US1384499A - Method of and apparatus for refining metals - Google Patents
Method of and apparatus for refining metals Download PDFInfo
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- US1384499A US1384499A US379447A US37944720A US1384499A US 1384499 A US1384499 A US 1384499A US 379447 A US379447 A US 379447A US 37944720 A US37944720 A US 37944720A US 1384499 A US1384499 A US 1384499A
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- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25C—PROCESSES FOR THE ELECTROLYTIC PRODUCTION, RECOVERY OR REFINING OF METALS; APPARATUS THEREFOR
- C25C7/00—Constructional parts, or assemblies thereof, of cells; Servicing or operating of cells
- C25C7/005—Constructional parts, or assemblies thereof, of cells; Servicing or operating of cells of cells for the electrolysis of melts
Definitions
- My invention aims to rovide a method of, and apparatus for, re ning meta-ls electrolytically and aims more particularly to provide means whereby impurities may readily be separated from electrolytically deposited metal by confining such impurities within a suitable container with which the refined metal does not communicate.
- my invention in one of its forms, may embody a plurality of communicating com artments which contain a suitable electro yte and each of whichis adapted to be served by suitable current conducting means, said compartments being partially separated from one another in such a manner as to prevent the impurities in one or more of them from contaminating the refined metal in other of the compartments.
- FIG. 3 a sectional view taken on the line 33 of Fig. 2; and 4 In Fig. 4, a sectional view corresponding to Fig. 2 of a modified form of my apparatus.
- This apparatus may take the form diagrammatically illustrated in the drawings, in which 1 is acompartment or cell to which current is conducted in any suitable manner, as by anodes 2, and in which 3 is a cell served by corres onding cathodes 4. It will be understood t at the cells 1 and 3 may take any suitable and convenient shape and that the arrangement and number of the anodes may be varied in accordance with the circumstances, and the results desired.
- the compartments 1 and 3 are separated by a partition 5 which is lower than the side walls of the compartments, such partition bein suflicientlyhigh to prevent the interming ing of the'metallic contents of the two cells, but low enough to permit the electrolyte 6 to form a means of communication between the two.
- the entire arrangement may be covered with a suitable covering 7 of firebrick orother suitable material, in which an aperture 8 may be provided for the admission of the metal to be refined.
- A, suit-- compartments are preferably made of sheet iron, the electrodes being insulated therefrom by suitable insulating bushings 10 and means for water cooling, such as the water jacket 11, are provided.
- the waterjacket is provided with suitable liquid intake and outlet ports 12.
- the electrolyte may be caused to congeal, thus forming a coating 13 over the sides and bottom of the compartments, 1 and 3, which coating is an insulator,"and thus prevents .the short-circuiting of thecircuit feeding the apparatus and also prevents contact between the fused metal and the metallic surfaces comprising the walls and bottom of the container.
- the apparatus may consist of a pair of metal containers separated by a layer 14 of suitable insulating material, such as mica or other highly refractory substance and each of the containers is lined on its bottom and a portion of its sides with a conducting substance 15, such as carbon, adapted to conduct current from the electrodes 2 and 4 to the molten metal therein contained.
- a conducting substance 15, such as carbon adapted to conduct current from the electrodes 2 and 4 to the molten metal therein contained.
- the molten metal completely covers this carbon lining during the normal working of the process and water cooling means, as at 16, is provided to cool the upper portion of the partition so that a layer of congealed electrolyte covers it as well as the sides of the container above the molten bath, as at 17, so that the fused electrolyte is prevented from coming into contact with the metallic walls or partition of the container.
- I may use a bath composed of suitable proportions of the fluorids of aluminium and sodium to which may be added aluminium oxid insuch proportions as have been found suitable for the ordinary reduction of aluminium by electrolysis or in other proportions as may be found to give good results. It will be understood that the electrolyte is not removed from .the apparatus but is used con- -tinuously and that due to the electrolysis,
- the charge of the apparatus as initially tus will causejthe unrefined metal to go into solution at the anode and be deposisted as pure metal by electrolysis at the cathode 4. It will be noted that because of the arrangement of the divided compartments, the refined metal cannot mingle with the impure metal contained in the compartment 1.
