US788506A - Apparatus for agitating the contents of electrolytic cells. - Google Patents

Apparatus for agitating the contents of electrolytic cells. Download PDF

Info

Publication number
US788506A
US788506A US18140103A US1903181401A US788506A US 788506 A US788506 A US 788506A US 18140103 A US18140103 A US 18140103A US 1903181401 A US1903181401 A US 1903181401A US 788506 A US788506 A US 788506A
Authority
US
United States
Prior art keywords
contents
cell
electrolytic
agitating
current
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
Application number
US18140103A
Inventor
Edgar Arthur Ashcroft
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Individual
Original Assignee
Individual
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Individual filed Critical Individual
Priority to US18140103A priority Critical patent/US788506A/en
Application granted granted Critical
Publication of US788506A publication Critical patent/US788506A/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Images

Classifications

    • 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
    • C25B9/70Assemblies comprising two or more cells
    • CCHEMISTRY; METALLURGY
    • C25ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25BELECTROLYTIC OR ELECTROPHORETIC PROCESSES FOR THE PRODUCTION OF COMPOUNDS OR NON-METALS; APPARATUS THEREFOR
    • C25B11/00Electrodes; Manufacture thereof not otherwise provided for
    • C25B11/02Electrodes; Manufacture thereof not otherwise provided for characterised by shape or form
    • C25B11/033Liquid electrodes
    • 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
    • C25B9/30Cells comprising movable electrodes, e.g. rotary electrodes; Assemblies of constructional parts thereof
    • C25B9/303Cells comprising movable electrodes, e.g. rotary electrodes; Assemblies of constructional parts thereof comprising horizontal-type liquid electrode

Definitions

  • My invention relates especially to electrolytic cells in which a fused electrolyte or intermediate electrode is employed at a comparatively high-current density and requires agitation or circulation and for moving and circulating an intermediate electrode of liquid metal, such as fused lead in the production of caustic soda or metallic sodium.
  • Figure 1 is a transverse longitudinal central section of an electrolytic cell constructed in accordance with this invention.
  • Fig. 2 is a plan of the same.
  • Fig. 3 is a longitudinal central section of an alternative form of cell.
  • Fig. 4 is a plan of the same.
  • Fig. 5 is a longitudinal central section of a third form of cell, and
  • Fig. 6 is a plan of the same.
  • an electrolytic vessel A containing an electrolyte B, such as fused sodium chlorid, has a central anode C, of carbon or the like, and a cathode D, which may be a mass of fused lead at the bottom of the cell.
  • An clectroniagnet E with an iron pot E to conduct the lines of magnetic force are placed concentrically beneath the cell A and set up a violent swirl of the whole contents of the bath, the necessary condition being that the lines of magnetic force shall cut the lines of current-flow more or less at right angles and shall lie in planes at right angles to the direction of the required motion.
  • the direction of rotation of the fluid-armature will be according to the relative directions of the magnetism and the current.
  • a second electrolytic vessel F containing an electrolyte Cr, such as fused caustic soda, is placed beside the first vessel A and is connected therewith by tangential passages H at the bottom of the vessels.
  • the second cell F has a cathode J, of nickel or the like, and the anode consists of the intermediate electrode D, such as sodiumlead alloy, and the current entering the first cell at C is thus conducted through the alloy D to the second cell, where it leaves by the cathode J.
  • An electromagnet K in an iron pot K is placed concentrically beneath the vessel, as before. If the swirls in the two vessels A and F be caused to take place in the same direction, some of the intermediate electrodes will pass along the channels H, thereby causing a systematic transference of the liquid electrode.
  • the transference of the liquid electrode between the cells may also be effected by the employment of a baffleplate L, the passages H being then arranged near the bafiie and on opposite sides thereof, so that the current of liquid in the cells impinging on the baflfle is directed through the passages H.
  • the single horseshoe-magnet M has been illustrated having one pole M vertically below the first cell A and the other pole M vertically below the second cell F, and the same efiect as before is produced, as the lines of magnetic force out the lines of current-flow at right angles and in such a direction as to produce unidirectional rotation.
  • the differences of level at the center and periphery produced by the rotation of the contents of the cells may be turned to account in transferring the intermediate electrode between the cells.
  • one passage H leads from the center of the first cell A to the periphery of the second cell F, and the other passage H leads from the center of the second cell to the periphery of the first, and as the pressure of the periphery in each case is greater than that at the center circulation is produced.
  • an electrolytic apparatus the combination of a cell containing a fused electrolyte and a fused electrode beneath the electrolyte, means for passing an electrolytic current through the cell in a substantial radial direction,and an electromagnet placed beneath the center of the cell to cause rotation of the contents.
  • an electrolytic apparatus the combination of a cell containing a central anode, an electrolyte and a cathode of fused material beneath the electrolyte, means for passing an electrolytic current through the cell, and an electromagnet placed beneath the center of the cell to cause rotation of the contents.
  • an electrolytic apparatus the combination of two cells containing fused electrolytes and an intermediate fused electrode beneath the electrolytes, means for passing an electrolytic current through each cell in a substantially radial direction, two electromagnets placed beneath the vessels to cause rotation of the contents and two conduits between the cells to cause transference of the intermediate electrode from one cell to another.

