US2562150A - Electrical contact for electrolytic cells - Google Patents

Electrical contact for electrolytic cells Download PDF

Info

Publication number
US2562150A
US2562150A US580782A US58078245A US2562150A US 2562150 A US2562150 A US 2562150A US 580782 A US580782 A US 580782A US 58078245 A US58078245 A US 58078245A US 2562150 A US2562150 A US 2562150A
Authority
US
United States
Prior art keywords
carbon
anode
fluorine
cell
electrolyte
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
US580782A
Inventor
Sidney G Osborne
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 US580782A priority Critical patent/US2562150A/en
Application granted granted Critical
Publication of US2562150A publication Critical patent/US2562150A/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
    • C25B9/60Constructional parts of cells
    • C25B9/65Means for supplying current; Electrode connections; Electric inter-cell connections

Definitions

  • This invention relates to electrolytic cells and more particularly to electrolytic cells suitable for the production of hydrogen and fluorine from a molten electrolyte comprising hydrogen fluoride absorbed in an alkali metal fluoride.
  • Hydrogen and fluorine gase may be produced in a suitable cell by the electrolysis of an electrolyte comprising a mixture of hydrogen fluoride and an alkali metal fluoride.
  • the cell may comprise a plurality of cathodes and anodes immersed in the electrolyte and the cell is constructed to collect the hydrogen and fluorine gases separately.
  • Electrolytic cells for this purpose are well known in the art and one such is described in the copending patent application of Kenneth E. Stuart and Sidney G. Osborne, Serial No. 526,634, filed March 15, 1944 (now Patent Number 2,544,285).
  • the anodes of electrolytic cells of this character may comprise nickel or carbon. Carbon has been found to be particularly satisfactory for us in this connection, the carbon anodes being at least partially immersed in the electrolyte and held in position by a suitable metal support above the surface of the electrolyte.
  • a further object of this invention is to provide means and method for improving the electrical conductivity between the metal support and the carbon anode of an electrolytic fluorine cell.
  • a further object of this invention is to provide means and method for reducing corrosion adjacent the contact surfaces of a carbon anode and the metal support associated therewith in an electrolytic fluorine cell.
  • An additional object of this invention is the provision of a joint, and method for forming same, between the contacting surfaces of a carbon anode and a metal support of an electrolytic fluorine cell which will resist the penetration of corrosive agents such as fluorine or molten electrolyte.
  • An additional object of this invention is the provision of an electrolytic fluorine cell which is constructed to insure optimum electrical conductivity between the anode and metal support therefor at all times.
  • An additional object of this invention is the provision of an electrolytic fluorine cell which may be operated over a long period of time without interruption because of carbon anode breakage.
  • a joint be tween the carbon electrode and the metal support which serves to strengthen the structure and which serves to prevent the penetration of corrosive fluorine or molten electrolyte between the contact surfaces.
  • This joint comprises an interlayer of particulate carbon positioned between the electrode and the metal support at the time these members are secured together.
  • the joint between an anode and its metal support may be formed by coating the surfaces to be contacted with a suspension of carbon in a volatile liquid.
  • the carbon anode and the metal support are then clamped Or otherwise secured together and the liquid is removed by evaporation. This may be effected by baking or otherwise heating the resulting joint.
  • a structure is formed which contains no cracks or crevices thereby strengthening the contact joint and preventing the penetration of the corrosive agents thereinto.
  • a particularly useful carbon suspension that may be used in forming the interlayer for the electrode structure of this invention may comprise a composition known commercially as aquadag.
  • Aquadag sometimes used as a lubricant in other arts, comprises a dispersion of colloidal graphite in water.
  • any other dispersion of particulate carbon in a volatile liquid may be employed without departing from the spirit and scope of this invention.
  • the relative proportions of particulate carbon or colloidal graphite to volatile liquid in the mixture that is used to form the interlayer do not appear to be particularly critical.
