US3923630A - Electrolytic cell including diaphragm and diaphragm-support structure - Google Patents

Electrolytic cell including diaphragm and diaphragm-support structure Download PDF

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Publication number
US3923630A
US3923630A US497864A US49786474A US3923630A US 3923630 A US3923630 A US 3923630A US 497864 A US497864 A US 497864A US 49786474 A US49786474 A US 49786474A US 3923630 A US3923630 A US 3923630A
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United States
Prior art keywords
diaphragm
support
electrolytic cell
cell
cathode
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
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US497864A
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English (en)
Inventor
Shyam D Argade
Stephen M Collins
James B Armitage
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BASF Corp
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BASF Wyandotte Corp
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Publication date
Application filed by BASF Wyandotte Corp filed Critical BASF Wyandotte Corp
Priority to US497864A priority Critical patent/US3923630A/en
Priority to IT50952/75A priority patent/IT1041242B/it
Priority to CA233,470A priority patent/CA1058559A/fr
Priority to FR7525352A priority patent/FR2281999A1/fr
Priority to NL7509777A priority patent/NL7509777A/xx
Priority to JP50098652A priority patent/JPS5145697A/ja
Priority to GB34015/75A priority patent/GB1516196A/en
Application granted granted Critical
Publication of US3923630A publication Critical patent/US3923630A/en
Assigned to BASF CORPORATION reassignment BASF CORPORATION MERGER (SEE DOCUMENT FOR DETAILS). Assignors: BADISCHE CORPORATION, BASF SYSTEMS CORPORATION, BASF WYANDOTTE CORPORATION, A MI CORP., GLASURIT AMERICA, INC., (MERGED INTO), INMONT CORPORATION, (CHANGED TO), LIMBACHER PAINT & COLOR WORKS, INC
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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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
    • C25B9/17Cells comprising dimensionally-stable non-movable electrodes; Assemblies of constructional parts thereof
    • C25B9/19Cells comprising dimensionally-stable non-movable electrodes; Assemblies of constructional parts thereof with diaphragms
    • CCHEMISTRY; METALLURGY
    • C25ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25BELECTROLYTIC OR ELECTROPHORETIC PROCESSES FOR THE PRODUCTION OF COMPOUNDS OR NON-METALS; APPARATUS THEREFOR
    • C25B13/00Diaphragms; Spacing elements
    • C25B13/02Diaphragms; Spacing elements characterised by shape or form

