US978211A - Art of extracting metals electrolytically. - Google Patents
Art of extracting metals electrolytically. Download PDFInfo
- Publication number
- US978211A US978211A US55948510A US1910559485A US978211A US 978211 A US978211 A US 978211A US 55948510 A US55948510 A US 55948510A US 1910559485 A US1910559485 A US 1910559485A US 978211 A US978211 A US 978211A
- Authority
- US
- United States
- Prior art keywords
- art
- electrolyte
- cathode
- extracting
- gold
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Lifetime
Links
- 229910052751 metal Inorganic materials 0.000 title description 13
- 239000002184 metal Substances 0.000 title description 13
- 150000002739 metals Chemical class 0.000 title description 8
- 238000000034 method Methods 0.000 description 16
- 239000003792 electrolyte Substances 0.000 description 14
- PCHJSUWPFVWCPO-UHFFFAOYSA-N gold Chemical compound [Au] PCHJSUWPFVWCPO-UHFFFAOYSA-N 0.000 description 12
- 239000010931 gold Substances 0.000 description 12
- 229910052737 gold Inorganic materials 0.000 description 12
- 239000000725 suspension Substances 0.000 description 5
- 239000004020 conductor Substances 0.000 description 4
- 238000000151 deposition Methods 0.000 description 4
- 230000000694 effects Effects 0.000 description 4
- 230000008021 deposition Effects 0.000 description 3
- 239000000463 material Substances 0.000 description 3
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 2
- 238000013019 agitation Methods 0.000 description 2
- 239000007788 liquid Substances 0.000 description 2
- 239000010970 precious metal Substances 0.000 description 2
- ZLMJMSJWJFRBEC-UHFFFAOYSA-N Potassium Chemical compound [K] ZLMJMSJWJFRBEC-UHFFFAOYSA-N 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 229910052802 copper Inorganic materials 0.000 description 1
- 239000010949 copper Substances 0.000 description 1
- 239000011889 copper foil Substances 0.000 description 1
- 230000001419 dependent effect Effects 0.000 description 1
- 230000005611 electricity Effects 0.000 description 1
- 238000005868 electrolysis reaction Methods 0.000 description 1
- 238000000605 extraction Methods 0.000 description 1
- 230000004927 fusion Effects 0.000 description 1
- 229910021385 hard carbon Inorganic materials 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 229910052700 potassium Inorganic materials 0.000 description 1
- 239000011591 potassium Substances 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 230000000284 resting effect Effects 0.000 description 1
- 150000003839 salts Chemical class 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
Images
Classifications
-
- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25B—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES FOR THE PRODUCTION OF COMPOUNDS OR NON-METALS; APPARATUS THEREFOR
- C25B15/00—Operating or servicing cells
Definitions
- My invention is directed particularly to a novel method of extracting gold and other precious metals from their ores after theyhave been reduced to a very minute or finely powdered state, and it has for its objects, first, to provide a method of effecting this result in as simple, efiicient and inexpensive a manner as possible; second, to devise a method of extracting gold when found in other than a metallic state (chlorids, for instance) by the agency of electrolysis andin su'ch manner that the gold is deposited on the cathode -of the apparatus used in practicing said method.
- 1 represents a water-tight vat or separating: chamber and 2 a rod, preferably of copper or other good conducting material, resting upon the opposite ends thereof.
- 5 is the dynamo electric machine or equivalent source of electrical energy and 6, 6, conductors running therefrom to the anode and cathode respectively, as shown.
- 7 is a pipe or tube adapted to beconnected to a source of heated vapor or gas, as steam or air, and 8, 8, are hral'iches thereof extend- I ing downward to points within the vat and beneath the cathode 3 and turned laterally in the plane of the anode and cathode at their lower ends as shown.
- the electrolyte which is illustrated in the drawing as submerging the anode and cathode when used in the process of extracting gold may be cyanid of potassium or of any other such equivalent materials as are used in the art of electrolytic methods of extracting valuable metals and the anode and catl1- ode may be located in the bodyof the electrolyte in any preferred manner, or may be of any preferred material and construction or shape, such matters coming well within the skill of those versed in the electrolytic art generally, the essential feature being that they shall be so located as to readily remove the cathode for the purpose of extracting the gold therefrom by fusion in the usual way.