  • the composition. used should be of sufiicient consistency to permit ready application to the surfaces to be contacted and which, upon evaporization of if! the liquid, will leave suiflcient carbon to provide an interlayer havin the desired function.
  • this invention is useful in the construction of electrolytic'cells for producing hydrogen and fluorine from a molten mixture of hydrogen fluoride and an alkali metal fluoride.
  • the invention has particular use in those anode structures comprising a carbon body secured to a support comprising a metal selected from the group consisting of iron and copper, a suitable electrolytic cell and anode structure in which this invention may be employed being disclosed in the above referred to application Serial No. 526,634.
  • this invention may be applied to theconstruction of any electrode which is adapted to be used in a fluorine cell and where-- in a carbon electrode is to be secured to a metal support through which an electric current is supplied to the carbon electrode.
  • Fig. 1 is an elevational view of a portion of a fluorine cell in accordance with the disclosure contained in the above-referred-to application Serial No. 526,634, and Fig. 2 is an enlarged par tial sectionalview of the upper portion of a carbon anode secured to a metal support in accoru ance with one embodiment of the invention.
  • a fluorine cell comprising a cell body Ill, a cooling jacket 12, removable cover plates [fl and 1-3, a conduit [8 for drawing off electrolyte within the cell body, said electrolyte, during operation of the cell, being normally maintained at level 28.
  • a cathode assembly is provided comprising a cathode plate 22 supported by an end plate 24 secured to a suitable electrical conductor 2%.
  • an anode assembly is provided comprising carbon plate 28 engaged by metal supports 36 and secured thereto by suitable bolts 32.
  • a conductor 34 is provided for supplying electrical current to the carbon anodes 28 through the metal supports 31
  • the metal supports 30 are preferably formed of iron or copper.
  • Means is also provided between the cathode and anode assemblies for permitting free diffusion of liquid electrolyte therebetween but for preventing the recombination of the hydrogen and fluorine gases that are liberated from the cathode and anode, respectively.
  • This means comprises a plate 36 secured to a flange 38 depending from the cover plate Hi and an additional plate lii secured to plate 36 extending between the cathode plate 2.2 and the carbon anode plate 28 and parallel thereto.
  • the plate (if) is provided with a Window adjacent the carbon anode .28 having a metal screen ei positioned therein permitting free diffusion of electrolyte between the electrodes but preventing free hydrogen and fluorine gases from intermingling within the electrolyte.
  • each carbon anode of the fluorine cell may be secured to the metal support as indicated in Fig. 2 wherein the anode 23 is clamped between two support plates 3! ⁇ by means of the bolts 32 provided with split washers 421.
  • interlayers l -l of carbon are provided between the support plates and the carbon anode.
  • the carbon interlayers comprise graphite particles formed from a suspension thereof in a volatile liquid, such as water, and from. which the water has been separated by evaporation in situ.
  • the graphite particles fill the space between the anode and the support and are efiective to strengthen the joint and to prevent fluorine gas or molten electrolyte from penetrating the structure.
  • the formation of fluorides in the joint is thereby prevented which, if present, would increase the resistance of the joint and increase the tendency of the anode to break adjacent the support.
  • a method of improving the resistance to penetration of fluorine gas and electrolyte between the contact surfaces of a metallic con-' ductor and a carbon anode of an electrolytic cell for the production of elemental fluorine from an electrolyte comprising hydrogen fluoride and an alkali metal fluoride which comprises introducing finely divided carbon in an aqueous vehicle between said surfaces and thereafter evaporating the water therefrom.
  • An electrode assembly suitably for use in an electrolytic cell for producing hydrogen and fluorine comprising a carbon member adapted to be immersed in the electrolyte of the cell, a metal support for said carbon member through which an electric current is supplied to said member, and a carbon interlayer in the joint between said member and said support formed by introducing finely divided. carbon in anaqueous vehicle between said surfaces and thereafter evaporating the Water therefrom.