Definitions

  • references C'ted aphragm can be made from polymeric material with 21 UNITED STATES PATENTS fluorocarbon polymer being illustrative of a suitable 1,963,959 6/1934 Enzor 204/258 m ri l- 3,312,614 4/1967 Schick 204/266 3,344,053 9/1967 Neipert 204/266 8 Clam, 4 Drawmg Flgures I I I I- a I r I I I I I I I I I I r S I i r I I I I I z I I I.
  • the asbestos slurry-type diaphragm has an important advantage in the cells inasmuch as the diaphragm conforms to the convoluted contours of the cathode and presents no attachment problems.
  • the cathode fingers are particularly fabricated from wire screen mesh so that the asbestos diaphragms can be deposited on the cathode from the asbestos slurry.
  • the use of other types of asbestos such as asbestos paper wrapped over the finger-type cathode and sealed at the top and bottom with cement and putty provide a poor seal and loss of current efficiency.
  • a diaphragm-type cell for the production of chlorine and caustic from aqueous alkali metal chloride solutions having a plurality of anodes mounted at the bottom of said cell, a cathode between adjacent anodes and spaced between each cathode and anode a diaphragm which divides the cell into anolyte and catholyte compartments the improvement which comprises:
  • a diaphragm assembly composed of an upper diaphragm support, a lower diaphragm support and a continuous diaphragm extending from said upper support to said lower support, both said diaphragm,
  • FIG. 1 is a side sectional view of a conventional diaphragm electrolytic cell showing the present invention installed therein.
  • FIG. 2 is a top cross-sectional view of the electrolytic cell taken along line 2-2 of FIG. 1.
  • FIG. 3 is an expanded schematic drawing showing the elements of the invention and their relationship to the conventional diaphragm electrolytic cell.
  • FIG. 4 is a side cross-sectional view of the conventional diaphragm electrolytic cell wherein an optional modification of the invention has been installed.
  • the present invention is installed in a typical electrolytic diaphragm cell having cell bottom and bus bar means 10 which is coated a nonconductive sealant layer 12 and through which sealant layer 12 protrudes a series of spaced anode metal stems 40 for connecting anodes 24 with bus bar means 10.
  • the stem 40 is secured to the bus bar means 10 by use of nut 42.
  • the cell is completed with the installation of cell sides 16 and cell top 14 along with weak cell liquor outlet 18, hydrogen outlet 20 and chlorine outlet 22, the exact positioning of the foregoing outlets being a matter of choice.
  • the porous cathode 26 is typically made of a ferrous metal with a woven wire construction although other means of fabricating can be employed.
  • the cathode 26 is so formed that it will be one continuous piece but containing a series of openings or passageways through which the anodes 24 can pass and most of the surface of cathode 26 will be parallel to the anodes 24.
  • the cathode 26/diaphragm 36 assembly can be prepared prior to insertion of diaphragm 36 into the cell.
  • each of the continuous sheet or endless belt diaphragm 36 to the lower diaphragm support 30, then lowering the cathode 26 down onto the lower diaphragm support 30 so that the diaphragm 36 extends upwardly through the passageways previously provided for the anode 24 and, thereafter, applying the upper diaphragm support 32 to the other edge of the endless band diaphragm 36.
  • This assembly is then set into the cell so that the anode 24 extends through the passageways made by the diaphragm 36 which parallels the passageways of the cathode 26.
  • the cathode 26 and lower diaphragm support 30 are then placed in mechanical and electrical attachment with the cell so that proper position of the cathode 26 and diaphragm 36 will be maintained.
  • Gas seals (not shown) between sidewall 16 and lower diaphragm support 30 and between sidewall 16 and upper diaphragm support 32 complete the separation between the cathode and anode chambers.
  • FIG. 3' The invention is illustrated schematically in FIG. 3'
  • the expanded drawing shows an anode 24 embedded in cell bottom and extending through the nonconductive sealant layer 12.
  • the lower diaphragm support 30 contains slots or openings which accommodate the insertion of anode 24.
  • the cathode 26 is of woven wire-mesh construction and is so woven that it has openings shaped corresponding to the openings or slots in the lower diaphragm support 30 but of a slightly larger nature thereby accommodating the endless belt diaphragm 36 which is attached to the lower diaphragm support 30 and the upper diaphragm support 32 which has the same configuration as the lower diaphragm support 30.
  • the lower diaphragm support 30 and the upper diaphragm support 32 are constructed of a chemically inert, electrically non-conducting thermoplastic material such as polyolefin derived form an olefin containing 2 to 4 carbon atoms including polyethylene, polypropylene, polybutene-l and mixtures thereof; polytetrafluoroethylene, copolymers of tetrafluoroethylene and polyperfluoroalkoxy compounds, chlorofluoropolyethylene, polyvinylidene fluoride polymers and acrylonitrile butadiene styrene terpolymers.
  • a chemically inert, electrically non-conducting thermoplastic material such as polyolefin derived form an olefin containing 2 to 4 carbon atoms including polyethylene, polypropylene, polybutene-l and mixtures thereof; polytetrafluoroethylene, copolymers of tetrafluoroethylene and polyperfluoroal
  • the properties of these polymers are improved by adding inert, non-conducting yet reinforcing fillers such as asbestos, glass fibers, mica, kaolin or carbon black.
  • An exemplary composition for use in this invention is an asbestos filled polypropylene composition, e.g., as disclosed in British Patent 1,246,034, which for the sake of brevity is incorporated herein by reference.