- the process may be modified in a number of ways; for instance, the initial charge may be added in molten form in order to avoid the necessity of starting as described above, and may be operated continuously by the addition through orifice 8 of unrefined metal either in solid or molten form, and by drawing off the refined metal at the orifice 9 at suitable intervals. .1
- a device for refining impure metal comprising a container for the unrefined metal, a container for the refined metal,
- a device for refining impure metal comprising a container for the unrefined metal, a container for the refined metal, means for permitting communication between said containers through an electrolyte and for preventingcommunication between the metals in said containers and means for container for refined metal adjacent thereto,
- a partition partially separatin said containers and an electrolyte from Wll0h refined metal is adapted to be deposited in one of said containers, within which said partition is submerged.
- the method of refining impure metals which comprises confining the impure metal in one of a plurality of partially separated containers containing an electrolyte, subjecting the electrolyte-to electrolysis and depositing the refined metal in another of said partially separated containers.
- the method of refining a metal which comprises confining the unrefined metal to one of a plurality of partially separated containers containing an electrolyte, subjecting the electrolyte and unrefined metal to electrolysis to cause the fusing of the electrolyte and the deposition therefrom of refined metal in another of said containers and preventing intermingling of the metallic contents of said containers.
- anode and cathode compartments in a device for refining metals by electrolysis, anode and cathode compartments, and a partition separating said compartments and of such height as to permit partial communication between said compartments through an electrolyte but preventing impure metal in the anode compartment from coming into contact with refined metal in the cathode compartment.
- anode and cathode compartments in a device for refining metals by electrolysis, anode and cathode compartments, and means separating said compartments and of such dimensions as to permit partial communication between said compartments through an electrolyte but preventing impure metal in the anode compartment from coming into contact with refined metal in the cathode compartment.
- an .anode chamber for impure metal and a cathode chamber said chambers being in partial communication with each other.
Description
S. A. TUCKER.
METHOD OF AND APPARATUS FOR REFINING METALS.
APPLICATION F LED MAY 7. 1920.
Patented July 12, 1921.
UNITED STATES PATENT OFFICE.
SAMUEL A. TUCKER, 01 NEW YORK, N. Y.
METHOD OF AND AIPARATUS FOR BEFINING METALS.
1,384,499. Application filed m 7,
To all whom it may concern Be it known that I, SAMUEL A. TUCKER, a citizen of the United States, and a resident of the borough of Manhattan, city, county, and State ofNew York, have invented-an Improvement in Methods of and Apparatus for Refinin Metals, of which the following is a speci cation.
My invention aims to rovide a method of, and apparatus for, re ning meta-ls electrolytically and aims more particularly to provide means whereby impurities may readily be separated from electrolytically deposited metal by confining such impurities within a suitable container with which the refined metal does not communicate.
While my invention may be used in connection with the refining of various metals,
. it has particular utility in connection with the refining of metals which are usually deposited from a fused bath, such as aluminium, magnesium, calcium, sodium, or similar metals. In connection with the refining of such metals, my invention, in one of its forms, may embody a plurality of communicating com artments which contain a suitable electro yte and each of whichis adapted to be served by suitable current conducting means, said compartments being partially separated from one another in such a manner as to prevent the impurities in one or more of them from contaminating the refined metal in other of the compartments. It will be understood, however, as pointed out above, that although m mvention is particularly applicable to t e refining of aluminium or similar metals,.it may be a plied to the refining of many other meta s, and it will also be understood that the particular apparatus which I shall describe hereafter as being forms of my apparatus which I prefer may be greatly modified and that I therefore do not wish to limit myself to any of the particular details of the apparatus or process.
In the drawings, I have shown:
In Figure 1, a lan view of one form of apparatus suitab e for carrying out the process'of my invention;
In Fi 2, a .sectional view thereof taken on the line 2--2 of Fig. 1;
In Fig. 3, a sectional view taken on the line 33 of Fig. 2; and 4 In Fig. 4, a sectional view corresponding to Fig. 2 of a modified form of my apparatus.
Specification of Letters Patent.
Patented July 12, 1921.
