US3658686A - Electrode assembly for compensating thermal expansion in an electrolytic cell - Google Patents

Electrode assembly for compensating thermal expansion in an electrolytic cell Download PDF

Info

Publication number
US3658686A
US3658686A US878705A US3658686DA US3658686A US 3658686 A US3658686 A US 3658686A US 878705 A US878705 A US 878705A US 3658686D A US3658686D A US 3658686DA US 3658686 A US3658686 A US 3658686A
Authority
US
United States
Prior art keywords
electrode assembly
cells
thermal expansion
plates
assembly according
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
US878705A
Other languages
English (en)
Inventor
Robert Schoberle
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
Application granted granted Critical
Publication of US3658686A publication Critical patent/US3658686A/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

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
    • C25B9/66—Electric inter-cell connections including jumper switches
    • 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

  • the rigid plate has plate electrodes secured thereon disposed vertically in spaced positions functioning as cathodes of a preceding one of next adjacent cells and the flexible membrane, which effects the thermal expansion compensation, has plate electrodes removably mounted relative thereto disposed vertically in spaced positions functioning as the anodes of the succeeding cell of the next adjacent cells and likewise supported on the rigid plate.
  • Another object of the invention is to provide a new and novel electrode assembly that carries out compensation for thermal expansion and is constructed so that corrosion of the various conductor ports is minimized by keeping the different metals remote from the electrolyte and the products of electrolysis.
  • Still another object is to provide an electrode assembly in which the anodes are removably supported thereon so that a quick removal and change over of defective electrodes can be carried out.
  • an electrode assembly comprising a rigid plate and a flexible membrane disposed in opposed relationship and spaced from each other.
  • the plate and membrane define the opposed walls of next-adjacent electrolytic cells.
  • Cathode plates are secured to the rigid wall plate of a preceding cell by welding them thereon disposed perpendicularly to the wall surface and in an upright position.
  • the anodes are similarly positioned relative to the flexible membrane and removably supported on the rigid plate.
  • the flexible membrane is framed circumferentially and is freely able to flex to carry out compensation of thermal expansion.
  • Each individual electrolytic cell in a succession or sequence of cells is provided with a flexible membrane so that the thermal expansion of each individual elementary cell is compensated and any additive thermal expansion problems are avoided.
  • FIG. 1 is an elevation view, partly in section, of a multiplecell constructed from a plurality of elementary electrolytic cells provided with thermal expansion compensating means according to the invention
  • FIG. 2 is a fragmentary sectional view on an enlarged scale taken along section line AA illustrating the assembly of two elementary electrolytic cells according to the invention
  • FIG. 3 is an elevation sectional view of an expansion-compensating electrode assembly according to the invention.
  • FIG. 4 is a plan view of the electrode assembly in FIG. 3.
  • the invention described is applied to electrolytic cells for electrolysis of sodium chloride from a sodium chloride brine or electrolyte.
  • the invention is equally applicable to electrolytic cells used for any desired electrolysis resulting in the liberation of heat and thermal expansion of the cells.
  • a multiple electrolytic cell is constructed from a succession of individual electrolytic cells.
  • Each of the basic electrolytic cells comprises a rigid tank 1 having a rigid bottom and opposed sides.
  • the cells are mounted on a base 2 to which they may be secured.
  • the cell tanks are preferably made of a synthetic resin constituting reinforced polyvinyl chloride, for example.
  • the cells may be constructed, for example, having the dimensions of about 1,100 millimeters in height with a width of about 950 millimeters and 538 millimeters in length.
  • the brine for producing the electrolytic products is introduced into the individual cell tanks through an inlet pipe 3.
  • the spent electrolyte and the products of electrolysis are discharged through a line 4.
  • Each of the cells is provided with two flanges 5 for removably mounting and securing thereon a thermal expansion compensating electrode assembly, as hereinafter explained, and constituting the end walls of a preceding cell and a succeeding next-adjacent cell.
  • the thermal expansion-compensating electrode assembly comprises a cathode support plate 6 made, for example, of steel, having welded thereto on one side steel cathodes 7, of 3 mm thickness, and on opposite sides are mounted copper cross-pieces 8 to which is secured an anode support plate 9 likewise made of copper.