  • Another equally suitable material is a polytetrafluoroethylene polymer or copolymer.
  • the upper diaphragm support 32 and the lower diaphragm support 30 are made from the foregoing polymeric materials in such a manner that the support members 30, 32 are both electrically non-conducting and are incapable of permitting the flow of electrolyte from one chamber to the other chamber. It is also within the scope of this invention to make the support frames 30, 32 out of a suitable metal or wire which is completely covered and encased with an insulating polymeric material disclosed above.
  • the endless belt diaphragm 36 can be made out of the same polymeric material as the diaphragm support members 30, 32 are made out of or it can be one of the other suitable polymeric materials, e.g., those enumerated above.
  • the endless belt diaphragm 36 is so fabricated with appropriate physical, chemical and electrochemical properties that it is porous and will permit the flow of electrolyte from one chamber to the other chamber.
  • the endless belt diaphragm 36 is attached to the diaphragm supports 30, 32 in any one of several conventional techniques used in fabricating polymeric objects such as heat-sealing, cementing or friction fit snap-in techniques.
  • the diaphragm 36 can be heat-sealed to the lower or bottom support 30 and mechanically, i.e., friction fitted, to the upper diaphragm support 32.
  • the fabricated diaphragm 36 may properly be classified as a porous membrane, or a felted fabric such as are presently employed in the various phases of electrolytic cell technology. It is also known in the cell technology to insert between diaphragm 36 and the electrodes, either or both anode 24 and cathode 26, an inert screen (not shown) to facilitate and improve the functioning of the cell. This modification can be used in conjunction with the present invention, if desired.
  • the anode 24 can be either a solid metal sheet, a woven wire arrangement or an expanded metal mesh as desired, the exact configuration of the anode 24 being beyond the scope of the present invention.
  • the anode 24 is made of a valve metal and, thereafter, coated.
  • a valve metal it is meant metal of tungsten, titanium, zirconium, tantalum and niobium.
  • titanium or tantalum is employed and it is normally a commercially pure grade such as electrolytic grade. Alloys of valve metals can be employed as long as the alloy meets the criterion of passivity, metal alloys which become passivated when polarized anodically and can remain passive well beyond anodic potential needed to convert a chloride ion to chlorine.
  • platinum group metal or metal compound e.g., oxide
  • the platinum group metals include platinum, ruthenium, osmium, rhodium, iridium and palladium and alloys of two or more of the foregoing metals.
  • Many means for applying and the formulations of platinum group metals and compounds for these coatings are known, for instance, see US. Pat. Nos. 3,632,498; 3,630,768; 3,616,446; 3,242,059; and 3,177,131 which for the sake of simplicity and brevity are herein incorporated by reference.
  • FIG. 4 shows an optical modification of the present invention which is designed to secure the benefits of the present invention to the diaphragm cell equipped with the conventional Hooker woven wire cathode employed therein.
  • the Hooker woven wire type cathode is well known in the art and generally disclosed in the Sconce textbook discussed above in the background section.
  • the cell bottom and bus bar 10 the nonconductive sealant layer 12 and anodes 24 with metal stem 40 and retaining nut 42 remain positioned without change as shown in FIG. 1.
  • the continuous sheet or endless belt diaphragm 36, the lower diaphragm support 30 and upper diaphragm support 32 are rearranged so that they form a series of equal distance-spaced closed openings on both sides. This is accomplished by attaching the endless belt diaphragm 36 to the anode 24 openings of the lower diaphragm support 30 as previously disclosed.
  • the upper diaphragm support 32 is now realigned so that the prior axial alignment of the openings in the lower diaphragm support 30 and the openings in the upper diaphragm support 32 are completely out of register. From a top view the openings in the upper support 32 are now spaced equidistant from each two adjacent openings in the lower support 30.
  • the cathode 26 is not encased by the diaphragm 36 and diaphragm supports 30, 32 and can be disengaged from the diaphragm 36 without disassembly of the diaphragm 36 diaphragm supports 32, 30 arrangement.
  • the conventional diaphragm electrolytic cell can be used as is without modification of the location of the chlorine outlet 22.
  • Gas seal (not shown) between sidewall 16 and lower diaphragm support 30 completes the separation between the cathode and anode chambers.
  • a diaphragm cell for the production of chlorine and caustic from aqueous alkali metal chloride solutions having a plurality of anodes mounted at the bottom of said cell, cathodes between adjacent anodes and spaced between each cathode and anode a diaphragm which divides the cell into anolyte and catholyte compartments the improvement which comprises:
  • a diaphragm assembly composed of an upper diaphragm support, a lower diaphragm support and an endless band diaphragm extending from said upper support to said lower support, both said diaphragm supports being made of an electrically nonconductive polymeric composition, said lower support resting on or adjacent to the bottom of said cell and having openings therein which allow said anodes to extend through said lower support, said diaphragm being in connection with said upper and lower supports thereby defining a continuous barrier separating said anodes from said cathodes so that all of the flow of electrolyte from the anode to the cathode is through said diaphragm.
  • separating screens are interposed between the diaphragm and'th'e anode and the cathode.