Description

y 1951 s. G. OSBORNE 2,562,150
ELECTRICAL CONTACT FOR ELECTROLYTIC CELLS Filed March 5, 1945 (Cafhoae) 22 [0 fer/dyer) 4 4 .30
( C arbor;
2 Y 28 (finode/ 5/24/7 6 flsbarne 9% M w/Md Patented July 21; 1951 UNITED ELECTRICAL CONTACT FOR ELECTROLYTIC CELLS Sidney G. Osborne, Niagara Falls, N. Y., assignor to the United States of America as represented by the United States Atomic Energy Commission Application March 3, 1945, Serial No. 580,782
2 Claims.
s This invention relates to electrolytic cells and more particularly to electrolytic cells suitable for the production of hydrogen and fluorine from a molten electrolyte comprising hydrogen fluoride absorbed in an alkali metal fluoride.
Hydrogen and fluorine gase may be produced in a suitable cell by the electrolysis of an electrolyte comprising a mixture of hydrogen fluoride and an alkali metal fluoride. The cell may comprise a plurality of cathodes and anodes immersed in the electrolyte and the cell is constructed to collect the hydrogen and fluorine gases separately. Electrolytic cells for this purpose are well known in the art and one such is described in the copending patent application of Kenneth E. Stuart and Sidney G. Osborne, Serial No. 526,634, filed March 15, 1944 (now Patent Number 2,544,285). The anodes of electrolytic cells of this character may comprise nickel or carbon. Carbon has been found to be particularly satisfactory for us in this connection, the carbon anodes being at least partially immersed in the electrolyte and held in position by a suitable metal support above the surface of the electrolyte.
In electrolytic cell of this general character considerable difliculty has been experienced in the breakage of carbon anodes adjacent the metal support and in the corrosion of the support at this point.
Accordingly, it is one object of this invention to provide means and method for reducing the tendency of a carbon anode of an electrolytic fluorine cell to break adjacent the metal support therefor.
A further object of this invention is to provide means and method for improving the electrical conductivity between the metal support and the carbon anode of an electrolytic fluorine cell.
A further object of this invention is to provide means and method for reducing corrosion adjacent the contact surfaces of a carbon anode and the metal support associated therewith in an electrolytic fluorine cell.
An additional object of this invention is the provision of a joint, and method for forming same, between the contacting surfaces of a carbon anode and a metal support of an electrolytic fluorine cell which will resist the penetration of corrosive agents such as fluorine or molten electrolyte.
An additional object of this invention is the provision of an electrolytic fluorine cell which is constructed to insure optimum electrical conductivity between the anode and metal support therefor at all times.
An additional object of this invention is the provision of an electrolytic fluorine cell which may be operated over a long period of time without interruption because of carbon anode breakage. 1 I
Further and additional objects will be apparent from the followin description, the accompanying drawing, and the appended clr In the operation of an electrolytic fluorine cell, fluorine gas will normally come into contact with the anode adjacent the metal support therefor. Also the molten electrolyte may contact this area due to splashing or effervescence of gas during electrolysis. It is important to prevent the fluorine gas or molten electrolyte from penetrating between the contact surfaces of the anode and the support since this may result in the deposition of fluorides. The deposition of the fluorides between these contact surfaces tends to exert considerable pressure which may result in the breakage of the carbon anode. Also these fluorides have a high electrical resistance which may result in local heating of the contact during the operation of the electrolytic cell, thus increasing the danger of breakage and the tendency of the joint to become insulated resulting in malfunctioning of the anode. Therefore, it has been found to be important that the joint between the anode and the metal support be formed so as to prevent the penetration of fluorine gas or electrolyte.
In accordance with this invention a joint be tween the carbon electrode and the metal support is provided which serves to strengthen the structure and which serves to prevent the penetration of corrosive fluorine or molten electrolyte between the contact surfaces. This joint comprises an interlayer of particulate carbon positioned between the electrode and the metal support at the time these members are secured together.
In accordance with one embodiment of this invention the joint between an anode and its metal support may be formed by coating the surfaces to be contacted with a suspension of carbon in a volatile liquid. The carbon anode and the metal support are then clamped Or otherwise secured together and the liquid is removed by evaporation. This may be effected by baking or otherwise heating the resulting joint. Thus a structure is formed which contains no cracks or crevices thereby strengthening the contact joint and preventing the penetration of the corrosive agents thereinto. V
A particularly useful carbon suspension that may be used in forming the interlayer for the electrode structure of this invention ma comprise a composition known commercially as aquadag. Aquadag, sometimes used as a lubricant in other arts, comprises a dispersion of colloidal graphite in water. However, it will be apparent to one skilled in the art that any other dispersion of particulate carbon in a volatile liquid may be employed without departing from the spirit and scope of this invention. The relative proportions of particulate carbon or colloidal graphite to volatile liquid in the mixture that is used to form the interlayer do not appear to be particularly critical. However, it will be evident that the composition. used should be of sufiicient consistency to permit ready application to the surfaces to be contacted and which, upon evaporization of if! the liquid, will leave suiflcient carbon to provide an interlayer havin the desired function.