- the cathode is illustrated in the drawing as being suspended from the conducting rod 2 by good conducting metallic hooks 9, 9.
- the ore to be treated is first pulverized or round to a fine powder and gradually fed lnto the electrolyte which is kept in an agitated condition or circulation by steam, hot air or gas issuing from the source of supply, not shown, throu 'h the pipes T and 8.
- a relatively la r an amount of the powdered ore will remain in suspension while the liquid is in motion when it is placed in the vat and is simultanenu'sly subjected to the action of electricity, motlbn and heat until the major part of the metal is deposited on the cathode 3
- the electrolyte should be heated to temperatures varying from 150 to 212 l inasmuch as such heating controls the liberation of the gold resolvent, and these temperatures will differ for different ores.
- the liberation of the gold resolvent is controlled in such a way that there is no sensible loss of the resolvent, and in the implication of heat simultaneously with )I'OPLI' agitation and by sinmltaneously subjecting the electrolyte to electrical currents I am enabled to obtain the best possible results in the separation of gold and other precious metals from electrolytes as thus treated.
- the microscopic particles of the gold in the ore are dissolved in the electrolyte during the process and reduced by a. deposition on the cathode. After the process has been continued for several hours, depending upon the nature of the electrolyte and the quality of the ore to be operated upon, it is discontinued and the electrolyte in a quiet or undisturbed condition is allowed to settle, so that all of the solid matter held in suspension falls to the bottom and the liquid ma y be siphoned oil into anothervat, when the electrodes and steam pipes may be lifted out, leaving said vat in condition for the next batch of material to be treated.
- the electrode upon which the gold is deposited is then subjected to suflicient heat to fuse it and'the gold is separated therefrom in the usual manner.
- a method of extracting metals which consists in simultaneously subjecting the powdered ore thereof while in suspension in an electrolyte to the agitating effect of a heated vapor orgas and 111 simultaneously effecting the deposition of the metal upon a fusible electrode.
- a method of extracting metals which consists in simultaneously subjecting the pmvdered'ore thereof while in suspension in an electrolyte to the agitating effect of a heated vapor or gas and in simultaneously effecting the deposition of the metal upon an velectrode capable of being disintegrated by heat.
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Electrochemistry (AREA)
- Materials Engineering (AREA)
- Metallurgy (AREA)
- Organic Chemistry (AREA)
- Manufacture And Refinement Of Metals (AREA)
- Electrolytic Production Of Metals (AREA)
Description
J. H. ROBERTSON.
ART OF BXTRACTING METALS ELBOTBOLYTIOALLY. APPLI A'I IoR I'I-LED mm: 20, 190B. nnnnwnn MAY 5, 1910.
978,211. Patented Dec. 13, 1910.
mzjllnlll I, 1 111,! I 1 4 1 I 1 1 13,1 lite nae? I "GAMES HART ROBERTSON, E NEW'YORK, N. Y.
ART OF EXTRACTING METALS ELECTROLYTICALLY.
Specification of Letters Patent.
Patented Dec. 13, 1910.
Application filed June 20, 1908, Serial No. 439,562. Renewed May 5, 1910. Serial No. 559,485.
v To all whom it may concern:
Be it known that I, JAMES HART ROBERT- SON, a citizen of the United States, and resident ofNew York, borough of Manhattan, county and State of New York, have made a new and useful Invention in the Art of Extracting Metals Electrolytically, of which the following is a specification.
My invention is directed particularly to a novel method of extracting gold and other precious metals from their ores after theyhave been reduced to a very minute or finely powdered state, and it has for its objects, first, to provide a method of effecting this result in as simple, efiicient and inexpensive a manner as possible; second, to devise a method of extracting gold when found in other than a metallic state (chlorids, for instance) by the agency of electrolysis andin su'ch manner that the gold is deposited on the cathode -of the apparatus used in practicing said method.
.My invention will be fully understood by referring to the accompanying drawing which is a sectional perspective and part diagrammatic view of an apparatus designed to practice the method hereinafter described and claimed.