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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 Non-Metals, Compounds, Apparatuses Therefor (AREA)
  • Hybrid Cells (AREA)
US497864A 1974-08-16 1974-08-16 Electrolytic cell including diaphragm and diaphragm-support structure Expired - Lifetime US3923630A (en)

Priority Applications (7)

Application Number Priority Date Filing Date Title
US497864A US3923630A (en) 1974-08-16 1974-08-16 Electrolytic cell including diaphragm and diaphragm-support structure
IT50952/75A IT1041242B (it) 1974-08-16 1975-08-13 Perfezionamento nelle celle elettro litiche in particolare nei diaframmi catodici
FR7525352A FR2281999A1 (fr) 1974-08-16 1975-08-14 Membranes en feuille continue pour cathodes electrolytiques de forme convolutee
CA233,470A CA1058559A (fr) 1974-08-16 1975-08-14 Diaphragmes en rideau pour electrodes de forme complexe
NL7509777A NL7509777A (nl) 1974-08-16 1975-08-15 Elektrolytische diafragmacel.
JP50098652A JPS5145697A (fr) 1974-08-16 1975-08-15
GB34015/75A GB1516196A (en) 1974-08-16 1975-08-15 Electrode assemblies and electrolytic cells containing them

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US497864A US3923630A (en) 1974-08-16 1974-08-16 Electrolytic cell including diaphragm and diaphragm-support structure

Publications (1)

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US3923630A true US3923630A (en) 1975-12-02

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US497864A Expired - Lifetime US3923630A (en) 1974-08-16 1974-08-16 Electrolytic cell including diaphragm and diaphragm-support structure

Country Status (7)

Country Link
US (1) US3923630A (fr)
JP (1) JPS5145697A (fr)
CA (1) CA1058559A (fr)
FR (1) FR2281999A1 (fr)
GB (1) GB1516196A (fr)
IT (1) IT1041242B (fr)
NL (1) NL7509777A (fr)