  • the cathode support plate 6 and the anode support plate 9 are spaced relative to each other to allow access to steel mounting nuts 10 for the steel anodes 11 constructed as plates welded to supports or mounts 12 extending through a flexible membrane 13.
  • the flexible membrane is disposed spaced from, and in opposed relationship, to the rigid support plate 6 so that the membrane and rigid support plate form the end walls of next adjacent primary electrolytic cells 1, as illustrated in FIG. 1.
  • the cathode supports 12 have a circular cross-section and are made of titanium.
  • the flexible membrane 13 is likewise made of titanium sheet having a thickness in the order of 1 mm.
  • the anodes 11 are made of titanium plated with an electrically conductive covering, for example, a platinum-iridium alloy or ruthenium oxide.
  • the anodes have a thickness of about two millimeters and a surface area of about 0.55 square meters.
  • the density of the conductive covering is 5 g/sq. meter.
  • each of the anodes is welded with titanium to three supports 12 and is disposed vertically similarly to the cathodes.
  • the anodes 11 are offset relative to the cathodes 7, as illustrated in FIG. 4, in order that within each cell the anodes and cathodes are interleaved.
  • the supports 12 are mounted on the flexible membrane 13 by means of nuts 14 which compress collars l5 and are threaded on threads of the respective supports 12.
  • the leakage of electrolyte is prevented by an annular seal 16 made of hypalon or another synthetic elastomer received in a groove 17.
  • a blind bore is provided in each support 12 and a copper stud 18 is received therein.
  • the studs extend through the anodic supporting plate 9 and are held in position by steel nuts 10 and steel washers l9 and press the supports 12 against the support plate 9.
  • the nuts 10, washers l9 and the threaded nut 14 on the circular supports 12 and the seal 15 are mounted externally of the cells and, therefore, are not subject to the corrosion that would take place if they were mounted internally thereof as in the usual manner.
  • the flexible membrane or sheet 13 has its peripheral or v marginal portions fixed between a rigid frame 20 and a flange 5 of the cell to which the frame and membrane are bolted.
  • the fluid tightness between the flange 5 and the flexible membrane 13 and between the rigid support plate 6 and its cell tank is insured by flexible seals 21, 21'.
  • the electrode assembly for compensating thermal expansion may be provided with only one set of the electrodes, for example, the anodes.
  • the flexible membrane can be made of a synthetic polymer sheet such as polytetrafluorethylene sheets. These sheets must be supported in order to resist the fluid pressure and can be provided with an external support such as a metallic grid, not shown.
  • a rigid supply conductor 22 and a rigid output conductor 22' are provided. These are secured to the endmost cells and electrically connected thereto to provide current to the anodes and cathodes of the cells which are electrically in series, as illustrated, since the electrode assembly members are electrically conductive.
  • the spacing between the two electrode support plates 6, 9 is such that the access to the anode mount members is readily provided.
  • the anode plates may be quickly removed individually to repair them, for example, to repair their active surfaces. There is no need to stop the electrolysis of the overall arrangement of cells and, therefore, downtime is avoided. The electrolysis can be continued by simply shortcircuiting the individual cell being worked on.
  • a bipolar electrode for compensating for thermal expansion of separate electrolytic cells interconnected in electrical series with interfoliated flat metal anode members and flat cathode members comprising a flexible impervious sheet defining in use a removable external sidewall of a separate electrolytic cell, a rigid conductive support spaced from in opposed relationship to said flexible impervious sheet mountable on another separate electrolytic cell next adjacent to the firstmentioned cell defining a removable external sidewall thereof, a set of parallel flat electrode members defining in use the cathode assembly of the last-mentioned cell and conductively mounted on one side of and perpendicularly to said support, a set of parallel flat metal members defining in use an anode assembly of the first-mentioned cell and removably mounted on the other side of and perpendicularly to said support, and conductive means fluid-tightly extending through said flexible impervious sheet mounting said anode assembly on said support.
  • a bipolar electrode assembly according. to claim I wherein said rigid conductive support comprises two parallel metal support plates conductively joined, metal spacers joining said two metal plates, one of these metal plates disposed supporting said parallel flat electrode members, the other metal plate removably supporting said anode assembly.
  • a bipolar electrode assembly according to claim I wherein anode assembly consists of activated titanium plates and said conductive means consist of titanium plugs secured to said titanium plates on the edge thereof, and means to insure fluid tightness with said flexible impervious sheet secured to said rigid conductive support.