Landscapes

  • 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. 788,506. PATENTE'D MAY 2, 1905.
, E.A. ASHCROFT. APPARATUS FOR. ACITATING THE CONTENTS OF ELECTROLYTIC CELLS.
APPLICATION FILED NOV. 16, 1903.
5 sums-42mm 1.
ll 1 Ill -l l ln No. 788,506. PATENTED MAY 2, 1905.
E. A. ASHCROFT. APPARATUS FOR. AGITATING THE CONTENTS OF ELECTROLYTIC GELLS.
APPLICATION FILED NOV. 16, 1903.
5 SHBETS-SHEET 2.
PATENTED MAY 2. 1905.
. E. A. ASHCROFT. APPARATUS FOR AGITATIVNG THE CONTENTS OF ELECTROLYTIC CELLS.
APPLIOATION FILED NOV. 16, 1903.-
5 Santa's-SHEET a.
No. 788,506. PATENTED MAY 2, 1905. E. A. ASHCROFT. APPARATUS FOR AGITATING THE CONTENTS OF ELECTROLYTIC CELLS.
' APPLICATION FILED NOV. 16, 1903.
5 SHEETS-SHEET 4.
I l 1 I x l I I No. 788,506. PATENTED MAY 2, 1905. E. A. ASHCROFT.
APPARATUS FOR-AGITATING THE CONTENTS OF ELECTROLYTIC CELLS.
v APPLICATION FILED NOV.16, 1903.
5 SHEETS-SHEET 6.
NTTED STATES Patented May 2, 1905.
PATENT OFFICE.-
APPARATUS FOR AGITATING THE CONTENTS OF ELECTROLYTIC CELLS.
SPECIFICATION forming part of Letters Patent No. 788,506, dated May 2, 1905.
Application filed November 16, 1903. Serial No- 181,401.
To (ti/Z whom it may concern:
Be it known that I, EDGAR ARTHUR Asuoaor'r, a subject of the King of England, residing at Weston, via Runcorn, in the county of Chester, England, have invented a new and useful Improved Apparatus for Agitating the Contents of Electrolytic Cells or Effecting Systematic Transference of Portions of the Contents from One Cell to Another, of which the following is a specification.
My invention relates especially to electrolytic cells in which a fused electrolyte or intermediate electrode is employed at a comparatively high-current density and requires agitation or circulation and for moving and circulating an intermediate electrode of liquid metal, such as fused lead in the production of caustic soda or metallic sodium.
The following details will explain how my invention is carried out.
If a circular vessel containing fused chlorid of sodium be carrying a current which enters the bath more or less centrally and leaves it more or less peripherally, (as when a fused lead cathode and carbon anode are employed in production of sodium-lead alloy or sodium amalgam from chlorid of sodium,) 2. common pot electromagnet having concentric poles when placed concentrically beneath the bath will set up a violent swirl of the whole contents of the bath, the necessary condition being that the lines of magnetic force shall cut the lines of current-flow more or less at right angles and in a plane at right angles to the direction of the required motion. The direction of rotation of the fluid-armature will be according to the relative directions of the magnetism and the current-flow.
If two vessels are placed side two pot-magnets arranged below them, the two swirls being caused to take place in'the same direction, it will be evident that by a simple arrangement of channels with or without baffles a regular flow into and out of each vessel may be made to take place, and in this manner an efiicient means is provided for the circulation of the intermediate electrode sometimes employed in the production of caustic soda or sodium-lead alloys as well as of agitating the contents of the bath.
by side and By employing a single horseshoe-electromagnet one pole of which is vertically below each of the two vessels served by the intermediate electrode the same effect is produced, the lines of magnetic force cutting the lines of current-flow at right angles and in such a direction as to produce unidirectional rotation.
In the accompanying drawings, Figure 1 is a transverse longitudinal central section of an electrolytic cell constructed in accordance with this invention. Fig. 2 is a plan of the same. Fig. 3 is a longitudinal central section of an alternative form of cell. Fig. 4 is a plan of the same. Fig. 5 is a longitudinal central section of a third form of cell, and Fig. 6 is a plan of the same.
Like letters indicate like parts throughout the drawings.