Cited By (34)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4036728A (en) * 1976-05-21 1977-07-19 Diamond Shamrock Corporation Converting a diaphragm electrolytic cell to a membrane electrolytic cell
US4081350A (en) * 1976-10-29 1978-03-28 Olin Corporation Diaphragms for use in the electrolysis of alkali metal chlorides
US4115237A (en) * 1977-01-03 1978-09-19 Olin Corporation Electrolytic cell having membrane enclosed anodes
FR2387298A1 (fr) * 1977-04-13 1978-11-10 Ici Ltd Cellule d'electrolyse a diaphragme
US4136004A (en) * 1975-07-15 1979-01-23 Kamarian Georgy M Solid electrode electrolyzer for electrolysis of aqueous solutions
US4153530A (en) * 1977-04-13 1979-05-08 Imperial Chemical Industries Limited Diaphragm cells
DE2855837A1 (de) * 1977-12-26 1979-07-12 Kanegafuchi Chemical Ind Verfahren und vorrichtung zum einbau einer membran in eine elektrolysezelle
JPS54100952U (fr) * 1977-12-26 1979-07-16
US4165271A (en) * 1977-10-03 1979-08-21 Olin Corporation Diaphragms for use in the electrolysis of alkali metal chlorides
US4166785A (en) * 1976-10-29 1979-09-04 Olin Corporation Diaphragms for use in the electrolysis of alkali metal chlorides
US4167469A (en) * 1976-10-29 1979-09-11 Olin Corporation Diaphragms for use in the electrolysis of alkali metal chlorides
DE2932197A1 (de) * 1978-08-10 1980-02-21 Kanegafuchi Chemical Ind Verfahren und vorrichtung zum einbau einer membran in eine elektrolysezelle
US4207164A (en) * 1977-10-03 1980-06-10 Olin Corporation Diaphragms for use in the electrolysis of alkali metal chlorides
US4236952A (en) * 1977-12-29 1980-12-02 Imperial Chemical Industries Limited Production of sheet materials
FR2464312A1 (fr) * 1979-08-30 1981-03-06 Olin Corp Structure de diaphragme en forme de gant pour cellule d'electrolyse
DE3034760A1 (de) * 1979-09-14 1981-04-02 Hooker Chemicals & Plastics Corp., 14302 Niagara Falls, N.Y. Scheidewand fuer elektrolysezellen und verfahren zu deren herstellung
US4268372A (en) * 1978-08-03 1981-05-19 Kanegafuchi Kagaku Kogyo Kabushiki Kaisha Method and apparatus for installing a membrane to an electrolytic cell
US4278524A (en) * 1977-09-26 1981-07-14 Olin Corporation Diaphragms for use in the electrolysis of alkali metal chlorides
US4278523A (en) * 1978-07-28 1981-07-14 Imperial Chemical Industries Limited Clamping diaphragms or membranes in electrolytic cells
US4288310A (en) * 1979-09-12 1981-09-08 Knight Allan R Membrane support assembly for electrolytic cell and method of making same
US4289601A (en) * 1979-11-30 1981-09-15 Olin Corporation Diaphragm structure for electrolytic cells for the electrolysis of aqueous salt solutions
US4361475A (en) * 1980-01-10 1982-11-30 Innova, Inc. Membrane block construction and electrochemical cell
EP0069940A2 (fr) * 1981-07-14 1983-01-19 Asahi Glass Company Ltd. Cellule d'électrolyse
US4395321A (en) * 1980-07-17 1983-07-26 Kanegafuchi Kagaku Kogyo Kabushiki Kaisha Separator electrolytic cell
US4402813A (en) * 1982-07-26 1983-09-06 Olin Corporation Composite fiber reinforced plastic electrode frame
US4432857A (en) * 1981-03-10 1984-02-21 Imperial Chemical Industries Plc Cladding cathodes of electrolytic cell with diaphragm or membrane
US4439298A (en) * 1982-07-26 1984-03-27 Olin Corporation Composite fiber reinforced plastic frame
US4500379A (en) * 1982-07-26 1985-02-19 Olin Corporation Method of making a composite fiber reinforced plastic frame
US4622113A (en) * 1983-11-17 1986-11-11 Toyo Soda Manufacturing Co., Ltd. Process for producing caustic alkalis
US6361665B1 (en) * 1989-06-13 2002-03-26 Pavel Voracek Device for electroactivating fluids and preparations consisting of electroactivated fluids
DE102007041828A1 (de) * 2007-09-03 2009-03-05 Siemens Ag Vorrichtung und Verfahren zum Abbau von Schadstoffen in einer Flüssigkeit sowie Verwendung einer solchen Vorrichtung
WO2011015556A1 (fr) 2009-08-04 2011-02-10 Siemens Aktiengesellschaft Procédé pour la décomposition de produits nocifs organiques dans des eaux usées industrielles et installation spécifique
WO2017173149A1 (fr) * 2016-03-30 2017-10-05 Alcoa Usa Corp. Appareils et systèmes pour cellules d'électrolyse verticales
CN113373495A (zh) * 2021-05-27 2021-09-10 东莞市琢器机械设备科技有限公司 感应式纳米隔膜

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
ATE5333T1 (de) * 1979-07-20 1983-12-15 Imperial Chemical Industries Plc Diaphragma zum umhuellen einer kathodenkammer einer elektrolytischen zelle, folie zur herstellung eines diaphragmas und verfahren zum umhuellen einer kathodenkammer.
DE3172133D1 (en) * 1981-06-23 1985-10-10 Dow Chemical Co Membrane support assembly for electrolytic cell and method of making same

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US1963959A (en) * 1933-01-23 1934-06-26 Howard E Dorsey Electrolytic gas producing device
US3312614A (en) * 1967-04-04 Diaphragm electrolysis cell
US3344053A (en) * 1964-05-04 1967-09-26 Dow Chemical Co Chlorine cell
US3398080A (en) * 1965-03-22 1968-08-20 Dow Chemical Co Mercury vertical cathode electrolytic cell
US3408281A (en) * 1965-07-15 1968-10-29 Dow Chemical Co Vertical mercury cathode electrolytic cell with diaphragm enclosed perforated cathode support