1 represents a water-tight vat or separating: chamber and 2 a rod, preferably of copper or other good conducting material, resting upon the opposite ends thereof.
3 is a metallic cathode of some light sheet metal, such as copper foil, and preferably corrugated so as to give it increased conducting capacity and depositing surface, said cathode being suspcmled directly from the rod 2 by two or more conductors, as shown.
4 is the anode of sheet or block form made preferably of some good conducting material, not readily disintegrated by an electrical current, as hard carbon.
5 is the dynamo electric machine or equivalent source of electrical energy and 6, 6, conductors running therefrom to the anode and cathode respectively, as shown.
7 is a pipe or tube adapted to beconnected to a source of heated vapor or gas, as steam or air, and 8, 8, are hral'iches thereof extend- I ing downward to points within the vat and beneath the cathode 3 and turned laterally in the plane of the anode and cathode at their lower ends as shown.
' The electrolyte which is illustrated in the drawing as submerging the anode and cathode when used in the process of extracting gold may be cyanid of potassium or of any other such equivalent materials as are used in the art of electrolytic methods of extracting valuable metals and the anode and catl1- ode may be located in the bodyof the electrolyte in any preferred manner, or may be of any preferred material and construction or shape, such matters coming well within the skill of those versed in the electrolytic art generally, the essential feature being that they shall be so located as to readily remove the cathode for the purpose of extracting the gold therefrom by fusion in the usual way. The cathode is illustrated in the drawing as being suspended from the conducting rod 2 by good conducting metallic hooks 9, 9.
The ore to be treated is first pulverized or round to a fine powder and gradually fed lnto the electrolyte which is kept in an agitated condition or circulation by steam, hot air or gas issuing from the source of supply, not shown, throu 'h the pipes T and 8. In View of the fact that a relatively la r an amount of the powdered ore will remain in suspension while the liquid is in motion when it is placed in the vat and is simultanenu'sly subjected to the action of electricity, motlbn and heat until the major part of the metal is deposited on the cathode 3, it will be appreciated that I am enabled by the use of this apparatus and by the practice of this method to speedily extract pure metals from electrolytes of this nature. I have ascertained that by the use of such an a paratus I am enabled to effect such a circuiiition of the ore through the electrolyte and to simultaneously so heat the same as to effect a very rapid extraction of. the metal.
I have ascertained in the practice of the hereinbefore described method that the electrolyte should be heated to temperatures varying from 150 to 212 l inasmuch as such heating controls the liberation of the gold resolvent, and these temperatures will differ for different ores. By the use of heat in this manner the liberation of the gold resolvent is controlled in such a way that there is no sensible loss of the resolvent, and in the implication of heat simultaneously with )I'OPLI' agitation and by sinmltaneously subjecting the electrolyte to electrical currents I am enabled to obtain the best possible results in the separation of gold and other precious metals from electrolytes as thus treated.
I used It will be understood, of course, that in the practice of this method and the use of this apparatus the sufficiency of heat and the use of this apparatus in extracting gold the salts thereof that may be found in the ore are dissolved and deposited on the cathode by the simultaneous action of heat, agitation and electrical energy.
The microscopic particles of the gold in the ore are dissolved in the electrolyte during the process and reduced by a. deposition on the cathode. After the process has been continued for several hours, depending upon the nature of the electrolyte and the quality of the ore to be operated upon, it is discontinued and the electrolyte in a quiet or undisturbed condition is allowed to settle, so that all of the solid matter held in suspension falls to the bottom and the liquid ma y be siphoned oil into anothervat, when the electrodes and steam pipes may be lifted out, leaving said vat in condition for the next batch of material to be treated. The electrode upon which the gold is deposited is then subjected to suflicient heat to fuse it and'the gold is separated therefrom in the usual manner. It will be appreciated also that inasmuch as varying voltages of electrical energy may often be required during the use of this process, dependent upon the particular quality of the powdered ore to be separated, the exciting dynamo to be used should be so constructed or arranged as to allow a large range in E. M. F, while the amperage ,ca )acity thereof should not be materially a 'eeted. It will also be apparent that any preferred source of heated vapor Having thus described my invention what I claim and desire to secure by Letters Patent of the United States is 1. A method of extracting metals which consists in simultaneously subjecting the powdered ore thereof while in suspension in an electrolyte to the combined action of a heated vapor or gas while in motion, and an electrical current. I u 2. A method of extracting metals which consists in simultaneously subjecting the powdered ore thereof while in suspension in an electrolyte to the agitating effect of a heated vapor orgas and 111 simultaneously effecting the deposition of the metal upon a fusible electrode.