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 Non-Metals, Compounds, Apparatuses Therefor (AREA)
US878705A 1968-11-22 1969-11-21 Electrode assembly for compensating thermal expansion in an electrolytic cell Expired - Lifetime US3658686A (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
BE66463 1968-11-22
US87870569A 1969-11-21 1969-11-21

Publications (1)

Publication Number Publication Date
US3658686A true US3658686A (en) 1972-04-25

Family

ID=25647441

Family Applications (1)

Application Number Title Priority Date Filing Date
US878705A Expired - Lifetime US3658686A (en) 1968-11-22 1969-11-21 Electrode assembly for compensating thermal expansion in an electrolytic cell

Country Status (4)

Country Link
US (1) US3658686A (hu)
BE (1) BE724302A (hu)
FR (1) FR2023877A1 (hu)
NL (1) NL164096C (hu)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3970539A (en) * 1974-12-23 1976-07-20 Basf Wyandotte Corporation End connector for filter press cell
US3983026A (en) * 1973-10-19 1976-09-28 Solvay & Cie Electrolytic cells with vertical electrodes

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
IT947905B (it) * 1971-03-02 1973-05-30 Krebs & Co Ag Impianto per elettrolisi provvisto di camere delle celle prive di dia frammi che sono percorse dall elet trolitio

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CA575665A (en) * 1959-05-12 L. Lucas Jessie Diaphragm type electrolytic cell
US3119759A (en) * 1961-03-20 1964-01-28 Applied Science Lab Inc Rotating electrolytic cell assembly

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CA575665A (en) * 1959-05-12 L. Lucas Jessie Diaphragm type electrolytic cell
US3119759A (en) * 1961-03-20 1964-01-28 Applied Science Lab Inc Rotating electrolytic cell assembly

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3983026A (en) * 1973-10-19 1976-09-28 Solvay & Cie Electrolytic cells with vertical electrodes
US3970539A (en) * 1974-12-23 1976-07-20 Basf Wyandotte Corporation End connector for filter press cell

Also Published As

Publication number Publication date
NL164096B (nl) 1980-06-16
NL6917375A (hu) 1970-05-26
NL164096C (nl) 1980-11-17
FR2023877A1 (hu) 1970-08-21
BE724302A (hu) 1969-05-22

Similar Documents

Publication Publication Date Title
JP5627600B2 (ja) 電解プロセス用の基本セルおよび関連するモジュール型電解装置
US3836448A (en) Frames for electrolytic cells of the filter-press type
US4309264A (en) Electrolysis apparatus
CA1060842A (en) Electrolytic cell
US3700582A (en) Electrolytic cell
US3658686A (en) Electrode assembly for compensating thermal expansion in an electrolytic cell
US9797051B2 (en) Method of retrofitting of finite-gap electrolytic cells
US3719578A (en) Electrolysis cell with anode support means
CA1090736A (en) An electrolysis cell having monopolar electrodes
US3318792A (en) Mercury cathode cell with noble metaltitanium anode as cover means
FI67575B (fi) Elektrolysapparat foer framstaellning av klor ur vattenhaltigaalkalihalogenidvattenloesningar
US4064031A (en) Electrolyzer
FI57275C (fi) Elektrolytisk cell
US3832300A (en) Bipolar diaphragm electrolyzer with cathode waves in horizontal plane
CA1036978A (en) Bipolar electrolytic cell
GB1591123A (en) Plate heat exchangers
US1535185A (en) Electrolytic apparatus
US3945909A (en) Bipolar electrodes and electrolytic cell therewith
FI56858C (fi) Tvaopolig elektrodkombination
GB1345254A (en) Electrolytic cell
US3981788A (en) Caustic alkali producing multiple vertical diaphragm type electrolytic cell admitting of easy assembly
FI77270C (fi) Monopolaer, bipolaer och/eller hybrid membrancell.
US4056459A (en) Anode assembly for an electrolytic cell
FI63443B (fi) Elektrolyscell
KR800000528B1 (ko) 복극식 전해조