US467350A - Electrolytical plant - Google Patents

Electrolytical plant Download PDF

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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
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plates
cathode
anode
plate
plant
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Premdor International Inc
Masonite International Corp
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Assigned to MASONITE INTERNATIONAL CORPORATION reassignment MASONITE INTERNATIONAL CORPORATION ASSIGNMENT OF ASSIGNORS INTEREST (SEE DOCUMENT FOR DETAILS). Assignors: STANLEY WORKS, THE
Assigned to PREMDOR INTERNATIONAL INC. reassignment PREMDOR INTERNATIONAL INC. ASSIGNMENT OF ASSIGNORS INTEREST (SEE DOCUMENT FOR DETAILS). Assignors: STANLEY WORKS, THE
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    • CCHEMISTRY; METALLURGY
    • C25ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25BELECTROLYTIC OR ELECTROPHORETIC PROCESSES FOR THE PRODUCTION OF COMPOUNDS OR NON-METALS; APPARATUS THEREFOR
    • C25B9/00Cells or assemblies of cells; Constructional parts of cells; Assemblies of constructional parts, e.g. electrode-diaphragm assemblies; Process-related cell features
    • C25B9/60Constructional parts of cells
    • C25B9/65Means 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.
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 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.
US467350D Electrolytical plant Expired - Lifetime US467350A (en)

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Cited By (1)

* Cited by examiner, † Cited by third party
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

Cited By (1)

* Cited by examiner, † Cited by third party
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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