1920. Serial no. swam.
In the process for the reduction of aluanodes of carbon. The operation of this device results in aluminium in the molten state being deposited within the cathode container, whence it is drawn off by suit.- able means. This reduction operation necessarily results inmixing with the reduced aluminium a considerable quantity of impurities from the electrolyte, some of which are as heavy or heavier than the aluminium and consequently drop into the molten mass, Whereas others of such impurities are carried down into the molten mass by the aluinimum in its separation from the electroyte.
In one form of the apparatus of my invention, I have provided one container in which the impure metal to be refined is placed and a second container in which the refined metal is deposited, there-being no direct communication between these containers, the onl communication being through the body 0 the electrolyte itself.
This apparatus may take the form diagrammatically illustrated in the drawings, in which 1 is acompartment or cell to which current is conducted in any suitable manner, as by anodes 2, and in which 3 is a cell served by corres onding cathodes 4. It will be understood t at the cells 1 and 3 may take any suitable and convenient shape and that the arrangement and number of the anodes may be varied in accordance with the circumstances, and the results desired.
The compartments 1 and 3 are separated by a partition 5 which is lower than the side walls of the compartments, such partition bein suflicientlyhigh to prevent the interming ing of the'metallic contents of the two cells, but low enough to permit the electrolyte 6 to form a means of communication between the two.
If desired the entire arrangement may be covered with a suitable covering 7 of firebrick orother suitable material, in which an aperture 8 may be provided for the admission of the metal to be refined. A, suit-- compartments are preferably made of sheet iron, the electrodes being insulated therefrom by suitable insulating bushings 10 and means for water cooling, such as the water jacket 11, are provided. The waterjacket is provided with suitable liquid intake and outlet ports 12. By properly adjusting the temperature of the cooling water and by selecting a suitable electrolyte, the electrolyte may be caused to congeal, thus forming a coating 13 over the sides and bottom of the compartments, 1 and 3, which coating is an insulator,"and thus prevents .the short-circuiting of thecircuit feeding the apparatus and also prevents contact between the fused metal and the metallic surfaces comprising the walls and bottom of the container.
In the modification shown in Fig. 4, the apparatus may consist of a pair of metal containers separated by a layer 14 of suitable insulating material, such as mica or other highly refractory substance and each of the containers is lined on its bottom and a portion of its sides with a conducting substance 15, such as carbon, adapted to conduct current from the electrodes 2 and 4 to the molten metal therein contained. The molten metal, however, completely covers this carbon lining during the normal working of the process and water cooling means, as at 16, is provided to cool the upper portion of the partition so that a layer of congealed electrolyte covers it as well as the sides of the container above the molten bath, as at 17, so that the fused electrolyte is prevented from coming into contact with the metallic walls or partition of the container. By this arrangement the fused electrolyte comes into contact only with molten surfaces of the pure and impure metal situated in their respective compartments and at the same time the carbon lining effectually prevents any contactv between the metallic surfaces of the. con= tainer and the molten metal. This arrangement makes it possible to employ less of the cooling water than is the case in the modification of the apparatus first described. In
using the apparatus described above in connection with the refining of aluminium, I may use a bath composed of suitable proportions of the fluorids of aluminium and sodium to which may be added aluminium oxid insuch proportions as have been found suitable for the ordinary reduction of aluminium by electrolysis or in other proportions as may be found to give good results. It will be understood that the electrolyte is not removed from .the apparatus but is used con- -tinuously and that due to the electrolysis,
the greater part of the impurities are eliminated and appear in the first runs of cathode metal and that thereafter the possibility of contamination of the reduced metal is greatly minimized.
The charge of the apparatus as initially tus will causejthe unrefined metal to go into solution at the anode and be deposisted as pure metal by electrolysis at the cathode 4. It will be noted that because of the arrangement of the divided compartments, the refined metal cannot mingle with the impure metal contained in the compartment 1.
The process may be modified in a number of ways; for instance, the initial charge may be added in molten form in order to avoid the necessity of starting as described above, and may be operated continuously by the addition through orifice 8 of unrefined metal either in solid or molten form, and by drawing off the refined metal at the orifice 9 at suitable intervals. .1
What I claim is:
1. A device for refining impure metal, comprising a container for the unrefined metal, a container for the refined metal,
means for permitting communication between said containers through an electrolyte and for preventing communication between the metals in said containers.