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3312614A (en) * 1967-04-04 Diaphragm electrolysis cell
US1963959A (en) * 1933-01-23 1934-06-26 Howard E Dorsey Electrolytic gas producing device
US3344053A (en) * 1964-05-04 1967-09-26 Dow Chemical Co Chlorine cell
US3398080A (en) * 1965-03-22 1968-08-20 Dow Chemical Co Mercury vertical cathode electrolytic cell
US3408281A (en) * 1965-07-15 1968-10-29 Dow Chemical Co Vertical mercury cathode electrolytic cell with diaphragm enclosed perforated cathode support

Cited By (47)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4136004A (en) * 1975-07-15 1979-01-23 Kamarian Georgy M Solid electrode electrolyzer for electrolysis of aqueous solutions
US4112149A (en) * 1976-05-21 1978-09-05 Diamond Shamrock Corporation Converting a diaphragm electrolytic cell to a membrane electrolytic cell
US4036728A (en) * 1976-05-21 1977-07-19 Diamond Shamrock Corporation Converting a diaphragm electrolytic cell to a membrane electrolytic cell
US4166785A (en) * 1976-10-29 1979-09-04 Olin Corporation Diaphragms for use in the electrolysis of alkali metal chlorides
US4081350A (en) * 1976-10-29 1978-03-28 Olin Corporation Diaphragms for use in the electrolysis of alkali metal chlorides
US4167469A (en) * 1976-10-29 1979-09-11 Olin Corporation Diaphragms for use in the electrolysis of alkali metal chlorides
US4115237A (en) * 1977-01-03 1978-09-19 Olin Corporation Electrolytic cell having membrane enclosed anodes
FR2387298A1 (fr) * 1977-04-13 1978-11-10 Ici Ltd Cellule d'electrolyse a diaphragme
US4156639A (en) * 1977-04-13 1979-05-29 Imperial Chemical Industries, Limited Diaphragm cells
US4153530A (en) * 1977-04-13 1979-05-08 Imperial Chemical Industries Limited Diaphragm cells
US4278524A (en) * 1977-09-26 1981-07-14 Olin Corporation Diaphragms for use in the electrolysis of alkali metal chlorides
US4165271A (en) * 1977-10-03 1979-08-21 Olin Corporation Diaphragms for use in the electrolysis of alkali metal chlorides
US4207164A (en) * 1977-10-03 1980-06-10 Olin Corporation Diaphragms for use in the electrolysis of alkali metal chlorides
DE2855837A1 (de) * 1977-12-26 1979-07-12 Kanegafuchi Chemical Ind Verfahren und vorrichtung zum einbau einer membran in eine elektrolysezelle
JPS54100952U (fr) * 1977-12-26 1979-07-16
US4521289A (en) * 1977-12-26 1985-06-04 Kanegafuchi Kagaku Kogyo Kabushiki Kaisha Method and apparatus for installation of a membrane to an electrolytic cell
JPS5812836Y2 (ja) * 1977-12-26 1983-03-11 鐘淵化学工業株式会社 塩化アルカリ電解槽用膜取付け装置
US4268373A (en) * 1977-12-26 1981-05-19 Kanegafuchi Kagaku Kogyo Kabushiki Kaisha Method and apparatus for installation of a membrane to an electrolytic cell
US4236952A (en) * 1977-12-29 1980-12-02 Imperial Chemical Industries Limited Production of sheet materials
US4278523A (en) * 1978-07-28 1981-07-14 Imperial Chemical Industries Limited Clamping diaphragms or membranes in electrolytic cells
US4268372A (en) * 1978-08-03 1981-05-19 Kanegafuchi Kagaku Kogyo Kabushiki Kaisha Method and apparatus for installing a membrane to an electrolytic cell
DE2932197A1 (de) * 1978-08-10 1980-02-21 Kanegafuchi Chemical Ind Verfahren und vorrichtung zum einbau einer membran in eine elektrolysezelle
