US467350A - Electrolytical plant - Google Patents
Electrolytical plant Download PDFInfo
- Publication number
- US467350A US467350A US467350DA US467350A US 467350 A US467350 A US 467350A US 467350D A US467350D A US 467350DA US 467350 A US467350 A US 467350A
- Authority
- US
- United States
- Prior art keywords
- plates
- cathode
- anode
- plate
- plant
- 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
- 229910052802 copper Inorganic materials 0.000 description 20
- 239000010949 copper Substances 0.000 description 20
- RYGMFSIKBFXOCR-UHFFFAOYSA-N copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 20
- 239000004020 conductor Substances 0.000 description 14
- 239000000463 material Substances 0.000 description 10
- 239000000243 solution Substances 0.000 description 10
- 239000002184 metal Substances 0.000 description 6
- 229910052751 metal Inorganic materials 0.000 description 6
- 241000512668 Eunectes Species 0.000 description 4
- 239000008151 electrolyte solution Substances 0.000 description 4
- 239000011810 insulating material Substances 0.000 description 4
- XEEYBQQBJWHFJM-UHFFFAOYSA-N iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 4
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 2
- 239000010425 asbestos Substances 0.000 description 2
- 239000010426 asphalt Substances 0.000 description 2
- 239000004568 cement Substances 0.000 description 2
- 239000011521 glass Substances 0.000 description 2
- PCHJSUWPFVWCPO-UHFFFAOYSA-N gold Chemical compound [Au] PCHJSUWPFVWCPO-UHFFFAOYSA-N 0.000 description 2
- 229910052737 gold Inorganic materials 0.000 description 2
- 239000010931 gold Substances 0.000 description 2
- 239000011396 hydraulic cement Substances 0.000 description 2
- 229910052742 iron Inorganic materials 0.000 description 2
- 239000007788 liquid Substances 0.000 description 2
- 238000007670 refining Methods 0.000 description 2
- 229910052895 riebeckite Inorganic materials 0.000 description 2
- 229910052709 silver Inorganic materials 0.000 description 2
- 239000004332 silver Substances 0.000 description 2
- QAOWNCQODCNURD-UHFFFAOYSA-L sulfate Chemical compound [O-]S([O-])(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-L 0.000 description 2
- 235000011149 sulphuric acid Nutrition 0.000 description 2
- 239000001117 sulphuric acid Substances 0.000 description 2
- 239000002023 wood Substances 0.000 description 2
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
- C25B9/00—Cells or assemblies of cells; Constructional parts of cells; Assemblies of constructional parts, e.g. electrode-diaphragm assemblies; Process-related cell features
- C25B9/60—Constructional parts of cells
- C25B9/65—Means for supplying current; Electrode connections; Electric inter-cell connections
Definitions
- My improvements consist in using an initial anode connected to the positive pole of the source of current-supply and a terminal cathode connected to the negative pole of the source of currentsupply, and intermediate are a series of pairs of cathode and anode plates, coupled in pairs by a vertical connection. These two plates of each pair are brought in close contact with each other, being only separable by a thin sheet of non-conducting material, as glass or asbestos.
- the anodeplates are formed of the crude material to be refined, while the cathode-plates are formed of pure copper or some other pure metal.
- Figure l is a plan view of electrolytic vat with plates in position.
- Fig. 2 is aperspective view of a method of connecting plates.
- Fig. 3 is a sectional view of electrolytic vat with plates in position.
- a A are two wooden tanks, the tank A being smaller and placed within the tank A.
- the space between the tanks A and A is filled with material B, which is of such character as to prevent leaking, such as asphaltum cement or hydraulic cement. It is preferable that this material should be an insulating material.
- C O 0 &c. are the anode-plates, which are cast in molds, preferably iron molds, and are provided with ears 0.
- a solution of sulphate of copper is placed in the vat or tank A, and the anode-plates are suspended in the solution by means of the ears 0, which rest either directly on the sides of the vat or on a piece of rubber or wood or on any non-conducting material.
- E E E E are the cathode-plates, formed of thin plates of copper or other metal, and these cathode-plates are also suspended in the liquid in the tank.
- the anode and cathode plates are connected in pairs by bringing the two plates together with a non-conducting surface between them and connecting them by one or more bolts or rivets 6, so that between a pair of anode and cathode plates there is no electrolytic solution.
- f are spacing-pins, which are inserted between each pair of plates to keep them from contact with each other and to cause the pairs of plates to retain proper position.
- D is the dynamo, and the first anode-plate is connected to the positive conductor H of said dynamo.
- the last cathode-plate is connected with the negative conductor g from the dynamo.
- the first anode-plate and the last cathode-plate stand by themselves, while the intermediate cathode and anode plates are connected together so as to form pairs.
- the object in connecting these plates in pairs in the manner herein described is to prevent any action between the cathode and anode of a pair through the medium of the electrolytic solution.
- the operation in refining copper is as follows:
- the anode-plates are composed of crude copper to be refined and the cathode-plates of pure copper or other metal.
- the current passes from the dynamo along the positive conductor to the first anode-plate, with which said conductor is directly connected and decomposes the solution between'the first anode and cathode plate which said current has to traverse, and deposits the copper upon the cathode-plate, while sulphuric acid set free dissolves an equal amount of copper from the anode-plate as has been deposited upon the cathode-plate.