As previously indicated, this invention is useful in the construction of electrolytic'cells for producing hydrogen and fluorine from a molten mixture of hydrogen fluoride and an alkali metal fluoride. The invention has particular use in those anode structures comprising a carbon body secured to a support comprising a metal selected from the group consisting of iron and copper, a suitable electrolytic cell and anode structure in which this invention may be employed being disclosed in the above referred to application Serial No. 526,634. However, it will be apparent to one skilled in the art that this invention may be applied to theconstruction of any electrode which is adapted to be used in a fluorine cell and where-- in a carbon electrode is to be secured to a metal support through which an electric current is supplied to the carbon electrode.
' For a more complete understanding of this invention, reference is made to the accompanying drawing disclosing one embodiment, wherein:
Fig. 1 is an elevational view of a portion of a fluorine cell in accordance with the disclosure contained in the above-referred-to application Serial No. 526,634, and Fig. 2 is an enlarged par tial sectionalview of the upper portion of a carbon anode secured to a metal support in accoru ance with one embodiment of the invention.
With particular reference to 1, a fluorine cell is provided comprising a cell body Ill, a cooling jacket 12, removable cover plates [fl and 1-3, a conduit [8 for drawing off electrolyte within the cell body, said electrolyte, during operation of the cell, being normally maintained at level 28. A cathode assembly is provided comprising a cathode plate 22 supported by an end plate 24 secured to a suitable electrical conductor 2%. Likewise an anode assembly is provided compris ing carbon plate 28 engaged by metal supports 36 and secured thereto by suitable bolts 32. A conductor 34 is provided for supplying electrical current to the carbon anodes 28 through the metal supports 31 As previously indicated, the metal supports 30 are preferably formed of iron or copper. Means is also provided between the cathode and anode assemblies for permitting free diffusion of liquid electrolyte therebetween but for preventing the recombination of the hydrogen and fluorine gases that are liberated from the cathode and anode, respectively. This means comprises a plate 36 secured to a flange 38 depending from the cover plate Hi and an additional plate lii secured to plate 36 extending between the cathode plate 2.2 and the carbon anode plate 28 and parallel thereto. The plate (if) is provided with a Window adjacent the carbon anode .28 having a metal screen ei positioned therein permitting free diffusion of electrolyte between the electrodes but preventing free hydrogen and fluorine gases from intermingling within the electrolyte.
During the operation of the cell, the electrolyte circulates by convection in the manner indicated by the arrows in Fig. 1 and the hydrogen and fluorine gases are collected separately and separately withdrawn from the cell body by' means, not shown. Additional details concerning the above described fluorine cell are presented in the aforesaid patent application Serial No. 526,634, from which it will be apparent that it is preferable to provide a number of anode plates, cathode plates, and diffusion plates within a single cell .body.
In accordance with the present invention each carbon anode of the fluorine cell may be secured to the metal support as indicated in Fig. 2 wherein the anode 23 is clamped between two support plates 3!} by means of the bolts 32 provided with split washers 421. As previously indicated, interlayers l -l of carbon are provided between the support plates and the carbon anode. The carbon interlayers comprise graphite particles formed from a suspension thereof in a volatile liquid, such as water, and from. which the water has been separated by evaporation in situ. The graphite particles fill the space between the anode and the support and are efiective to strengthen the joint and to prevent fluorine gas or molten electrolyte from penetrating the structure. The formation of fluorides in the joint is thereby prevented which, if present, would increase the resistance of the joint and increase the tendency of the anode to break adjacent the support.
Other mechanical means for attaching the carbon anode to the metal support will be readily apparent to one skilled in the art.
While there has been described What is at present considered to be the preferred embodiment of the invention, it will be understood that various modifications may be made therein and it is intended to cover in the appended claims all such modifications as fall within the true spirit and scope of the invention.
I claim:
1. A method of improving the resistance to penetration of fluorine gas and electrolyte between the contact surfaces of a metallic con-' ductor and a carbon anode of an electrolytic cell for the production of elemental fluorine from an electrolyte comprising hydrogen fluoride and an alkali metal fluoride, which comprises introducing finely divided carbon in an aqueous vehicle between said surfaces and thereafter evaporating the water therefrom.
2. An electrode assembly suitably for use in an electrolytic cell for producing hydrogen and fluorine comprising a carbon member adapted to be immersed in the electrolyte of the cell, a metal support for said carbon member through which an electric current is supplied to said member, and a carbon interlayer in the joint between said member and said support formed by introducing finely divided. carbon in anaqueous vehicle between said surfaces and thereafter evaporating the Water therefrom.
SIDNEY G. OSBORNE.
REFERENCES CITED The following references are of record in the file of this patent:
UNITED STATES PATENTS Number France June 29, 1925 OTHER REFERENCES Berichte der deutschen chemischen Gesellschaft; vol. 54 (1921), pages 759 through '766.'
Radio, October 1942, pages 14 and 44.
Industrial & Engineering Chemistry, vol. 39 (1947), page 253.
US580782A 1945-03-03 1945-03-03 Electrical contact for electrolytic cells Expired - Lifetime US2562150A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
US580782A US2562150A (en) 1945-03-03 1945-03-03 Electrical contact for electrolytic cells