2. A device for refining impure metal, comprising a container for the unrefined metal, a container for the refined metal, means for permitting communication between said containers through an electrolyte and for preventingcommunication between the metals in said containers and means for container for refined metal adjacent thereto,
a partition partially separatin said containers and an electrolyte from Wll0h refined metal is adapted to be deposited in one of said containers, within which said partition is submerged. Y
5. In an apparatus for refining impure metals, a container for unrefined metal, a
communicating container for refined metal,
an electrolyte in said containers, a partition between said containers extending to above the level of the metal in the containers and to below the upper level of the electrolyte therein and means for causing an electrolysis of the electrolyte.
6. The method of refining impure metals which comprises confining the impure metal in one of a plurality of partially separated containers containing an electrolyte, subjecting the electrolyte-to electrolysis and depositing the refined metal in another of said partially separated containers.
7. The method of refining a metal which comprises confining the unrefined metal to one of a plurality of partially separated containers containing an electrolyte, subjecting the electrolyte and unrefined metal to electrolysis to cause the fusing of the electrolyte and the deposition therefrom of refined metal in another of said containers and preventing intermingling of the metallic contents of said containers.
8. The method of refining aluminium which com rises charging one of a plurality of partial y separated compartments with aluminium oxid, charging said compartment and an adjacent compartment partially separated therefrom with a common electrolyte comprising fluorids and subjecting, said charges to electrolysis to deposit metallic aluminium in the second of said compartments.
9. In a device for refining metals by electrolysis, anode and cathode compartments, and a partition separating said compartments and of such height as to permit partial communication between said compartments through an electrolyte but preventing impure metal in the anode compartment from coming into contact with refined metal in the cathode compartment.
10. In a device for refining metals by electrolysis, anode and cathode compartments, and means separating said compartments and of such dimensions as to permit partial communication between said compartments through an electrolyte but preventing impure metal in the anode compartment from coming into contact with refined metal in the cathode compartment.
11. In a device for refining metals by electrolysis, an .anode chamber for impure metal and a cathode chamber, said chambers being in partial communication with each other.
through an electrolyte while maintaining the impure and refined metals out of contact with each other. p 12. 'The method of refining metals by electrolysis which comprises the ste of electrolyzing a charge of impure meta serving as an anode in an anode chamber and depositing the pure metal in a communicating cathode chamber from a superposed electrolyte. In testimony whereo I have signed my name to this specification this 6th day of May, 1920.
SAMUEL A. TUCKER.
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US379447A US1384499A (en) | 1920-05-07 | 1920-05-07 | Method of and apparatus for refining metals |
Applications Claiming Priority (1)
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US379447A US1384499A (en) | 1920-05-07 | 1920-05-07 | Method of and apparatus for refining metals |
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US1384499A true US1384499A (en) | 1921-07-12 |
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Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2451490A (en) * | 1944-08-04 | 1948-10-19 | Reynolds Metals Company Inc | Production of aluminum |
US2451491A (en) * | 1945-01-30 | 1948-10-19 | Reynolds Metals Co | Enriching the alumina content of recirculated cryolite fusions in aluminum production |
DE1110881B (en) * | 1956-07-13 | 1961-07-13 | Pechiney Prod Chimiques Sa | Power supply to the anode layer for aluminum refining according to the three-layer process |
US4118292A (en) * | 1976-06-09 | 1978-10-03 | National Research Development Corporation | Packed bed electrorefining and electrolysis |
-
1920
- 1920-05-07 US US379447A patent/US1384499A/en not_active Expired - Lifetime
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2451490A (en) * | 1944-08-04 | 1948-10-19 | Reynolds Metals Company Inc | Production of aluminum |
US2451491A (en) * | 1945-01-30 | 1948-10-19 | Reynolds Metals Co | Enriching the alumina content of recirculated cryolite fusions in aluminum production |
DE1110881B (en) * | 1956-07-13 | 1961-07-13 | Pechiney Prod Chimiques Sa | Power supply to the anode layer for aluminum refining according to the three-layer process |
US4118292A (en) * | 1976-06-09 | 1978-10-03 | National Research Development Corporation | Packed bed electrorefining and electrolysis |
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