Referring to Figs. 1 and 2, an electrolytic vessel A, containing an electrolyte B, such as fused sodium chlorid, has a central anode C, of carbon or the like, and a cathode D, which may be a mass of fused lead at the bottom of the cell. An clectroniagnet E with an iron pot E to conduct the lines of magnetic force are placed concentrically beneath the cell A and set up a violent swirl of the whole contents of the bath, the necessary condition being that the lines of magnetic force shall cut the lines of current-flow more or less at right angles and shall lie in planes at right angles to the direction of the required motion. The direction of rotation of the fluid-armature will be according to the relative directions of the magnetism and the current. A second electrolytic vessel F, containing an electrolyte Cr, such as fused caustic soda, is placed beside the first vessel A and is connected therewith by tangential passages H at the bottom of the vessels. The second cell F has a cathode J, of nickel or the like, and the anode consists of the intermediate electrode D, such as sodiumlead alloy, and the current entering the first cell at C is thus conducted through the alloy D to the second cell, where it leaves by the cathode J. An electromagnet K in an iron pot K is placed concentrically beneath the vessel, as before. If the swirls in the two vessels A and F be caused to take place in the same direction, some of the intermediate electrodes will pass along the channels H, thereby causing a systematic transference of the liquid electrode.
Referring to Figs. 3 and 4, the transference of the liquid electrode between the cells may also be effected by the employment of a baffleplate L, the passages H being then arranged near the bafiie and on opposite sides thereof, so that the current of liquid in the cells impinging on the baflfle is directed through the passages H. In this case the single horseshoe-magnet M has been illustrated having one pole M vertically below the first cell A and the other pole M vertically below the second cell F, and the same efiect as before is produced, as the lines of magnetic force out the lines of current-flow at right angles and in such a direction as to produce unidirectional rotation.
Referring to Figs. 5 and 6, the differences of level at the center and periphery produced by the rotation of the contents of the cells may be turned to account in transferring the intermediate electrode between the cells. Thus one passage H leads from the center of the first cell A to the periphery of the second cell F, and the other passage H leads from the center of the second cell to the periphery of the first, and as the pressure of the periphery in each case is greater than that at the center circulation is produced. I
I am aware that certain uses of a magnetpole have been suggested for moving mercury carrying a current in various processes and industrial operations.
WVhat I claim as my invention, and desire to secure by Letters Patent, is-
1. In an electrolytic apparatus, the combination of a cell containing a fused electrolyte and a fused electrode beneath the electrolyte, means for passing an electrolytic current through the cell in a substantial radial direction,and an electromagnet placed beneath the center of the cell to cause rotation of the contents.
2. In an electrolytic apparatus, the combination of a cell containing a central anode, an electrolyte and a cathode of fused material beneath the electrolyte, means for passing an electrolytic current through the cell, and an electromagnet placed beneath the center of the cell to cause rotation of the contents.
3. In an electrolytic apparatus the combination of two connected cells containing fused electrolytes and an intermediate fused electrode beneath the electrolytes, means for passing an electrolytic current through each cell in a substantially radial direction and two electromagnets placed beneath the vessels to cause rotation of the contents and the transference of the intermediate electrode from one cell to the other.
4:. In an electrolytic apparatus the combination of two cells containing fused electrolytes and an intermediate fused electrode beneath the electrolytes, means for passing an electrolytic current through each cell in a substantially radial direction, two electromagnets placed beneath the vessels to cause rotation of the contents and two conduits between the cells to cause transference of the intermediate electrode from one cell to another.
In testimony whereof I have signed my name to this specification in the presence of two subscribing witnesses.
EDGAR ARTHUR ASHCROFT.
Witnesses:
WILLIAM H. BALLANTYNE, HARRY B. BRIDGE.
US18140103A 1903-11-16 1903-11-16 Apparatus for agitating the contents of electrolytic cells. Expired - Lifetime US788506A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
US18140103A US788506A (en) 1903-11-16 1903-11-16 Apparatus for agitating the contents of electrolytic cells.