- the current thus travels from -the anode-plate through the solution of sulhate of copper to the cathode-plate along of the same with the anode-plate to this anodeplate, and thence through the solution to the next cathode-plate, and so on until the last cathode-plate is reached, which plate is connected with the negative conductor from the the cathode-plate and along the connection 5 dynamo.
- the copper to be refined may conwith insulating material interposed between t-ain gold and silver, and this falls to the botsaid plates and metallic connection between tom of the tank or vat in a highly concensaid plates.
- An electrode consisting of a plate of re- THOMAS D. SIMPSON, m fined material and a plate of crude material FRANK S. BUSSER.
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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.) 2 Sheets-Sheet 1.
0; STALMANN. ELEGTROLYTIOAL PLANT.
N0 4 Patented Jan. 19, 1892.
WIT/YES SE6 MJJM 2 Shts Sheet (No Model.)
0. STALMANN. ELEGTROLYTIGAL PLANT.
Patented Jan. 19, 1892. w I i h Ma ena-'01P: mC/WW UNITED STATES PATENT OFFICE.
OTTO STALMANN, OF ANACONDA, MONTANA.
ELEC TROLYTICAL PLANT.
SPECIFICATION forming part of Letters Patent No. 467,350, dated January 19, 1892.
Application filed June 8, 1891. Serial No. 895,568- (No model.)
To all whom it may concern:
Be it known that I, OTTO STALMANN, a citizen of the United States, residing at Anaconda, county of Deer Lodge, and State of Montana, have invented a new and useful Improvement in Electrolytical Plants, of which the following is a full, clear, and exact description, reference being had to the accompanying drawings, which form a part of this specification.
My improvements consist in using an initial anode connected to the positive pole of the source of current-supply and a terminal cathode connected to the negative pole of the source of currentsupply, and intermediate are a series of pairs of cathode and anode plates, coupled in pairs by a vertical connection. These two plates of each pair are brought in close contact with each other, being only separable by a thin sheet of non-conducting material, as glass or asbestos. The anodeplates are formed of the crude material to be refined, while the cathode-plates are formed of pure copper or some other pure metal.
I will now describe one embodiment of my invention.
In the drawings, Figure l is a plan view of electrolytic vat with plates in position. Fig. 2 is aperspective view of a method of connecting plates. Fig. 3 is a sectional view of electrolytic vat with plates in position.
A A are two wooden tanks, the tank A being smaller and placed within the tank A. The space between the tanks A and A is filled with material B, which is of such character as to prevent leaking, such as asphaltum cement or hydraulic cement. It is preferable that this material should be an insulating material.
E E E are the cathode-plates, formed of thin plates of copper or other metal, and these cathode-plates are also suspended in the liquid in the tank.
\Vith the exception of the initial anode and terminal cathode, the anode and cathode plates are connected in pairs by bringing the two plates together with a non-conducting surface between them and connecting them by one or more bolts or rivets 6, so that between a pair of anode and cathode plates there is no electrolytic solution.
f are spacing-pins, which are inserted between each pair of plates to keep them from contact with each other and to cause the pairs of plates to retain proper position.
D is the dynamo, and the first anode-plate is connected to the positive conductor H of said dynamo. The last cathode-plate is connected with the negative conductor g from the dynamo.
As may be seen, the first anode-plate and the last cathode-plate stand by themselves, while the intermediate cathode and anode plates are connected together so as to form pairs. The object in connecting these plates in pairs in the manner herein described is to prevent any action between the cathode and anode of a pair through the medium of the electrolytic solution.
The operation in refining copper is as follows: The anode-plates are composed of crude copper to be refined and the cathode-plates of pure copper or other metal. The current passes from the dynamo along the positive conductor to the first anode-plate, with which said conductor is directly connected and decomposes the solution between'the first anode and cathode plate which said current has to traverse, and deposits the copper upon the cathode-plate, while sulphuric acid set free dissolves an equal amount of copper from the anode-plate as has been deposited upon the cathode-plate. The current thus travels from -the anode-plate through the solution of sulhate of copper to the cathode-plate along of the same with the anode-plate to this anodeplate, and thence through the solution to the next cathode-plate, and so on until the last cathode-plate is reached, which plate is connected with the negative conductor from the the cathode-plate and along the connection 5 dynamo. The copper to be refined may conwith insulating material interposed between t-ain gold and silver, and this falls to the botsaid plates and metallic connection between tom of the tank or vat in a highly concensaid plates.
trated state and may be collected as a by- Intestimonyof whichinventionlhave here- 5 prpldnct without? eizlztrg exprignsle. V unto set my hand.
ELVlng 110W [1 y GSOII e my lHVell 101], r v 1 what I claim as new, and desire to protect by O F l O bl ALMANN Letters Patent, is- Witnesses:
An electrode consisting of a plate of re- THOMAS D. SIMPSON, m fined material and a plate of crude material FRANK S. BUSSER.
Publications (1)
Publication Number | Publication Date |
---|---|
US467350A true US467350A (en) | 1892-01-19 |
Family
ID=2536212
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
US467350D Expired - Lifetime US467350A (en) | Electrolytical plant |
Country Status (1)
Country | Link |
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US (1) | US467350A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US20070006679A1 (en) * | 2003-05-20 | 2007-01-11 | Bangaru Narasimha-Rao V | Advanced erosion-corrosion resistant boride cermets |
-
0
- US US467350D patent/US467350A/en not_active Expired - Lifetime
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US20070006679A1 (en) * | 2003-05-20 | 2007-01-11 | Bangaru Narasimha-Rao V | Advanced erosion-corrosion resistant boride cermets |
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