A method of extracting metals which consists in simultaneously subjecting the pmvdered'ore thereof while in suspension in an electrolyte to the agitating effect of a heated vapor or gas and in simultaneously effecting the deposition of the metal upon an velectrode capable of being disintegrated by heat.
In testimony whereof I have signed my name to this specification in the presence of two subscribing witnesses.
JAMES HART ROBERTSON.
Witnesses C. J. KIN'rNIca, M. F. KnA'rnyc.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US55948510A US978211A (en) | 1910-05-05 | 1910-05-05 | Art of extracting metals electrolytically. |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US55948510A US978211A (en) | 1910-05-05 | 1910-05-05 | Art of extracting metals electrolytically. |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US978211A true US978211A (en) | 1910-12-13 |
Family
ID=3046589
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US55948510A Expired - Lifetime US978211A (en) | 1910-05-05 | 1910-05-05 | Art of extracting metals electrolytically. |
Country Status (1)
| Country | Link |
|---|---|
| US (1) | US978211A (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4510027A (en) * | 1981-04-15 | 1985-04-09 | Freeport Minerals Company | Simultaneous leaching and electrodeposition of precious metals |
| WO2005040435A1 (en) * | 2003-10-27 | 2005-05-06 | David Pearce | Oxidative leach process for recovery of hydrocarbons and the extraction of metals |
-
1910
- 1910-05-05 US US55948510A patent/US978211A/en not_active Expired - Lifetime
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4510027A (en) * | 1981-04-15 | 1985-04-09 | Freeport Minerals Company | Simultaneous leaching and electrodeposition of precious metals |
| WO2005040435A1 (en) * | 2003-10-27 | 2005-05-06 | David Pearce | Oxidative leach process for recovery of hydrocarbons and the extraction of metals |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| AU2012358205B2 (en) | A system and method for extraction and refining of titanium | |
| JPH07505443A (en) | Electrochemical system for recovery of metals from metal compounds | |
| US4159232A (en) | Electro-hydrometallurgical process for the extraction of base metals and iron | |
| US978211A (en) | Art of extracting metals electrolytically. | |
| EP0244919B1 (en) | An electrode for an electrolytic cell for recovery of metals from metal bearing materials and method of making same | |
| CA1064860A (en) | Electrolytic cell for use in hydroelectrometallurgy | |
| JP2005036245A (en) | Method and electrochemical cell for electrochemically decomposing precursors in powder form | |
| US1449462A (en) | Method and apparatus for the electrolytic recovery of copper | |
| US2481079A (en) | Method of making electrolytic dendritic powdered iron | |
| US588883A (en) | Process of making litharge or protoxid of lead from lead ore | |
| US1001449A (en) | Method or process of and apparatus for extracting metals from the ores thereof. | |
| US596458A (en) | Process of and apparatus for extracting metals from ores | |
| US679253A (en) | Process of obtaining volatile elements from their compounds. | |
| US1494071A (en) | Process for recovering precious metals | |
| SU379659A1 (en) | Vseso! <Ezna> & 1 | |
| US590524A (en) | Apparatus for extracting precious metals from black sand | |
| US584242A (en) | Process of making commercial lead from lead ore | |
| US1502213A (en) | Electrolytic process for the production of sulphides | |
| US1304222A (en) | George d | |
| US1545385A (en) | Process for electrolyzing fused metallic salts | |
| US1849749A (en) | Electric furnace | |
| US876346A (en) | Process of precipitating metals. | |
| US578171A (en) | Charles p | |
| RU2534093C2 (en) | Method of copper-electrolyte processing | |
| US1953364A (en) | Amalgamation |