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US580782A US2562150A (en) 1945-03-03 1945-03-03 Electrical contact for electrolytic cells

Publications (1)

Publication Number Publication Date
US2562150A true US2562150A (en) 1951-07-24

Family

ID=24322548

Family Applications (1)

Application Number Title Priority Date Filing Date
US580782A Expired - Lifetime US2562150A (en) 1945-03-03 1945-03-03 Electrical contact for electrolytic cells

Country Status (1)

Country Link
US (1) US2562150A (en)

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2878461A (en) * 1954-04-02 1959-03-17 Titanium Metals Corp Electrode attachment device
US2920028A (en) * 1954-07-12 1960-01-05 Columbia Southern Chem Corp Electrolytic cell series
US3023393A (en) * 1958-10-22 1962-02-27 Union Carbide Corp Liquid electrical connection for electrolytic cells
US3072558A (en) * 1961-02-13 1963-01-08 Dow Chemical Co Composite anode
US3676324A (en) * 1969-11-07 1972-07-11 Phillips Petroleum Co Composite carbon electrode structure having improved electrical conductivity

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR594709A (en) * 1925-06-02 1925-09-17 Le Carbone Sa Process for making porous bodies of electrodes of batteries, electrolysers or accumulators and industrial products thus obtained watertight
US1957940A (en) * 1928-11-23 1934-05-08 Conradty Ottmar Body for use in electrolysis
US2249765A (en) * 1937-07-06 1941-07-22 Du Pont Electrical contact in electrolytic cells

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR594709A (en) * 1925-06-02 1925-09-17 Le Carbone Sa Process for making porous bodies of electrodes of batteries, electrolysers or accumulators and industrial products thus obtained watertight
US1957940A (en) * 1928-11-23 1934-05-08 Conradty Ottmar Body for use in electrolysis
US2249765A (en) * 1937-07-06 1941-07-22 Du Pont Electrical contact in electrolytic cells

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2878461A (en) * 1954-04-02 1959-03-17 Titanium Metals Corp Electrode attachment device
US2920028A (en) * 1954-07-12 1960-01-05 Columbia Southern Chem Corp Electrolytic cell series
US3023393A (en) * 1958-10-22 1962-02-27 Union Carbide Corp Liquid electrical connection for electrolytic cells
US3072558A (en) * 1961-02-13 1963-01-08 Dow Chemical Co Composite anode
US3676324A (en) * 1969-11-07 1972-07-11 Phillips Petroleum Co Composite carbon electrode structure having improved electrical conductivity

Similar Documents

Publication Publication Date Title
US3591483A (en) Diaphragm-type electrolytic cells
EP0026995A1 (en) Thin carbon-cloth-based electrocatalytic gas diffusion electrodes, processes, and electrochemical cells comprising the same
CA1044175A (en) Electrolytic process for the production of metals in molten halide systems
Savinell et al. Discharge Characteristics of a Soluble Iron‐Titanium Battery System
US2358419A (en) Electrode for use in electrolytic processes
US3891531A (en) Electrolytic diaphragm cells including current connection means between the cell base and anode
US2562150A (en) Electrical contact for electrolytic cells
CA2035815C (en) Carbon electrode, and method and apparatus for the electrolysis of a hydrogen fluoride-containing molten salt by the use of the carbon electrode
GB1354314A (en) Electrolytic cell
US2249765A (en) Electrical contact in electrolytic cells
US3271289A (en) Mercury cathode electrolytic cell having an anode with high corrosionresistance and high electrical and heat conductivity
US2510128A (en) Method of plating metals with zirconium
US3796648A (en) Electrolytic cell having self-aligning anodes
US3394062A (en) Method for the electrolytic production of hydrogen and oxygen
JPH10106900A (en) Electrode for electric double layer capacitor
US2428584A (en) Liquid electrode electrolytic cell
GB1242577A (en) Apparatus for electrochemical generation of electric current
US4085027A (en) Hybrid bipolar electrode
US3000801A (en) Process for the electrolytic production of fluorine
US3507701A (en) Process of using fuel cell including tungsten oxide catalyst
US2422590A (en) Production of fluorine
US3838384A (en) Protected electrode lead for use in a corrosive environment
US2257746A (en) Electrolytic process of preparing arsenates
US3041266A (en) Fluorine cell anode assembly
Vavalides et al. High-Capacity, Long-Life Fluorine Cell