FR2433059A1 (fr) * 1978-08-10 1980-03-07 Kanegafuchi Chemical Ind Procede et appareil pour la pose d'une membrane sur une cellule electrolytique destinee a l'electrolyse d'une solution aqueuse de chlorure de metal alcalin
FR2464312A1 (fr) * 1979-08-30 1981-03-06 Olin Corp Structure de diaphragme en forme de gant pour cellule d'electrolyse
US4288310A (en) * 1979-09-12 1981-09-08 Knight Allan R Membrane support assembly for electrolytic cell and method of making same
DE3034760A1 (de) * 1979-09-14 1981-04-02 Hooker Chemicals & Plastics Corp., 14302 Niagara Falls, N.Y. Scheidewand fuer elektrolysezellen und verfahren zu deren herstellung
US4283264A (en) * 1979-09-14 1981-08-11 Hooker Chemicals & Plastics Corp. Electrolytic cell separator, tubular member component thereof and methods for manufacturing and using such separator and component
US4289601A (en) * 1979-11-30 1981-09-15 Olin Corporation Diaphragm structure for electrolytic cells for the electrolysis of aqueous salt solutions
US4361475A (en) * 1980-01-10 1982-11-30 Innova, Inc. Membrane block construction and electrochemical cell
US4395321A (en) * 1980-07-17 1983-07-26 Kanegafuchi Kagaku Kogyo Kabushiki Kaisha Separator electrolytic cell
US4432857A (en) * 1981-03-10 1984-02-21 Imperial Chemical Industries Plc Cladding cathodes of electrolytic cell with diaphragm or membrane
EP0069940A3 (en) * 1981-07-14 1983-02-16 Asahi Glass Company Ltd. Electrolytic cell
EP0069940A2 (fr) * 1981-07-14 1983-01-19 Asahi Glass Company Ltd. Cellule d'électrolyse
US4537673A (en) * 1981-07-14 1985-08-27 Asahi Glass Company Ltd. Electrolytic cell
US4402813A (en) * 1982-07-26 1983-09-06 Olin Corporation Composite fiber reinforced plastic electrode frame
US4439298A (en) * 1982-07-26 1984-03-27 Olin Corporation Composite fiber reinforced plastic frame
US4500379A (en) * 1982-07-26 1985-02-19 Olin Corporation Method of making a composite fiber reinforced plastic frame
US4622113A (en) * 1983-11-17 1986-11-11 Toyo Soda Manufacturing Co., Ltd. Process for producing caustic alkalis
US6361665B1 (en) * 1989-06-13 2002-03-26 Pavel Voracek Device for electroactivating fluids and preparations consisting of electroactivated fluids
DE102007041828A1 (de) * 2007-09-03 2009-03-05 Siemens Ag Vorrichtung und Verfahren zum Abbau von Schadstoffen in einer Flüssigkeit sowie Verwendung einer solchen Vorrichtung
US20110017610A1 (en) * 2007-09-03 2011-01-27 Alexander Hahn Device and process for breaking down pollutants in a liquid and also use of such a device
WO2011015556A1 (fr) 2009-08-04 2011-02-10 Siemens Aktiengesellschaft Procédé pour la décomposition de produits nocifs organiques dans des eaux usées industrielles et installation spécifique
DE102009036080A1 (de) 2009-08-04 2011-02-17 Siemens Aktiengesellschaft Verfahren zum Abbau von organischen Schadstoffen in industriellem Abwasser und zugehörige Anlage
WO2017173149A1 (fr) * 2016-03-30 2017-10-05 Alcoa Usa Corp. Appareils et systèmes pour cellules d'électrolyse verticales
CN109312484A (zh) * 2016-03-30 2019-02-05 美铝美国公司 用于垂直电解池的装置和系统
CN109312484B (zh) * 2016-03-30 2022-02-11 美铝美国公司 用于垂直电解池的装置和系统
CN113373495A (zh) * 2021-05-27 2021-09-10 东莞市琢器机械设备科技有限公司 感应式纳米隔膜

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IT1041242B (it) 1980-01-10
GB1516196A (en) 1978-06-28
FR2281999A1 (fr) 1976-03-12
NL7509777A (nl) 1976-02-18
JPS5145697A (fr) 1976-04-19

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