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US18140103A US788506A (en) 1903-11-16 1903-11-16 Apparatus for agitating the contents of electrolytic cells.

Publications (1)

Publication Number Publication Date
US788506A true US788506A (en) 1905-05-02

Family

ID=2856996

Family Applications (1)

Application Number Title Priority Date Filing Date
US18140103A Expired - Lifetime US788506A (en) 1903-11-16 1903-11-16 Apparatus for agitating the contents of electrolytic cells.

Country Status (1)

Country Link
US (1) US788506A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3030888A (en) * 1957-11-12 1962-04-24 Keltz Laurence Electromagnetic pump
US3574485A (en) * 1958-11-28 1971-04-13 Broido Louis Method and apparatus for movement of liquids by electromagnetic means
US5240569A (en) * 1991-09-30 1993-08-31 Rockwell International Corporation Magnetically enhanced electrolysis cell system

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3030888A (en) * 1957-11-12 1962-04-24 Keltz Laurence Electromagnetic pump
US3574485A (en) * 1958-11-28 1971-04-13 Broido Louis Method and apparatus for movement of liquids by electromagnetic means
US5240569A (en) * 1991-09-30 1993-08-31 Rockwell International Corporation Magnetically enhanced electrolysis cell system

Similar Documents

Publication Publication Date Title
US788506A (en) Apparatus for agitating the contents of electrolytic cells.
JP6345005B2 (en) Ammonia electrosynthesis system
US3785951A (en) Electrolyzer comprising diaphragmless cell spaces flowed through by the electrolyte
NO128335B (en)
US3450623A (en) Electrolytic apparatus for the regeneration of chromium salt solutions
US800984A (en) Process of purifying metals.
US968492A (en) Electrolytic cell.
US473117A (en) Electrode for use in electro-metallurgical processes
US651849A (en) Electrolytic apparatus.
US1077894A (en) Electrode.
US1239443A (en) Apparatus for electrolytic deposition.
US825057A (en) Method of making sulfuric acid.
US1585716A (en) Preparation of sodium
US565953A (en) Emile andreoli
US1296046A (en) Electrolytic cell.
US512266A (en) Emile andreoli
US1376495A (en) Electrolytic cell
US1941816A (en) Electrolytic method and cell for the decomposition of water
US1092369A (en) Process of making chlorates and apparatus therefor.
US2291644A (en) Apparatus for electrolysis of fused electrolytes
US1190879A (en) Method of regenerating electric batteries.
US1486546A (en) Electrolytic separation
US895159A (en) Method of producing amalgams or alloys.
US1359716A (en) Ebhest a
US674927A (en) Electrode for electrolytic cells.