composed of a group of carbon cylinders 1D, suspended from the frame by a threaded support F, which may be raised or lowered vertically by the hand-wheel G. Heavy copper bars H I are used forleading the current first to the carbon anode of the first crucible and then from the lining of the crucible to the carbon anode of the second crucible. The positive electrodes or anodes are formed of cylindrical blocks of carbon and are held by screws in a cast-copper electrode-holder, so arranged that the cylinders may be given a different grouping or arrangement, so as to vary the electrical resistance of the crucible during the progress of the operation of reduction. When the cylinders are all arranged centrally on the holder, the distance from the cylinders to the wall of the crucible is greatest and the resistance at a maximum. The ready-prepared and thoroughly-mixed dry solvent is introduced into the crucibles at the begin ning of the operation. The chloride of aluminium adds to the fusibility of the fluoride and becomes a poor conductor. The positive electrodes are adj usted into contact with the bottom of the crucible at starting and then raised so as to spring an are, which acts upon and fuses the compound solvent.
The apparatus might be used to decompose alumina alone without the use of the solvent if the interior resistance of the generator is as low as three thousandths of an ohm; but my experiments demonstrate that alumina becomes too good a conductor of electricity, so that its internal resistance becomes much lower than the generator and the economy of the process of reduction is lowered. By the IOC use of the solvent compound the resistance of the bath is continuously maintained in a good working condition. The poor conductivity of the fused solvent prevents its rapid decomposition, so that only a small amount of the solvent is decomposed and but a slight addition is needed after several days work. After the arc is established between the positive and negative electrodes the dry solvent is introduced into the crucible by a small shovel, both crucibles being filled. After about five hours continuance of the current fusion will be indicated by variations of an ampere-meter in the circuit, the resistance gradually decreasin The positive electrodes are then gradually raised until the distance between the bottom of the crucibles and the bottom surface of the positive electrodes will be about the same or a little less than the distance between the electrodes and the side of the crucible. In less than ten hours fusion will be completed. Then about four pounds of calcined hot alumina is introduced into the crucibles and the process continued until the ampere-meter indicates about two amperes for each square centimeter of surface of the positive electrodes exposed to the cnrrentin the fused solvent. The outer positive cylinders are then disconnected from the spider or holder and brought toward the central group, so as to arrange them together and maintain them at a maximum distance from thelining of the crucible, and in case of further increase of conductivity the positive electrode should be raised by its adjusting-screw until the distance to the bottom of the crucible is equal to the distance to the sidewall. The
alumina sinks to the bottom of the crucible, and is decomposed by a combined chemical and electrolytic means, the carbon at the high temperture developed having a very strong affinity for the oxygen and freeing the metal from the alumina. The operation should be continued as long as carbonic gas is given oit in any considerable quantity, after which a second portion of calcined alumina should be added and the same operation repeated. The pure metal may be withdrawn from the draw-oft cock and run into molds and cast into bars or any form desired. When reduced in accordance with the process herein described, no deposition of carbon (black substance) or formation of the oxides of the alkalies or alkaline metals is formed, as in other electrical processes of aluminium reduction now practiced.
Having thus described my invention, what I claim as new, and desire to secure by Letters Patent, is
1. The process of extracting aluminium from its oxides, consisting in leading a decomposing eleetric current through a fused mass of fluoride and chloride of aluminium to which free alumina has been added.
2. The process for the reduction of aluminium, consisting of fusing electrically a solvent composed of fluoride and chloride of aluminium in proportions specified, introducinginto this solvent hot calcined alumina and maintaining uniform the resistance of the fused mass during decomposition.
3. As an apparatus for reducing metals from their ores, a generator of electricity combined with a cup-shaped negative electrode and a positive electrode provided with regulating devices for varying its distance from the bottom and sides of the cup-shaped cavity.
In testimony whereof I aflix my signature in presence of two witnesses.
MICHAEL EMME.
Vitnesses:
FRANK E. ELLIs, N. R. FOWLER.
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